NUREG/IA-0099

International

Agreement Report

RELAP5 Assessment Using

Semiscale SBLOCA Test S-NH-i

Prepared by

Euy-Joon Lee, Bub-Dong Chung, Hho-Jung Kim

Safety Analysis Departmen t

Korea Institute of Nuclear Safety

P.O. Box 16, Daeduk Danji

Taejon, Korea

Office of Nuclear Regulatory Research

U.S. Nuclear Regulatory Commission

Washington, DC 20555

June 1993

Prepared as part of

The Agreement on Research Participation and Technical Exchange

under the International Thermal-Hydraulic Code Assessment

and Application Program (ICAP)

Published by

U.S. Nuclear Regulatory Commission
NOTICE

This report was prepared under an international cooperative

agreement for the exchange of technical information. Neither

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their employees, makes any warranty, expressed or implied, or

assumes any legal liability or responsibility for any third party's

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by such third party would not infringe privately owned rights.

Available from

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U.S. Government Printing Office

P.O. Box 37082

Washington, D.C. 20013-7082

and

National Technical Information Service

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NUREG/IA-0099

International

Agreement Report

RBLAP5 Assessment Using

Semiscale SBLOCA Test S-NH-i

Prepared by

Euy-Joon Lee, Bub-Dong Chung, Hho-Jung Kim

Safety Analysis Department

Korea Institute of Nuclear Safety

P.O. Box 16, Daeduk Danji

Taejon, Korea

Office of Nuclear Regulatory Research

U.S. Nuclear Regulatory Commission

Washington, DC 20555

June 1993

Prepared as part of

The Agreement on Research Participation and Technical Exchange under the International Thermal-Hydraulic Code Assesment

and Application Program (ICAP)

Published by

U.S. Nuclear Regulatory Commission
NOTICE

This report is based on work performed under the sponsorship of The Korea

Advanced Energy Institute of Korea. The information in this report has been

provided to the USNRG under the terms of an information exchange agreement

between the United States and Korea (Agreement on Thermal-Hydraulic Research

between the United States Nuclear Regulatory Comimission and The Korea Advanced

Energy Research Institute, May 1, 1986). Korea has consented to the publication

of this report as a USNRC document in order that it may receive the widest

possible circulation among the reactor safety community. Neither the United

States Government nor Korea or any agency thereof, or any of their employees,

makes any warranty, expressed or implied, or assumes any legal liability of

responsibility for any third party's use, or the results of such use, or any

information, apparatus, product or process disclosed in this report or

represents that its use by such third party would not infringe privately

owned rights.
RELAP5 ASSESSMENT USING SENISCALE SBLOCA TEST S-NH-i

Abstract

2-inch cold leg break test S-NH-i, conducted at the 1/1705 volume

scaled facility Semiscale, was analyzed using RELAP5/MOD2 Cycle 36.04 and

110D3 Version 5m5. Loss of HPIS was assumed, and reactor trip occurred on

a low PZR pressure signal (13.1 MPa), and pumps began an unpowered

coastdown on SI signal (12.5 KPa). The system was recovered by opening

ADV's when the PCT became higher than 811 K. Accumulator was finally

injected into the system when the primary system pressure was less than

4.0 NPa. The experiment was terminated when the pressure reached the

LPIS actuation set point.

RELPAP5/N0D2 analysis demonstrated its capability to predict, with a

sufficient accuracy, the main phenomena occurring in the depressurization

transient, both from a qualitative and quantitative points of view.

Nevertheless, several differences were noted regarding the break flow

rate and inventory distribution due to deficiencies in two-phase choked

flow model, horizontal stratification interfacial drag, and a CCFL model.

The main reason for the core to remain nearly fully covered with the

liquid was the under-prediction of the break flow by the code.

Several sensitivity calculations were tried using the MOD2 to

improve the results by using the different options of break flow

modeling(downward, homogeneous, and area increase). The break area

compensating concept based on "the integrated break flow matching" gave

the best results than downward junction and homogeneous options. And the

110D3 showed improvement in predicting a CCEL in SG and a heatup in the

core.

Executive Summary

The Semiscale SBLOCA test S-NH-i has been analyzed using the

RELAP5/1'1D2 Cycle 36.04 and 110D3 Version 5m5 to validate its

applicability to 0.5 % cold leg break sequence with HPIS unavailable.

The objective of the calculation was to improve physical understanding

and to identify areas of desirable code model improvements based on

comparisons between data and predictions. The main goal of the base case

calculation was to assess the simuulation capability for the following

phenomena during three different phases of sequence:

- top-down drain of coolant in the primary system;

0 stratified two-phase flow in horizontal legs;

- loop seal clearing and associated temporary core liquid

depression with liquid holdup in steam generator primary side

leading to core heatup;

- quick core level recovery after loop seal clearing;.

- vessel inventory boiling leading to second core uncovery;

- core reflooding due to accumulator injection.

The base calculation predicted the top-down drain and the cyclic

loop seal formation and clearance. However, subcooled break flow was

overestimated while the vapor phase break flow was quite underestimated.

It finally influenced the time of core uncovery and, therefore, the

depressurization rate along with the timing of injection governed the

flooding rate of the core by the accumulator.

V
Thus, sensitivity studies regarding different options for the break

(downward junction, homogeneous option, and area compensated one) were

motivated to investigate their effects on the T/H results. Among them,

the area compensated one, which increased the break area by 17 % to match

the boundary condition based on the integrated break flow, gave the best

results among all the cases. A downward junction model improved the

density and the break flow predictions in early boil-off phase, but not

much in the later two-phase and recovery phase after accumulator

injection. The improper coding of the interfacial drag in'the horizontal

stratification regime caused the liquid slug to move from the cold leg

not into the break but into the downcomer. The liquid filled downcomer

prevented the core from heating up. Also, the liquid holdup

experimentally observed in the primary side of the steam generator was

not predicted by the RELAP5/MOD2 due to the deficiencies of the CCFIJ

models. These deficiencies overally contributed to predicting inventory

mass distribution inaccuratly. A homogeneous option reduced the

oscillation of cold leg density. However, the above two options could

not predict a heatup because the downcomer was still covered with the

liquid slug. However, liOD3 modeling was able to predict the CCFL

phenomena in steam generator primary side and the heatup in the core.

Vi
Acknowledgement

This report was completed under the sponsorship of the Korean

Ministry of Science and Technology. Dr. Sang Hoon Lee, President of the

Korea Institute of Nuclear Safety, contributed significantly to the

project administration.

Authors express great appreciation to professors E. C. Lee and C.

S. Hang in Seoul National University and professors M. H. Chun and S.

H. Chang in Korea Advanced Institute of Science and Technology for their

in-depth technical reviews in Korea.

Final thank goes to Miss E. K. Him for preparing data plots.

Vii
List of Tables

Table 1 Mlajor Design Comparisons of Semiscale and PWR........... 25

Table 2 Comparison of Initial Conditions...................... 26

Table 3 Chronology of Main Events............................ 27

Table 4 Sensitivity Study Matrix............................. 27

viii
List of Figures

Fig. 1 Semiscale 1Jod-2C.................................... 29

Fig. 2 Nodalization of Semiscale S-NH-i ..................... 30

Fig. 3 Break Flow Rate..................................... 31

Fig. 4 Integrated Break Flow................................32

Fig. 5 Upper Plenum Pressure ............................... 33

Fig. 6 Pressurizer Liquid Level............................. 34

Fig. 7 Pressurizer Pressure ................................ 35

Fig. 8 Core Thermal Power.................................. 36

Fig. 9 ILCL Flowrate ...................................... 37

Fig. 10 BLOL Flowrate ...................................... 38

Fig. 11 IL Feed Flowrate .................. ;................. 39

Fig. 12 EL Feed Flowrate.................................... 40

Fig. 13 IL SG Pressure ..................................... 41

Fig. 14 EL SG Pressure......................................42

Fig. 15 Density BLCL ....................................... 43

Fig. 16 IL SG Level........................................4,4

Fig. 17 BL SG Level ........................................ 45

Fig. 18. DC Liquid Level..................................... 46

Fig. 19 Vessel Liquid Level ................................. 47

Fig. 20 Peak Cladding Temperature ............................ 48

Fig. 21 Intact Loop Sf6 ADV Relief Flow....................... 49

Fig. 22 Broken Loop S/G ADV Relief Flow....................... 50

Fig. 23 Intact- Loop Accumulator Injection Flow................. 51

ix
Fig. 24 Broken Loop Accumulator Injection Flow................. 52

Fig. 25 MOM3 BLSG Primary Side Liquid Level ................... 53

Fig. 26 M1OD3 PCT........................................... 54

Fig. 27 Downcomer Flow rate ................................. 55

Fig. 28 Time Step Size ..................................... 56

Fig. 29 CPU Time........................................... 57

x
List of Contents

Abstract ................................................. ii

Executive Summary........................................... v

Acknowledgment.............................................vii

List of Tables ............................................ yiii

List of.Figures ............................................ ix

-1. Introduction ............................................ 1I

2. Facility and Test Description ............................. 4

3. RELAP5 Mlodelling Description............................... 6

4. Comparisons of Calculations to Measurements.................. 8

4.1 Blowdown Phase ....................................... 10

4.2 Core Boiloff Phase.................................... 12

4.3 Recovery Phase ....................................... 17

5. Run Statistics........................................... 19

6. Conclusions............................................. 20

References ............................................. 23

Tables ................................................. 25

Figures................................................. 29

Appendix

.Xi

,1. Introduction

'The International, Code: Assessment .and Application Program (ICAP) has

been conducted by fourteen nations .under the auspices of, the 1JSNRC[lJ.

For the pressurized -water reactor analysis, the USNRC selected .two Best

Estimate (BE) codes: RELAP5/120D2 and MOD3-.and TRAC/PFlI/hODl and !IOD2.

The objective of the ICPA' is ..to .provide --assessment .of . the .major

thermal-hydraulic computer codes ' against -various experimental data and to

provide input--to code improvement -and -user guideline. enhancement [2]. In,

addition, the ICAP. has an objective of providing the necessary data .base

for the qualitative characterization of computer codes as applied in a

best-estimate fashion to hypothetical accident scenarios.

As. a part of -the Korean contribution ,to the ICAP, .this report

included the results -,and conclusions., of, assessment. studies involvingcomparisons between Semiscale Test S-NH-i data and RELAP5IIODZ [3)J code

calculations~on a Cyber 170-875 and 110D3 on a Cray-2S.. S-NH-i simulated

a small break loss-ofrcoolant. accident, (LOCA) .event with a break size of

0. 5% which is equivalent to a 2 inch break of a typical 27.5 inch

Pressurized Water Reactor (PWR)..cold leg. .RELAP5/MOD2-<is an advanced,

one dimensional, thermal :hydraulic,,, computer code - used to .calculate

reactor :transient response.. ?Three...major~deficiencies (critical, flow,

critica heat flux,. and interfacial -drag 1,models) have been identified

through IIOD2 assessment. A MOM3 calculation.; .[4) on a, CRAY-ZS showed

improvements in CCFL in the steam generator primary riser side.

1
Test S-NH-i [53J[6] was designed to investigate a small break LOCA

with a concurrent failure of high-pressure injection and to look into

specified recoveries to mitigate core temperature excursions. Data from

S-NH-i were used to assess the effectiveness of the code in calculating

system response to various operator actions taken to mitigate a core

heatup. The test assumed a total loss of the high pressure injection

system CHPIS) when a break occurred. Without HPIS, operator action would

be required to reduce the primary pressure to accumulator set points

prior to a heater rod temperature excursion. The Version of the MOD-2

code used in this calculation was Cycle 36.04 with minor modification by

Seeberger £7). A recent assessment of RELAP5/MODZ against S-NH-i was

done by Yuann [8] who pointed out the deficiencies of the code such as

underpredicting break flow, overpredcting interfacial drag, and a delayed

core heatup tine due to overestimated mass inventory. The Yuann 's report

contains a description of the test and the RELAP5/MODZ modeling

approaches employed in the calculation.

The main goal of the calculation is the assessment of the code with

respect to the simiulation capability of the following phenomena occurring

during a small break LOCA experiment:

- top-down drain of coolant in the primary system;

- stratified two-phase flow in horizontal legs;

- loop seal clearing and associated temporary core liquid

depression, with liquid holdup in SG primary side,

leading to core heatup;

2
- quick core level recovery after loop seal clearing;

- vessel inventory boiling leading to second core uncovery;

- core reflooding due to accumulator injection.

The report describes the results of the calculation performed by the

RELAP5/IIOD2 and MOM3 code and shows the comparisons of the calculation

results with the main variables obtained in the experiment. A brief

description of the Semiscale facility and S-NH-l test is provided in

Section 2, and the features of the REIJAP5 code and modelling is provided

in Section 3. Section 4 discusses the results of the base calculation

with the RELAP5/?IOD2. The reasons for sensitivity and nodalization

studies and their results are also included in Section 4. Four

sensitivity calculations were done for downward flow, homogeneous flow,

and an increased break area in addition to MOM3 calculation. The code

efficiency is evaluated in Section 5 by examining the run statistics.

The conclusions drawn from this study are given in Section 6.

3
2. Facility and Test Description

The Semiscale Mod-2C system is a scaled, two-loop representation of a

pressurized water reactor (PWR), with a fluid volume and a core power of

about 1/1705 of a full sized PWR. Geometric similarities of component

layout have been maintained between the Semiscale system and a PWR, as

shown in Figure 1 and Table 1. The Semiscale Mod-2C system consists of a

pressure vessel with simulated reactor internals and electrically heated

fuel rods and an external downcomner. The intact loop simulates three

unaffected loops of a four loop PWR, and the broken loop simulates an

affected loop in which a small break is assumed to occur. The unique

feature of the Mod-ZC system is the installation of Type III steam

generator which has an external downcomer to allow gamma densitometers to

measure the riser density. The unaffected loop steam generator consists

of six inverted U-tubes. The outside diameter of the U-tubes is 0.0222

m, which is similar to the outside diameter of typical PWR steam

generator U-tubes (about 0.018 in). The reactor internals consist of a

5X5 array of internally heated electric rods of which 23 are powered.

The rods are geometrically similar to nuclear fuel rods, with a heated

length of 3.66 m and an outside diameter of 0.011 m. External heaters

were wrapped in a relatively uniform manner on the vessel, downcomer,

pressurizer, and primary loop piping to offset environmental heat losses.

4
Test S-NH-i was conducted in the Serniscale Mod-2C system. The

*S-NH-i test represents a 0.5 X centerline pipe break between the broken

loop pump and the vessel. The break was simulated by an orifice that has

a scaled area equivalent to a 0.051 mn (2 inch) diameter break in a PWR.

The break was initiated at 0 s, and complete loss of HPIS was assumed to

occur. The core scram, primary coolant pump trip, auxiliary feedwater

flow initiation, and main steam isolation valve (MSIV) isolation all

automatically occurred after the low pressurizer pressure signal was

reached. The core power decreased to ANS decay heat corresponding to 3 s

after the scram signal was initiated to simulate the control rod drop

time. An operator induced recovery was initiated at a peak cladding

temperature of 811 K, at which time the steam generator atmospheric dump

valves (ADV) in both loops were latched open at 2630 s in experiment.

Auxiliary feedwater flow was continued to maintain the secondary level

between 9 and 10 mn. The steam generator ADVs were cyclically closed and

opened when the steam generator level was at 2 and 4 mn, respectively.

Accumulator injection flow was terminated when the primary system

pressure exceeded 4.2 HPa, or when the accumulator emptied. The test was

terminated when the pressurizer pressure dropped to 1.38 MPa, which is

the nominal low pressure injection (LPIS) set point. No LPIS was used

for S-NH-i.

5
3. RELAP5 Modelling Description

The RELAP5/MOD2 code is an advanced, one dimensional, system

analysis computer code developed at the INEL for the U.S. Nuclear

Regulatory Commision, Office of Nuclear Reactor Safety Research. Cycle

36.04 of the RELAP5/tlOD2 code was used for the assessment studies. The

Semiscale Mod-2C input model is represented by the nodalization diagram

shown in Figure 2. It consists of 181 hydrodynamic volumes and 256 heat

structures. Steam generator secondary sides, emergency core cooling

system (EGGS) injection systems, vessel and piping external heaters, and

system environmental heat loss were all modeled in detail. Also, a

chopped cosine for the core axial power profile was modeled by 12

consecutive heat structures. The non-equilibrium option was applied to

all hydrodynamic volumes and junctions except the pump discharge, where

the one-velocity, gas-liquid equilibrium momentum equation was used.

Modeling concept for MON3 basically camne from the one used for ISP-26

assessment with LSTF [15).

0.5 % break was modeled by 1.23 mm(O.047 inch) nozzle diameter,and a

normal, non-homogenous, abrupt and choking option were used for the

model. Discharge coefficients, 0.9 and 1.2 were applied to the RELAP5

critical flow model at the break to compensate the overprediction in

subcooled and underprediction in two-phase region, respectively. A

sensitivity calculation was proposed to increase the nozzle diameter

because the code underpredicted the break flow in the overall transient.

Operator actions involving the secondary coolant system were modeled with

feed and bleed operation using trips and controls.

6
The RCS auxiliary feed pump was assumed to be on for about 30 min

starting at I min after scram to simulate the automatic initiation of

auxiliary feed for a large PWR, and later an atmospheric dump valve (ADV)

was assumed to open, as recovery procedure for bleeding. A PCT higher

than 811 K actuated the signal to open ADV.

The vessel and piping external heaters were modeled mechanistically

in RELAP5, and the measured power was an input as a boundary condition.

The measured core power and normalized pump coastdown speed were also

input as boundary condition. Normally, the HPIS flow rates were input as

a function of primary system pressure, but not used in this calculation

because the HPIS was disabled for the S-NH-i test.

Desired steady-state initialization was achieved by adjusting the

steam generator secondary pressure using control systems to achieve the

desired primary cold leg temperature. The results are shown in Table 1

for Test S-NH-I. The calculated and measured initial conditions were

compared well with a few exceptions. These exceptions are due to the

adjustment of the steam generator pressure[1Z).

7
4. Comparisons of Calculations to Measurements

During a small break loss of coolant accident,the primary coolant

inventory loss will continue until the break flow rate decreases

sufficiently, due to break uncovery or primary system depressurization to

allow the emergency core cooling system to make up the coolant loss.

Such coolant inventory depletion will involve concurrent liquid level

depressions in the downflow side of the cross-over leg , for each loop,

and in the vessel riser section (upper plenum and core). 'Meanwhile, the

upflow side of the cross-over leg, cold leg and downcomer will remain

liquid filled up to the break elevation. The core level depressions will

continue until the dowuflow-side level of the cross-over leg reaches to

the bottom of the legs and thus allows the vapor to clear the liquid seal

in the cross-over legs toward the break. When this liquid clearing (loop

seal clearing) initiates, the core liquid level starts to recover. This

occurs because the vapor can now reach the downcomer and eliminates a

back pressure to allow the downcomer liquid to go into the core

regiont 8).

In the present study the RELAP5/MODZ Cycle 36.04 code was used for

the base calculations, and their results are shown in Figures 3 to 29.

Figures 25 and 26 show the improved results obtained from MOD3 version

5m5 as a sensitivity calculation. The major initial conditions, as shown

in Table 2, and the sequence of events, sunmmarized in Table 3, are

compared with the experiment. The calculated steady-state parameters are

in good agreement with the corresponding measured values except the

temperature rise in the core between inlet and outlet.

8
The input listing for the base calculations is attached in Appendix.

Included in this subsection is a comparison of the calculated results

with measured data. Hydraulic behavior can be explained primarily with

discharge flow rate, depressurization rate, external ECCS flow, system

mass inventory and finally core mixture level. Thermal behavior, then,

can be described with the core thermal power, S/G secondary modelling,

core void and PCT. Figure 3 shows the break discharge flow rate while

Figure 4 depicts the integrated break flow. Figure 5 also shows the

depressurization rate of primary system, which characterizes the overall

system T/H transient.

Comparisons were made in three different phases:l) the blowdown

phase, 2) the primary boiling and core heatup phase and 3) the recovery

phase. The first phase was defined for a time interval from 0 to 150

seconds as the pressurizer level decreased to zero, the second phase for

a time interval from 150 to 3000 seconds as the core starts to boil and

heat up and the third phase for a time interval from 3000 to 5000 seconds

as the system is recovered from the actuation of ADV valves and

accumulator valves. The assessment parameters are listed in Table 4.

9
4.1 Blowdown phase ( 0 to 150 s)

The initiating event in the S-NH-i test was the opening of the

blowdown valve in the broken loop between the pump and vessel. After the

break was opened, break flow was first characterized as subcooled

critical flow, followed by saturated liquid blowdown and finally

two-phase mixture blowdown. The break flow measurement system in

Semiscale (12] is subject to a considerable lag time due to the distance

between the break plane and the catch tank. Therefore, a direct

comparison between the measured and calculated break flow is not

meaningful during the early blowdown phase.

However, the pressurizer interfacial liquid level is a good

indication of the early water inventory loss, and it suggests good

agreement between the calculation and test data as shown in Figure 6. As

the pressurizer drained, a rapid depressurization of the primary system

resulted as shown in Figure 7. An inflection point observed as about

50.0 s in calculation and 60.0 s in measurement. This abrupt increase in

depressurization rate was caused by the pressurizer emptying and the

system power trip. The more discharge flow rate, the earlier inflection

point was observed.

The power trip signal in the calculation was generated at 39.9 s,

which was 21 s earlier than measured. System power responses from both

the measurement and calculation are shown on Figure 8. Except for the

timing, good agreement can be observed. After the scram signal, the

reactor coolant pumps (RCPs) coasted down and the main steam valves of

both steam generators began to close.

10
The trend of volumetric flow rate throughout the system was correctly

calculated considering 41 s pump coastdown delay, as shown in Figure 9

through 12 which show flow rates in the intact loop cold leg flowrate,

broken loop cold leg, intact and broken loop feed flow rates in the steam

generator.

Due to closure of the main steam valve in each steam generator, thle

steam generator shell side pressure rose sharply and then stabilized, as

shown in Figures 13 and 14. The energy transfers from the primary system

in both calculation and test are not expected to be different by

significant amounts of magnitude. However, the initial stored energy in

the metal mass in the steam generator and aux feed pump flow are the

areas of possible differences between the test and the calculation.

Another important contributor to a lower steam generator pressure was the

failure of the loop main steam valve to close completely in experiment,

as shown in Figures 13 and 14. As system pressure continuously decreased

after the scram, the safety injection system signal was generated at 46 s

in the calculation, which was 20.1 s ahead of the test.

11
4.2 Primary boiloff and core heatup phase (150 to 3000 s)

The period between the completion of automatic responses in the

first 150 s and the initiation of the recovery phase is discussed in this

subsection. This phase is characterized as a period of low

depressurization rate and a boiling of primary inventory leading to core

uncovery and core heatup. During this period, auxiliary feedwater flows

were terminated on high water level signals in steam generators and

normally assumed to operate for about 30 min in this type SBLOCA [13).

Discussion in this subsection includes the break flow response, system

pressure and flow responses, primary mass distribution, and core heatup

phenomena. The break flow discussion includes the results of a

sensitivity study dealing with the effect of the break modeling

options (downward,homogenous ,and area increase).

On an overall basis, RELAP5 undercalculates break flow, resulting in

consistently more mass in the primary system throughout this period. A

comparison of calculated and measured break flow rates is shown in Figure

3. It can be seen that the calculated break flow was initially higher

during the phase of saturated liquid blowdown but lower in this second

phase, as shown in Figure 3. The calculated transition from saturated to

vapor-phase blowdown occurred at 750 s, which was 1250 s earlier than in

the test indicating the crtical flow model deficiency. This is evidenced

by the responses of the broken loop cold leg density, which are shown in

Figure 15. The trend of the calculated break flow followed the measured

break flow during the two-phase period; however, again the calculated

values were lower than the data.

12
The total loss of primary water inventory in the calculation was almost

consistently 7 kg (15.4 lbin) less than that measured, as shown in Figure

4, which yields th e tendency to calculate a later core uncovery and

heatup.

.In general, both primary and secondary pressures were calculated to

be slightly lower than the measured, as shown in Figures 5, 13 and 14.

As stated before, the magnitude at which pressure stabilizes is a

function of the gross energy balance. For the whole system, such a

balance involves core power, external heater power and brea-k energy,

environmental heat loss, stored energy and primary-to-secondary heat

transfer. The stored energy is a possible area of difference between the

test and the-calculation. It is probable that the stored energy of the

system was not the same condition as in the calculation. Another factor

that could have affected the overall energy balance, and thus the primary

pressure, is the RELAP5 modeling of global heat loss for S-NH-i.

After the coolant pumps were tripped, a two-phase natural

circulation flow was established during the second phase. Figure 18

shows that there was a certain amount of flow sustained in the

downcommer, which terminated before the complete drainage of the intact

loop steam generator. RELAP5 correctly calculated the two-phase peaking

in flow with a slight shift in time. This peaking in flow is related to

shifting cold leg mass inventory not into break but into downcomer and is

discussed in detail in Reference [14). The calculated primary mass

distribution generally agreed with the test measurement during this

phase.

13
Exceptions were the broken loop steam generator liquid hold-up , liquid

slug movement into downcomer and not to break junction in horizontally

stratified cold leg volume and the timing of events mainly caused by the

difference in break flow and the unphysical liquid slug movement. For

this reason, only the increased area case was able to predict the heatup

while the other two options failed to predict the core heat up. The

primary system void formation generally progressed from the top to down.

The sequence of the system drainage was as follows: pressurizer, part of

SG primary U-tube, upper vessel, hot and cold legs, pump suction, finally

downcommer and core.

Figures 16 and 17 show that the steam generator U-tubes started to

drain at approximately the same time as the vessel. For the broken loop,

the drainage started about 1500 s earlier in the calculation. The reason

for early drainage of the steam generator in the calculation is also

related to differences in break flow and CCFL. Significant liquid

hold-up was measured in the broken loop steam generator but not

calculated by the MOD2 code. In the calculation, the broken loop steam

generator was empty by 850 s. The disagreement between RELFAP5 and the

data could also have been caused by primary-to-secondary heat transfer

differences. Even though in the data the broken loop steam generator was

at a lower pressure than the calculated one possibly due to the leak, the

steam generator remained as a heat sink for both the test and the

calculation. Therefore, the code should have calculated condensation

occurred in the primary tubes, indicating by a head of fluid rather than

the 0 m level shown in Figure 17.

14
NOD3 with a CCFL modeling predicted the liquid holdup as in Figure

25, and this improved prediction of the liquid level such that a

considerable PCT was observed as in Figure 26. Following the drainage of

the steam generators, the pump suctions also started to drain. In the

calculation, the drainage was completed when the upflow side of the steam

generator tubes were empty. When drainage started, a sudden expulsion of

water from the broken loop pump suction to the cold leg was observed in

the calculation. As a result, a sudden drop of liquid level in the pump

suction and a corresponding increase of cold leg density were observed.

In turn, a peak of the break flow was induced (Figure 3).

After complete draining of the steam generators and partial draining

of the pump suctions, the vessel and downcommer liquid levels decreased

at a similar rate in both the calculation and the test, as fluid in the

vessel simply boiled off (shown in Figures 18 and 19). Because of

differences in draining of loop components, the boiloff of the vessel

fluid started about 700 s later for the calculation than the data. With

similar boiloff rates, the code showed a core heat-up about 560 s later

than the data, as shown in Figure 20. A temporary turnaround in core rod

temperature in the data was due to a partial broken loop suction

clearing, liquid slug entrained into core rather than into break from the

cold leg (Fig. 15,18,19, and 20).

15
Finally, the recovery setpoint [peak cladding temperature (PCT) =

811 Kilwas reached at 2630 s in the test, which was about 700 s earlier

than in the calculation. Except for differences in event timing, caused

by differences in system drain and break flow, the core temperature

responses to the vessel level and the core heatup rate show good

agreement between the calculation and the test. However, the energy

extracted from the coolant is different indicating that system inventory

was overestimated and initial stored energy would be different.

Because the primary forcing phenomenon in this transient was the

break flow, a sensitivity study was performed. For the base-case study,

the break flow was significantly underpredicted when the actual orifice

area was used;thus, several options including downward junction and

homogeneous options and 17 % increased area method was tested to

compensate the underestimation and to match the break flow rate as an

important boundary condition. The break flow area sensitivity study

results are also shown in Figure 20. In the base-case calculation, the

mass flow out the break was significantly underpredicted;and,as a result,

sufficient primary system inventory was maintained to prevent a core

heat-up in calculation after the observed core heat-up. The core heat-up

was calculated to occur about 1000 s after the observed occurrence

through the area compensating method. Clearly, among three methods, the

area compensation provided the better prediction of the break mass flow

during the second phase.

16
4.3 Recovery phase (3000 to 5000 s)

The period between initiation of recovery actions and the test

termination is discussed in this section. Recovery actions consisted of

latching open both steam generator ADV valves and normal accumulator

injection. The recovery action was taken to increase system

depressurization rate to reach accumulator and LPIS set points more

quickly. Recovery was initiated when the PCT reached 811 K, which

occurred at 2630 s in the test and 3300 s in the calculation. When an

I\FV valve on each steam generator was manually lifted, the steam flow

drastically increased as shown in Figures 21 and 22. Except for the

timing, the calculated and measured ADY relief flows are in good

agreement in the area compensated case. As a result of ADV relief, the

shell side of the steam generators depressurized quickly as in the area

increased case, as shown in Figure 13 and 14. The calculated

depressurization rate in each steam generator was slower than measured.

In turn, a slower primary system depressurization in the calculation

resulted. There are two likely causes for the difference between the

calculated and actual depressurization rates in the steam generators.

The first possibility is that the energy relief rates through the ADV

valves were different, and the second possibility is that the stored

energy and the aux feed pump flow rates were different.

As a result of a faster primary depressurization rate in the test,

the accumulator injection set point [4.2 N~a) was reached earlier in the

test than in the calculation. The faster depressurization rate

contributed to a faster core quench as shown in Figure 20.

17
The accumulators injected emergency water into the vessel earlier in the

test than in the calculation by about 700 s as shown in Figures 23 and

24. The timing difference was caused by different primary

depressurization in both the test and the calculation. Correctly

calculating accumulator injection requires correct calculation of the

primary depressrization during the injection period.

The PCTs are shown in Figure 20. With less accumulator injection

flow rate and the slower system depressurization in the calculation, the

core was quenched faster than measured, and the difference in PCTs was

about 80 K. The calculation was terminated at 5000 s as the pressure

approaches LPIS pressure (1.38 N~aI.

18
5. Run Statistics

CDC 170-875 with NOS Version 2.6.1 was used to calculate S-NH-i

using RELAP5/MOD2 Cycle 36.04. Figures 28 and 29 show the time step size

and CPU time vs. the transient time in the base case calculation. The

time step control cards chose the minimum and the maximum time step as

1.OE-7 and 5.0, respectively. Grind time and computational efficiency

can be summarized as follows:

CPU 5749.49

Grind time, GT - = _____ = 0.002275

C * DT (181)*(13962)

where CPU: computer time

C: number of volume

DT: number of time step

19
6. Conclusions

The RELAP5/IIODZ Cycle 36.04 calculation correctly simulated most of

the important thermal-hydraulic responses for Test S-NH-i. However, the

integrated break flow was undercalculated, and thus the primary mass was

greater in the calculation than in the test. To compensate 'this

overestimated mass inventory, 17 % increased break area model was tested

as well as downward junction option and homogenous option. A better

result was obtained with the increased area option. The improvement

implemented in MlOM Version 5m5 was investigated to see the effect on

CCFL prediction. Generally, the RELAP5/NOD3 5m5 calculation produced

results qualitatively similar to the test. However, several important

differences were observed resulting in the following conclusions and

recommendations:

1. The calculated break flow during subcooled was overestimated but,

during saturated and two-phase period, underestimeted; and, in overal,

the integrated mass was 17 X underestimated at 2500 s before any external

ECCS flow injected. Thus, 17 % break area increase with 0.9 and 1.2 of

Cd's were used to model the correct break flow rate which lead to a

better result. The code also showed a sharp transition from two-phase

mixture to single phase vapor break flow probably due to the deficiency

in calculating a* sound speed and two-phase choking criteria at around 0.1

of void.

20
2. During the boil-off phase, the liquid slug was delivered from the

cold leg not into the break but into the downcomer because the code has

deficiency in calculating the interface drag in horizontal stratification

flow regime; and it delayed the core heatup.

3. Overall mass inventory overestimated by the 110D2 did not result in

the core heatup contrary to the test results; the inaccuracy of

predicting the mass distribution in the loop appeared to be the main area

to be improved. The improvement should include the break flow model,

CCFI ,and horizontal stratification interfacial drag model.

4. The liquid hold-up and condensation observed in the broken loop steam

generator during the second phase of the experiment was not predicted. A

reason for excessive condensation was no CCFJJ model available in MOD2.

MOMD predicted the CCFL and the core heatup successfully without even

considering the area increased.

21
References

1. U. S. Regulatory Commission, Compendium of ECCS Research for Realistic

LOCA Analysis, NUREG-1230, May 1987.

2. Guidelines and Procedures for the International Code Assessment and

Applications Program, NUREG-1271, April 1987

3. V. H. Ransom et al., RELAP5/MOD2 Code Mannual

Volume 1: Code Structure, System Models and Solution Methods

Volume 2: Users Guide and Input Requirement, NUREG/CR-4312, March 1987

4. EG&G Idaho, Inc., Appendix A RELAP5 Input Data Requirements, prepared

for release of RELAP5/MOD3, January 1990.

5. W.A. OWCA, Quick Look Report for Semiscale MOD-2C Experiment S-NH-i,

EGG-RTH-7147, Feb 1985.

6. J. L. Anderson, Experiment Operating Specification for the Semiscale

MOD-2C Small Break LOCA without HP! Experiment Series, EGG-SEMI-6920,

June, 1985.

7. Seeberger, RELAP5/MODZ-RH2 Modification of Cycle 36.04, U811-87-3065a,

December 22 1987, Kraftwerk Union, Eralngen.

8. R. Y. Yuann, K. S. Liang and Janice L. Jacobson, RELAP5/MODZ Assessment

Using Semiscale Experiments S-NH-i and S-LH-2, EGG-2520, October 1982.

9. William E. Burchill, Physical Phenomena of a Small-Break Loss of Coolant

Accident in a PWR, Nuclear Safety, Vol 23, No 5, Sep-Oct 1982.

10. Naugab Lee, Limiting Counter Current Flow Phenomenon in Small Break LOCA

Transient, Nuclear Engineering and Design, 102, 1987, pp. 211-216.

22
11. Parez Salim and Y. A. Hassan, Mlodeling and Loss of Coolant Accident

Analysis of a Nuclear Power Plant Using RELAP5/NOD2, pp. 275-285,

Nuclear Technology, Vol 90, June 1990.

12. E. Klingler, K. E. Suckett, The Semiscale MOD-ZC Small Break (0.5 % and

2.1 %) Configuration Report for Experiments S-NH-I, S-NH-2, S-NH-3 and

S-NH-5, EGG-RTH-7323, July 1986.

13. D. L. Gillas and Janice M. Carpenter, Experimental Data Report for LOFT

Nuclear Small Break Experiment L3-7, NUREG CR-1570, EGG-2049, 1980.

14. G. 6. Loomis, Summary of the Semiscale Program (1965-1986),

NUREG/CR-4045, EGG-2509, July 1987.

15. S. Lee, B. Chung, and H. Kim, RELAP5 Assessment Using LSTF SB-CL--iS,

Submitted to INEL and USNRC, Feb 1991.

23

Table 1 Major Design Comparisons of Semiscale and PWR

Semis cale

!lod-2C

PWR size modelled / No of loops

No of loops

Scale (volume)

Elevation scale

Power (MW)

Pressure (MPa)

Pumps

Steam generator

No of heater rods &

size (length & dia)

Downcomer

Broken leg dia(mm)

Intact leg dia(mm)

Break dia (mm)

No of SG tubes!

elevation scale

3411 MWt/4

2

1:1705

1:1

2

16

Active

Active

25

3.66m/20.72mm

External

33.98

66.95

1.23

6,2

1:1

25
Table 2. Comparison of Initial Conditions

Parameters Neasured (6] Calculated, SNHSOT

Pressurizer pressure,MPa 15.64 15.47

Core power, MW 2.00 2.01

Core DT, K 37.00 31.19

Pressurizer liquid level, cm 257.00 257.38

Loop-to-loop fluid temp

difference of cold leg, K 4.20 3.13

Cold leg fluid temp, K 550.00 547.82

Primary flow rates, L/s

Intact loop cold leg 9.10 9.10

Broken loop cold leg 3.20 3.20

Loop flow split 2.84:1 2.84:1

S.G. secondary pressures, MPa

Intact loop 4.55 4.55

Broken loop 4.48 4.48

S.G. secondary masses, kg

Intact loop 73 73

Broken loop 23 23

S.G. feedwater flowrates, kg/s

Intact loop 0.82 0.84

Broken loop 0.25 0.26

S.G. feedwater temp, K 494 505

26
Table 3. Chronology of Main Events

Events Specified Measured (6) Calculated

Cold leg break

P(PRZ)=13.1 MPa (1887 psig)

Main steam valves close

Core power decay initiated

P(PRZ)=12.51 M.Pa (1801 psig)

Main feedwater secured

Auxiliary feedwater started

Reactor coolant pumps tripped

S.G. ADV valves latched open

Accumulator injection begun

Test terminated

0

T=T(SCRAM)

T(SCRAM)

T(SCRAM)+3.2

T=T(SIS)

T(SIS)

T(SIS)

T(SIS)+2

PCT=811K

P(PRZ)=4.22 MPa

P(PRZ)=1.38 MPa

0

61

62

64.5

67

68

68

70

2630

2828

5000

0

39.92

40.93

46.91

47,9Z

47.92

48.94

3330.00

3520.00

4000.00

Table 4. Sensitivity Study Matrix

Case 0 (Base) Case 1 Case 2 Case 3 Case 4

Break Reference Dounward Homogeneous Area Reference

Option 00100 20100 00110 00100 00100"

.Area 12.174e-4 12.174e-4 12.174e-4 14.405e-4 12.174e-4

Code MOD2 MOD2 MOD2 MOD2 NMOD3

Computer Cyber Cyber Cyber Cyber Cray

2 7

Recirculation lines

Type IIl steam

generation

downcomerPressure

vessel .----.-

BROKEN LOOP'

Fig. 1 'Semiscale Mod-2C

29
I'.

CD,

C')

C-,

CD

C,,

Heater bonds ow

~~ZJ Heat slabs

Internal healers

Semiscale nodalization diagram for TEST S-NH-i RELAP5 calculation
SEMTSCALE: 0.5% SOLOCGA S-{IH--1 0. 150

0. 125

-0. 100

S0.075

IiM~ 0.050

c-.

(13

-Exo :MDOT RAK 1 

-eCase 0 (SNHIPFO: t4F-.OWJF

*Case 1 (SNH1PFD -~Case 2 ~SNF11PFF1 -- Case 3 ISNHIPFA)

C,3

0.025

0

1000 0"000 3000 4000

Time (s)

Figj. 3 Break Flow Rate
ISO

7;m 12o0!

IiLeDSEMI¶3GALE 0.5% Sf3LOCA '3-+H-1

T-]

C-.

60

30

0

4000

Time (s)

Fig. 4 Integrated Break Flow
SEMISCALE : 0.5% Sr3L.OCA S-NH--1

-Exp PV-Pvu*-i,3-,-- -o Case 0 (NlPO P16201

-+ Case 1 (SNH1PFD17 -fi Case 2 (SN-H1PRI

-+Case 3 ISNIIPFA

cla

(j)

SI,

On.

12

9.0

6. 0

3.0

0 500 1 000 15o() 2000 2500 '3Ooo 3500

T ime (S)

Fi!;(j. 5 Upnper Plenum Pressure
SEMISflAUBE 0.5% 53BLOCA SN200

C~3

(.1

(I)

0*

-I

'-I

(0

I-)

(I,

f-.

C-.

C

(-I

ISO0

100

50

0

150

T imfne (s)

Fig. 6 Pressurizer Liquid Level
SEMIESCALE: 0.5% SBLOCA S-rlh-i- 16

ICI

C-.

En C- C)

r-I

14 Z

12

10L

a.0 o6.0.

150

T im ne (s)

Fig. ? Pressurizer Pressure
SEMISiCALE. 0.5% SBLOCA S-Mi-1

2.5 I-- - DC'(PW.R (S HlPFO : CtI1TIL./I

I[SNH 1PFD

! SNH 1 FR) I SNHlrFA) 2.0

c..

CI)

C

F'-

C"

C-.

C

C-,

0. 500L

0

0 30 60 90 M5

T-ime (s)

Fig. 8 Core Therm~ia Power
SEMISCALE :0.5% SBLOCA S-NH-I 12

-Exp: Q *1.......

oe Case 0 (SNHIPFO) MFLO -A Case I ~SN~l-PFDJ

2 (SNHIPFH U, -+ CaseR ISNHIPFA

-J

rti

0

4-J

-If-i

0

6.0

3.0

0

0 30 60 90 120 150

Time (s)

Fig. 9 ILCL Flowrate
SEMISCALE: 0.5% SBLOCA S-NH-I

4.0

C-., Go

cn

a.)

:r_

0

U-f

.1-1

4-) a.)

0

2.0

0

-2.

0 30 60 90 120 150

Time (s)

Fig. 10 BLCL Flowrate
1.0(

V 0.600

0.200)

0

1SEMISCALE 0.5% Sf3LOL.A SN

- - Exp mr OT*ILFO Q

-e cs e 0 (SNHlf-Fo) MFL.JJ ClOY)O -7ý Cime 1 tSNFH1PFO) -q Cii3e 23 SNFIIPFFI

2 ~------ --- sp,__3 (SNF 1PFA) I

W,

150

w

0 390 1)0 90 120)

Time (s)

Figj. 11 IL Feed Flowrate
SEME)GALE. 0.5% SI3LOCA L3-NHI-i

0. 300 -. Exp :M[ OT*8iL. OW-

-o Case 0 (SWIHr1r0) : MFLOWJ 72200

j 2S21 s ~SNH1FO icjas 2 2 (SI'HPRiI) se3 (SNHIPFA)

0.200

((1

0)

~1

IIen

en

en

0. 100 1-.

0 L~I 1].

-0.10(l'L I I I w

0 30 60 90 120 150

Time (s)

Fig. 12 BL Feed Flowrate
SEMVISCAL.E 0.5% Sa3[.dA S-NI-'I 8.0 ___

-. Exp PSi-1 11?

ae Gasce 0 (SINI- PfO) :P 60101

ca Cs e 1 SzNI-1PFOJ

-i]Ca oe 2 SIfIFI-IWF -+Case 3ý ISNFIIPFA

os .0

rA I

wr

L..

E:-

2.0

0

0 1000 200( 3000

1I

4000

Ti ine (s)

Fig. 1i3 IL SG Pressure
SEMISCA-LE :0.5% SBLOGA S-NHI-I

0. 0 - Exp :Pi~i1'1 W6

-0 Case 0 (SNHlPF0) P 70101

-6 Case 1 SNHIPFfl' -fji Case 2 (SNHIPIFi) -i+ Case 3 (SNH1PTFA)

(9.0

(A,

L...

Cr.

en

U,

-I-,

Cfl

(J)

4t. 0

2.0

0

0 1000 2000 3000 4000

T imine (s)

Fig;. 14 f3L SG Pressure
SEMISCALE :0. 5% S8L.OCA S--NFI-'i

1200

900

Cr)

600

cr

300

0

0 500 1000 1500 2000 2500 3000

Time (s)

Fig. 15 Density BL.GL
SEMISCALE :0. 5% SEILOCA S-NH-I

-Exp :LI ~P971-57E

-SCase 0 (SNHIPFO): CNTRLVAFR 7 -A Case 1 ISNH1PFO) -pi Case 2 (SNMIPFH)

-+ Case 3 (SNH1PFAI

G)

-1

*ri

a)

ci.

(0

800

800 L

400

200 -

0OL

-200 

0 

L

500 1000 1500 2000 2500 38000 3500

Time (s)

Fig. 16 IL SG Level
SI-.MIS(;AL.E- OJ: 0ý SIBLOCA 5-NFI-1

11 -- LExp LL. PL.H993-517C- -

-ea P;,s 0 (SW 1PFO) CNVC(.I-VAFI 11

C F>,s p 1 (SNH 1PF6J -fj~ C;,se 2 S1sN1PRIF

±Cas~e. 3 IS*H11FPFA) __

cn1

I-.,

-I

LL~

* -I

-I

MY)o

600 L6

400):-

200:r

-200 L

0 500 I 000 1 V00 2000 2.500 1-000 39500

Time (s)

Fin. 17 BL SG Level
~iiM 1:itA. (.")/ S BirL(I(A l-i-W-*1

100

I-)

0

9'-100

.-1 -.200

-I

(1)

ci.

0.i

MI

-300

--400

-500

'+-* Case 93 SN~iFT**A'I

-ff. Case 2 (SNH1PFHJ -*Case 1 (SNFI1PFDJ -. Case ) (SNH IPEG) CNTALVAR 563

-Exp :L00129-573B

0 500 1000 1500 2000 2bOO. '.0O0 3500

Timie~ (S)

Fig. 18 DC Liquid Le~
SEMISCALE :0.5% SOLOCA S-NH-I

0

-I

U

a)

U)

U,

-100

-200

-:300

-400

3500

Time (s)

Fig. 19 Vessel Liquid Level
SEMISCALE :0.5% SBLOCA S-NH-I

tt0,

a)

C- a)

C3.

E

C.-

a,

a)

C-,

0 '1000 2000 3000 4000

Time (s)

Fig. 20 Peak.Cladding Temperature
SEMvISCALE: 0.5% SBLOCA S-NH-I

0.200

0. 150

U,

M)

ýC0.100 0

r-1

4,

S0. 050

0:

4000

Time (s)

Fig. 21 Fig Intact 21 Loop S/G ADV Relief Flow
SEMISCALE :0.5% SBLOCA S-NH-I o0.060 -I

0.060

Ex: P MMUOT*BL*A VI -Case 0 (SNHIPFO : MFLOWJ 73400

h~ Case I ~SNH1PFD I

-M Case 2 SNHIPFI-U -+ Case 3 ISNH1PFAJ

cn

Un 0.040

4-

U)

S0.020 I

I - t S -

M a W.' I ra ,IMI*A I ... &q 01- - .4 .

20000 -- -25600 350 - ý000

Time (s)

Fig. 22 Broken Loop S/S ADV Relief Flow
SEMISCALE: 0.5% SBLOCA S-NH--I 0.060

S0. 040

0

g~0. 020

0

Ca,

I.-

21

Time (s)

Fig. 23 Intact. Loop Accumulator Injection Flow
SEMISCALE :0.5% SBLOCA S-NH-I

0.040

.0.030

0

U,

c-n

L\;P

T:0.020

0

F-'

(n

0.01

0

4000

Time (s)

Fig. 24 Broken Loop accumulator Injection Flow
SEMISC,\LE :0.5% SBLOCA S-NHI-I

ul

U

a)

T-3

0 500 1000 1500 2000 2500 3000 3500

Ti me (s)

Fig. 25 MOD3 SLSG Primary Side Liquid Level
SEMISCALE : 0.5% SBLOCA S-NHI-I

03

C-.

4-)

cu

C0)

0-)

0 11000 2000 3000 4000 5000

Time (s)

Fig. 26 MOM3 PCT
SEMISCALE :0.5% SBLOCA S-NH-I

15

12

-Exp : QV*DC-423

-eCase 0 (SNH1PFO): MFLOWJ 11001

-6 Case I (SNH1PFDJ

-B Case 2 ISNHIPFH)

-+ Case 3 ISNH1PFAI

I

c,

c"

c,,

0

I-I

MM,

M,

6.0

3.0

0

-3.(C

L

Li 5U LiLa I'-' LI Li I '.fl-~ U It~ Li La flJ Li U I~ Li La I'.J Li La I ~J

I I I

0 500 1000 1500 2000 2500 3000 3500

Time (s)

Fig. 27 IOowncomer Flow Rate
SEMISCALE :0.5% SBLOCA S-NH-I

5.0

4.0

3.0

a)n

2.0

1.0

0

1000 1500 2000 2500 3500

Time (s)

Fig. 28 Time Step Size
SEMISCALE :0.5% SBLOCA S-NH-I

0,

E

I0~

C-,

C-'

3500

Time (S)

Fig. 29 CPU Time

Appendix

/JOB

SNHlS2,T6000.

/USER

ATTACH, STH2XT, RE364BX.

PIJRGE,SNISZRP/NA.

DEFINE, RSTPLT=SNIS2RP.

FL,RSTPLT ,SBF=NO.

RFL, CM=370000, EC=2OO.

REDUCECRE364BX, ,*PL=50000.

/EOR

SEMISCALE MOD-2C

STANDARD TRANSIENT ***********

INPUT DECK

******************** FOR RELAP5/MOD2 ************

*******NOTES-

***1. THIS MODEL IS BASED ON THE STANDARD MOD-2A MODEL

DOCUMENTED IN REFERENCE 2 BELOW;~

***2. STEADY"STATE RUNS ARE MADE EITHER WITH THE PROVIDED

CONTROL SYSTEMS PACKAGE OR WITH ADDITIONAL COMPONENTS **

FOR SINGLE CONDITION STEADY STATE CALCULATIONS.

***3. VESSEL HEATER TAPE TO OFFSET VESSEL HEAT LOSS IS

INCLUDED WITH THIS MODEL. A CONTROL SYSTEM TO SHUT OFF **

THE VESSEL HEATERS AND REDISTRIBUTE THE POWER AMONG

*THE REMAINING HEATERS IS ALSO INCLUDED IN THIS MODEL. **

***4. THE THERMAL CONDUCTIVITY OF THE INSULATION ON THE

VESSEL AND PIPING HAS BEEN MODIFIED TO GIVE 56 KW`

HEAT LOSS. THE THERMAL CONDUCTIVITY OF THE INSULATION **

ON THE STEAM GENERATORS HAS BEEN MODIFIED TO GIVE

14 KW HEAT LOSS. AN ADDITIONAL 35 K•W IS LOST DUE TO

PUMP SEAL COOLING WHEN PUMPS ARE RUNNING AT FULL SPEED. **

THE HEATER TAPE IS WRAPPED IN THE "NO BREAK"

CONFIGURATION FROM DRAWING 414220.

***5. THE SYSTEM CONFIGURATION INCORPORATED IN THIS MODEL IS **

THE COMMUNICATIVE COLD LEG BREAK CONFIGURATION.

ALL UHI SYSTEM COMPONENTS ARE REMOVED AND UPPER HEAD

INTERNALS ARE MODELED AS MODIFIED TO REFLECT NON-UHI

PLANT CONFIGURATION.

***6. STEAM GENERATOR COMPONENTS HAVE BEEN RENODALIZED TO

REFLECT THE PPCC GUIDELINES AS ESTABLISHED BY CAAP

LETTER FROM C. DAVIS.

**~* 7.STEAM SEPARATOR COMPONENTS REFLECT RECOMMENDED MODEL

CHANGES FROM-J. TRAPP. (NO JUNCTIONS ARE ABRUPT, AND

INLET IS HOMOGENEOUS)

***8. PRIMARY COOLANT PUMP DISCHARGE JUNCTION IS HOMOGENEOUS ***
***9. THE PRESSURIZER IS THE 20 FOOT LONG PRESSURIZER WITH

HEAT STRUCTURE TO MODEL THE WALLS AND WITH HEATER

TAPE AND INSULATION ON THE OUTSIDE.

***10. A LEAK BETWEEN THE UPPER HEAD TO THE UPPER PLENUM

THROUGH THE SUPPORT COLUMNS AROUND THE PLUGS IS

INCLUDED IN THIS MODEL.

***11. THE PRESSURIZER SPRAY AND ASSOCIATED THERMAL SHOCK

SHIELD ARE INCLUDED IN THIS MODEL. NORMAL SPRAY GOES **

FROM THE INTACT LOOP COLD LEG TO THE PRESSURIZER VIA

TIME DEPENDENT VOLUMES AND JUNCTIONS, MATCHING TEMP.

IF AUXILARY SPRAY IS ALSO USED THE SPRAY TEMP WILL NOT ***

MATCH THE COLD LEG TEM1P. IF THE THERMAL SHOCK SHIELD **

WAS NOT INCLUDED IN THE TEST BOTH THE HYDRAULICS AND

HEAT STRUCTURE OF THE PRESSURIZER MUST BE MODIFIED.

* ~REFERENCES*

* 1. V. H. RANSON ET AL., RELAP5/MOD2 CODE MANUAL, VOLUME 1 AND 2, *

* ~EGG-SAAM-6377, SEPTEMBER 1983.*

* 2. MN. T. LEONARD, "RELAP5 STANDARD MODEL FOR THE SEMISCALE MOD-2A*

* 3. SYSTEM DESIGN DESCRIPTION FOR THE MOD-3 SEMISCALE SYSTEM, *

* ~REVISION B, DECEMBER 1980.*

-RELAP5 MODEL FOR THE SEMIISCALE NH-i POSTTEST - STEADY STATE (PZR LEVEL 90.10.6)

**FOR CONTROL SYSTEM STEADY STATE RUNS, MAKE APPROPRIATE CHANGES *

**IN COMPONENTS - *

** 610, 635, 710, 735, 980, 989, 991, TRIPS, AND CONTROL SYSTEMS *

*PROBLEM TYPE OPTION

0000100 NEW STDY-ST

*INP-CHI• OR RUN

0000101 RUN

*UNITS INPUT OUTPUT (SI OR BRITISH)

0000102 BRITISH SI

*TIME OUT MIN MAX

0000105 125.0 150.0

**VOL NO ELEY FLUID NAME

*0000120 101010000 1.0 WATER PRIMARY

*0000121 600010000 0.0 WATER ILSG

*0000122 700010000 0.0 WATER BLSG

T TEND -MIN ST MAX ST 'ST CL MR Mi WR

*0000201j 2. 1.0-7 0..05 3 20 40 40

0000201 1000. 1.0-7 0.05.. 3 40. 2000 -2000

*0000202 10. 1.0-7 0.05 3 20 160 160

*0000203 25. 1.0-7 0.05 3. 40 *300- 300

*0000204 100. 1.0-7 0.05 3 40 1500 1500
*0000205

*0000206

200.

1005.

1.0-7

1.0-7

0.05

0.05

3

3

40

40

1000 1000

2000 2000

**TRIPS -- TRIP CANCELLATION CARD 400 VARIABLE TRIP CARDS 401-599 *

** -- TRIP STOP CARD 600 LOGICAL TRIP CARDS 601-699 *

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

**

401

402

403

406

407

408

409

410

411

412

413

414

415

416

417

418

419

420

421

423

424

425

426

429

430

431

432

433

436

437

439

440

441

442

443

460

461

462

463

464

465

470

471

472

473

474

475

600

624

640

641

642

TERMINATE CALCULATION *

OPEN BREAK *

ALWAYS FALSE - USED IN MOTOR VALVES THAT ONLY CLOSE, ETC *

BEGIN TRANSIENT *

HPIS PRESSURE SETPOINT *

BEGIN UPIS *

BEGIN CORE DECAY - SCRAM *

CLOSE MAIN INTACT LOOP STEAM GENERATOR STEAM VALVE *

CLOSE MAIN BROKEN LOOP STEAM GENERATOR STEAM VALVE *

BEGIN INTACT LOOP PRIMARY COOLANT PUMP COASTDOWN *

BEGIN BROKEN LOOP PRIMARY COOLANT PUMP COASTDOWN *

CLOSE MAIN INTACT LOOP STEAM GENERATOR FEEDWATER VALVE *

CLOSE MAIN BROKEN LOOP STEAM GENERATOR FEEDWATER VALVE *

OPEN AUXILARY INTACT LOOP STEAM GENERATOR FEEDWATER VALVE *

OPEN AUXILARY BROKEN LOOP STEAM GENERATOR FEEDWATER VALVE *

OPEN PRESSURIZER SPRAY VALVE *

TURN OFF STEAM GENERATOR MASS CONTROLLER *

ALWAYS TRUE

OPEN PRESSURIZER RELIEF VALVE *

VALVE OUT TIME DEPENDENT VOLUME PRESSURIZER FOR STEADY STATE *

OPEN STEAM GENERATOR CROSS-OVER LINE VALVE *

CLOSE STEAM GENERATOR CROSS-OVER LINE VALVE *

MONITOR MAXIMUM HEATER ROD TEMP - MAY WANT TO STOP CALCULATION**

TURN OFF PRESSURIZER LEVEL CONTROLLER *

BEGIN USING TEST POWER FOR GUARD HEATER BANK 110 (HOT LEGS) *

BEGIN USING TEST POWER FOR GUARD HEATER BANK 111 (BL PMP SUC) *

BEGIN USING TEST POWER FOR GUARD HEATER BANK 112 (COLD LEGS) *

BEGIN USING TEST POWER FOR GUARD HEATER BANK 113 (IL PMP SUC) *

BEGIN USING TEST POWER FOR VESSEL EXTERNAL HEATERS (BANK 116) *

BEGIN USING TEST POWER FOR PRESSURIZER EXT HEATERS (BANK 117) *

TURN ON PRESSURIZER HEATER RODS *

TURN OFF POWER TO UPPER HEAD HEATERS *

TURN OFF POWER TO UPPER VESSEL.HEATERS *

TURN OFF POWER TO MIDDLE VESSEL HEATERS *

TURN OFF POWER TO VESSEL AND DOWNCOMER HEATERS *

PRESSURE TO OPEN INTACT LOOP STEAM GENERATOR RELIEF VALVE *

PRESSURE TO CLOSE INTACT LOOP STEAM GENERATOR RELIEF VALVE *

UPPER LIMIT ON INTACT LOOP SECONDARY PRESSURE FOR STEADY STATE**

'LOWER LIMIT ON INTACT LOOP SECONDARY PRESSURE FOR STEADY STATE**

RATE TO CLOSE MAIN INTACT LOOP STEAM VALVE FOR STEADY STATE *

RATE TO OPEN MAIN INTACT LOOP STEAM VALVE FOR STEADY STATE *

PRESSURE TO OPEN BROKEN LOOP STEAM GENERATOR RELIEF VALVE *

PRESSURE TO CLOSE BROKEN LOOP STEAM GENERATOR RELIEF VALVE *

UPPER LIMIT ON*BROKEN LOOP SECONDARY PRESSURE FOR STEADY STATE**

LOWER LIMIT ON BROKEN-~LOOP SECONDARY PRESSURE FOR STEADY STATE**

RATE TO CLOSE MAIN-.BROKEN LOOP STEAM VALVE FOR STEADY STATE *

RATE TO'OPEN-MAIN BROKEN LOOP STEAM VALVE FOR STEADY STATE *

STOP CALCULATION *

OPEN STEAM GENERATOR CROSS-OVER LINE VALVE *

TURN OFF POWER TO UPPER HEADi HEATERS *

TURN OFF POWER TO UPPER VESSEL'HEATERS *

TURN OFF POWER TO MIDDLE VESSEL HEATERS *
**643 TURN OFF POWER TO VESSEL AND DOWNCOlMER HEATERS *

**660 RESET INTACT LOOP STEAM RELIEF VALVE FOR HYSTERESIS EFFECTS *

**661 OPEN INTACT LOOP STEAM GENERATOR RELIEF VALVE *

**662 USED IN STEADY STATE CONTROL TO OPEN INTACT LOOP STEAM VALVE *

**663 USED IN STEADY STATE CONTROL TO CLOSE INTACT LOOP STEAM VALVE *

**670 RESET BROKEN LOOP STEAM RELIEF VALVE FOR HYSTERESIS EFFECTS *

**671 OPEN BROKEN LOOP STEAM GENERATOR RELIEF VALVE *

**672 USED IN STEADY STATE CONTROL TO OPEN BROKEN LOOP STEAM VALVE *

**673 USED IN STEADY STATE CONTROL TO CLOSE BROKEN LOOP STEAM VALVE *

*TRIP VR CO PARA RELA VA CO PARA ADD INDX TIMEOF

0000401 TIME 0 GE NULL 0 1000.0 L -1.

0000402 TIME 0 GE NULL 0 9999.0 L -1.

0000403 TIME 0 LT NULL 0 0. L -1.

0000406 TIME 0 GE NULL 0 9999.0 L -1.

0000407 P 999010000 LE NULL 0 1827.5 L -1.

0000408 TIME 0 GE TIMEOF 407 26.3 L -1.

0000409 TIME 0 GE TIMEOF 407 4.6 L -1.

0000410 TIME 0 GE TIMEOF 407 7.3 L -1.

0000411 TIME 0 GE TIMEOF 407 7.3 L -1.

0000412 TIME 0 GE TIMEOF 407 4.7 L -1.

0000413 TIME 0 GE TIMEOF 407 4-.35 L -1.

0000414 TIME 0 GE TIMEOF 407 0.0 L -1.

0000415 TIME 0 GE TIMEOF 407 0.0' L -1.

0000416 TIME 0 LT NULL 0 0.0 L -1.

0000417 TIME 0 LT NULL 0 0.0 L -1.

0000418 TIME 0 LT NULL 0 0. L -1.

0000419 TIME 0 LE NULL 0 50. N -1.

0000420 TIME 0 GE NULL 0 0. L 0.

0000421 P 999010000 GE NULL 0 2305. N -1.

0000422 TIME 0 GE TIMEOF 412 64. L -1.

0000423 TIME 0 GE NULL 0 9988. L -1.

0000424 TIME 0 LT NULL 0 0. L -1.

0000425 TIME 0 LT NULL 0 0. L -1.

0000426 CNTRLVAR 29 GE NULL 0 922.0 N -1.

0000429 TIME 0 LE NULL 0 340. N -1.

0000430 TIME 0 GE TIMEOF 406 0. L -1.

0000431 TIME 0 GE TIMEOF 406 0. L -1.

0000432 TIME 0 GE TIMEOF 406 0. L -1.

0000433 TIME 0 GE TIMEOF 406 0. L -1.

0000436 TIME 0 GE TIMEOF 406 0. L -1.

0000437 TIME 0 GE TIMEOF 406 0. L -1.

0000439 TIME 0 LT NULL 0 0. L -1.

0000440 CNTRLVAR 565 LT NULL 0 +184.0 N -1.

0000441' CNTRLVAR 564 LT NULL 0 +90.0 N -1.

0000442 CNTRLVAR 561 LT NULL 0 -62.0 N -1.

0000443 CNTRLVAR 561 LT NULL 0 -423.0 Ni -1.

0000600 401 426

0000624 424 AND -425 N -1.

0000640 422 AND 440 L -1.

0000641 422 AND 441 L -1.

.0000642 422 AND 442 L -1.

*0000643 422 AND 443 N -1.;

*STEAM GENERATOR RELIEF VALVE TRIPS, INCLUDING.HYSTERESIS EFFECTS

0000460 P 611010000 GT NULL .0 1048.0 N .- 1.

0000461 P 611010000 GT NULL 0 1045.0 N * -1.
0000470 P

0000471 P

705010000 GT

705010000 GT

NULL

NULL

0

0

1048.0 N

1045.0 N

-1.

-1.

*STEAM GENERATOR RELIEF VALVE LOGIC

0000660

0000661

0000670

0000671

461

460

471

470

AND

OR

AND

OR

661

660

671

670

N

N

N

N

-1.

-1.

-1.

-1.

* TRIPS USED FOR CONTROLLING STEAM GENERATOR PRESSURES IN STEADY-STATE *

" ACCEPTABLE PRESSURE BANDS - TRIPS 46Z & 463 (IL) AND 472 & 473 (BL) *

" MAX AND MIN PRESSURE RATE CHANGES - TRIPS 464, 465(IL), 474, 475(BL) *

" OPEN OR CLOSE STEAM VALVES - TRIPS 662 & 663 (IL) AND 672 & 673 (BL) *

0006

0000462

0000463

0000464

00004652

0000662

0000663

0000472

0000473

0000474

0000475

0000672

P 611010000

P 611010000

CNTRLVAR 631

CNTRLVAR 631

.462 AND

463 -AND

P 705010000

P 705010000

CNTRLVAR 731

CNTRLVAR 731

472 AND

473 AND

INTACT LOOP

GE NULL

LE NULL

GT NULL

LT NULL

464 N -1.

465 N. -1.

0

0

0

0

857.7

853.7

-2500.

2500.

N

N

N

N

N

N

N

N

-1.

-1.

-1.

-1.

-1.

-1.

-1.

-1.

BiROKEN LOP

GE NULL

LE NULL

GT NULL

L-T- 'NULL

474 N -1.

475 N -1.

0

0

0

0

857.7

853.7

-2500.

2500.

* INTACT

* LOOP

*

*

*

*

*HOT LEG, VESSEL OUTLET TO PRESSURIZER SURGE LINE TEE*

* REF DRAWINGS: *

*

*

*

HOT LEG NOZZLE - 407986

3 PC-lB (SP-1) - 414684

2.5PC-18 (SP-2) - 407346

2.5PC-2 (SP-3) -. 415155

* INLET ELEV =OUTLET ELEV =+ 8.500 IN.

2000

2010000

2010001

2010102

NAME

C201

TYPE

PIPE

NO VOL

2

AREA

.0396502

.0314314

VOL NO

1

2

* HOT VESSEL NOZZLE (ID = 2.880 IN)

* 3IN SCH 160

LENGTH VOL NO
2010301

2010302

2010501

2010502

2010601

2010701

2010801

2010901

2011001

2011101

2010

2011201

2011300

2011301

2.6425000

2.4716667

HZ ANG

-45.0

-45.0

VR ANG

0.0

ELV CH

0.-0

ROUGH

6.667E-5

F LOSS

0.05

CTIL FLG

0

1

2 * SPOOL PIECES 1 AND 2

VOL NO

VO 1N

2

VOL NO

2

HlY DIA VOL NO

0.0 2

R LOSS

0.05

JUN NO

I.

VOL NO

2

VCAHS 'JUN NO

0 1

CTL

3

3

P .RESS

2258.30

2258.30

CTL FLG

1

TEMP

592. 30

592.30

ZERO

0.0

0.0

ZERO

0.0

0.0

AIR FLG

0

0

VOL NO

1

2

FLOW-F FLOW-G

17.450 0.0

VELJ JUN NO

0.0 1

*HOT LEG -PRESSURIZER SURGE LINE TEE*

* REF DRAWINGS: 2.5PC-2 (SP-3) - 415155

* 2.5PC-6 (SP-4) - 414431

* PRESSURIZER CONNECTION IS HORIZONTAL TO THE HOT LEG CENTER LINE.

* INLET ELEV = OUTLET ELEV =+ 8.500 IN.

2000

2020000

2020001

2020101

2020200

NAME

C202

NO JUN

3

TYPE

BRANCH

CTL

1

AREA LENGTH VOLUME -HZ ANG

.0246289 2.7433333 0.0 0.0

VR ANG ELV CH

0.0 0.0

ROUGH

6.667E-5

CTL PRESS

3 2258.30

HY DIA

0.0

TEMP

592.30.

CTL

0
*FROM TO JUN AREA F LOSS R LOSS VCAHS

2021101 201010000 202000000 .0246289 0.075 0.075 0

2022101 202010000 203000000 .0246289 0.075 0.075 0

2023101 997010000 202000000 7.4667E-4 0.0 0.0 101

*FLOW-F FL0W-G VELJ

2021201 17.450 0.0 0.0

2022201 17.450 0.0 0.0

2023201 0.000 0.0 0.0

*PRESSURIZER TIME DEPENDENT VOLUME (FOR STEADY STATE CALCULATIONS) *

* ELEV =+326.875 IN.

*NAME TYPE

9890000 C989 TMDP VOL

*AREA LENGTH VOLUME HIZ ANG VR ANG ELV CH

9890101 .06926263 10.00 0.0 0.0 0.0 0.0

* .ROUGH HY DIA CTL

-.9890102 .0.0 0.0 0

*CIL FLG

9890200 2

*TIME PRESSURE QUALE

9890201 0.0 2243.73 1.0

*TIME DEPENDENT PRESSURIZER JUNCTION*

* ELEV = +326.875 IN.

*NAME TYPE

9910000 TMD-PRZ VALVE

*FROM TO JUN AREA F LOSS R LOSS VCAHS

9910101 989000000 999000000 .06926263 0.0 0.0 100

*CTL FLOW-F FLOW-G VELJJ

9910201, 1 0.0 0.0 .0.0

* VLV TYPE

9910300 MTRVJJV

*OP TRIP CL TRIP SLOPE INIT POS TABLE

9910301 403 423 0.20 1.0 0

*PRESSURIZER DESIRED LEVEL TIME DEPENDENT JUNCTION.

* FOR STEADY STATE -INPUT FOR GETTING AND MAINTAINING DESIRED LEVEL

* ELEV = 87.000 IN.
9850000

NAME

PZRLVLJ

TYPE

THDPJUN

*FROM TO JUN AREA

9850101 980000000 999010000 .012

9800

9850200

9850202

9850203

CTL FLG

1

TABLE TAKES

KG

-1Q.O -

0.0

10.0

TRIP SEARCH VARIABLE

0 CNTRL VAR 985

INTO ACCOUNT

LB

-22.0462

0.0

22. 0462

CONVERSION OF EG TO LB

0.0

0.0

0.0

0.0

0.0

0.0

*PRESSURIZER DESIRED LEVEL TIME DEP VOLUME - TEMP FROM BOTTOM PZR *

* FOR STEADY STATE - INPUT FOR GETTING AND MAINTAINING DESIRED LEVEL

* ELEV = 87.000 IN.

9800000

9800101

9800102

9800200

9800201

9800202

9800203

9800204

NAME

PZRLVIJV

TYPE

TflDP VOL

AREA -LENGTH

.012 10.00

VOLUME

0.0

HZ ANG

0.0

VR ANG ELV CH

0.0 0.0

ROUGH

0.0

CTL FLG

1

TEMP (F)

80.0

575.0

1340.0

17540.0

HY DIA

0.0

CTL

0

TRIP SEARCH VARIABLE

0 TEMPF 999070000

TEMP (F)

80.0

575.0

1340.0

17540.0

QUALE

0.0

0.0

0.0

0.0

*PRESSURIZER SPRAY TIME DEPENDENT JUNCTION*

* ELEV = +326.875 IN.

9100000

NAME

PZRSPRY

TYPE

TMDPJUN

*FROM TO

9100101 920000000 999000000

JUN AREA

.012

9100200

CTL FLG

I

TRIP

418

*CHECK FLOWS FOR 260

* TIME

9100201 -1.0

9100202 0.0.

9100203 2000.0

- SAME IF

FLOW-F

0.0

0.0

0.0

NORMAL SPRAY

FLOW-G

0.0

0.0

0.0

ONLY

VELJ

0.0

0.0

0.0
*PRESSURIZER SPRAY TIME DEP VOLUME - TEMP FROM INTACT LOOP COLD LEG *

* ELEV = +326.875 IN.

9200000

NAME

PZRSPRV

9200

9200101

*** NORMAL

*9200200

AREA

. 0412

ROUGH

0.0

TYPE

TMDP VOL

LENGTH

10.00

HY DIA

0.0

VOLUME

0.0

HZ ANG

0.0

VR ANG ELV CH

0.0 0.0

GIL

0

SPRAY *****

GIL FLG TRIP SEARCH VARIABLE

1 0 TEMPF 261010000

** TEMP (F)

*9200201 80.0

*9200202 575.0

*9200203 -1.340.0

*9200204 17540.0

***AUXILARY SPRAY

* GIL FLG

9200200 3

ThM]P (F) QUALE

80.0 0.0

575.0 0.0

1340.0 0.0

17540.0 0.0

OR COMBINATION **

9200201

TIME PRESSURE

0.0 1Z.3

TEMP

80.0

*PRESSURIZER PRESSURE RELIEF VALVE*

* ELEV = +326.875 IN.

*NAME TYPE * SIMULATE

9340000 PRSRV VALVE * SRV

*FROM TO

9340101 999000000 940000000

JUN AREA

1. 4748E-5

F LOSS

0.0

R LOSS

0.0

VCAHS

100

9340102

CD1

0.7

CD2

0.84

*CTL FLOW-F

9340201 1 0.0

FLOW-G

0.0

*VELJ

0.0

9340300

9340301

VLV TYPE

TRPVLV

TRIP

421

*PRESSURIZER RELIEF VALVE - TIME DEP DISCHARGE VOLUME*
* ELEY

9400000

9400101

9400102

9400200

9400201

= +326.875 IN.

NAMNE

PRSDV

TYPE

TMDP VOL

AREA LENGTH

10.00 10.00

VOLUME

0.0

HZ PING

0.0

VR PING ELV CH

0.0 0.0

ROUGH

0.0

HY DIA

0.0

CTL

0

CTL fLG

2

TIME

0.0

PRESSURE

1Z.3

QUALE

1.0

*LONG PRESSURIZER*

*

*

*

*

*

*

*

*

*

REF DRAWINGS: 416200

416199

418126

- PZR

- PRZ

-ýPZR

ASSEMBLY

INSTALLATION

THERMAL SHOCK SHIELD FOR SPRAY, NO LINER

VESSEL ID = 3.631 IN, TOTAL INTERIOR HEIGHT = 239.875 IN

BOTTOM OF PRESSURIZER MODEL IS TOP OF HEATER ROD RETAINER

WHICH IS 5.2 INCHES BELOW THE LOW4ER PRESSURE TAP

INCLUDES 6 HEATER RODS 0.75 INCHES DIA.

*TOTAL VOLUME =2417.26 IN3 WITHOUT THERMAL SHIELD

* INLET ELEV = TOP = +326.875 IN.

* OUTLET ELEV =.BOTTON = + 87.000 IN.

9900

9990000

99901001

9990101

9990102

9990103

9990201

9990202

9990203

9990301

9990601

NAME

C999

TYPE

PIPE

NO VOL

8

AREA

0.07190844

0.07190844

0.05350067

AREA

0.07190844

0.07190844

0.05350067

LENGTH

2.500000

2. 562500

2. 583333

2. 093750

VR PING

-90.0

VOL NO

1

7

8 * INCLUDES 6 HTR RODS, GRID PLATE.

JUN NO

1

6

7

VOL NO

1

6

7

8

VOL NO

8
9990701

9990702

9990703

9990704

9990801

9990802

9990803

9990901

9991001

9991103

9991201

9991202

9991203

9991300

9991301

ELV CH

-2.500000

-2.562500

-Z.583333

-2.093750

ROUGH

6.667E-5

6.667E-5

6. 667E-5

F LOSS

0.0

GIL FLO

0

VCAHS

0

VOL NO

1

6

7

8

HY DIA

.2858333

.3025833

.1005325

R LOSS

0.0

VOL NO

8

JUN NO

7

QUALS

1.00

0.0777

0.00

VOL NO

1

7

8

JUN NO

7

GIL

2

2

2

PRESS

2258.30

2258.30

2258.30

ZERO

0.0

0.0

0.0

ZERO

0.0

0.0

0.0

AIR FLG

0

0

0

VOL NO

2

3

8

CTIL FLG

1

FLOW-F

0.0

FLOW-G

0.0

VELJ

0.0

JUN NO

7

*PRESSURIZER VESSEL OUTLET*

*

*

*

*

REF DRAWINGS:

OUTLET 6 HOLES

ELEV = +87.000

416204 & 416205

+ ANNUJLUS AROUND

IN.

GRID PLATE

9980000

NAME

J*998

TYPE

SNGLJUN

*FROM TO JUN AREA

9980101 999010000 997000000 6.1762E-3

F LOSS

0.0

R LOSS VCAHS

0.0 100

-CIL FLOW-F

9980201 1 0.0

FLOW-G

0.0

VELJ

0.0

*PRESSURIZER SURGE LINE*

* REF DRAWINGS: 416119 &.416204

* INLET ELEV = TOP = + 87.000 IN.

* OUTLET ELEV = BOTTOM = + 8.500 IN.

9970000

NAME

G*997

TYPE

PIPE
9970001

9970101

9970102

9970103

9970301

9970302

9970303

9970601

9970602

9970603

9970701

9970702

9970703

9970801

9970802

9970901

9970902

9971001

9971101

9971201

9971300

9971301

NO VOL

3

AREA

6. 1762E-3

7.4667E-4

7.4667E-4

LENGTH

0.5416667

5.64583333

4. 0625600

VR ANG

-90 .0

-90 .0

-5.46

ELV CH

-0.5416667

-5.6458333

-0. 3541667

ROUGH

6.667E-5

6.667E-5

F LOSS

7.8434

7.8434

VOL NO

1

2

3

VOL NO

1

2

3

VOL NO

1

2

3

VOL NO

1

2

3

* INCLUDES HEATER ROD RETAINER

HlY DIA

.0479447

.0308333

R LOSS

7.8434

7.8434

VOL NO

1

3

JUN NO *

*

*

*

TOTAL R' = 1.63E9 M**-4

DIVIDED EQUALLY AMONG

THE TWO JUNCTIONS

K = (R')(2A**2)

CTL FLG VOL NO

0 3

VCAHS

0

CTL PRESS

3 2258.30

CIL FLG

1

FLOW-F

0.0

JUN NO

2

TEMP

592.30

FLOW-U

0.0

ZERO

0.0

ZERO

.0.0

AIR FLU

0

VOL NO

3

VELJ JUN NO

.0.0 2

*HOT LEG PRESSURIZER SURGE LINE TEE TO STEAM GENERATOR INLET*

*

* REF DRAWINGS: *

*

*

*

2.5PC-6 (SP-4)

2.5PC-7 (SP-5)

2.5PC-8 (SP-6)

2.5PC-9 (SP-7)

INLET PLENUM

414431 -

414425

414426

414427

414271 *

*

*

*

INLET ELEV = + 8.500 IN. (HOT LEG CENTERLINE)

OUTLET ELEV = + 73.969 IN. (BOTTOM OF INLET PLENUM)
2000

2030000

20303001

2030101

2030301

2030302

2030303

2030601

2030602

20310603

2031070

2031070

20310703

2030801

NAME

C203

TYPE

PIPE

NO VOL

3

AREA

.0246289

LENGTH

2. 6542072

2.33291ý7

2.1884513

VR ANG

+45.0

+90.0

+45.0

ELV CH

1.3941666

2. 3329167

1. 7286602

ROUGH --6.667E-5

F LOSS

0.075

0.050

VOL NO

3

VOL NO

1

2

3

VOL NO

1

2

3

VOL NO

1

2

3

HY DIA

0.0

R LOSS

0'O 075

0.050

* 2.5 IN SCH-160

* SPOOL PIECES 4,5,6

* SPOOL PIECE 7 & INLET PLENUM CONNECT

VOL NO

3

JUN NO

1

2

CTL FLG VOL NO

0 3

VCAHS

000

CTL

3

3

3

PRESS

2258.30

2258.30

2258.30

GIL FLG

1

JUN NO

2

TEMP

592. 30

592.30

592. 30

ZERO

0.0

0.0

0.0

ZERO

0.0

0.0

0.0

AIR FLU

0

0

0

VOL NO

3

FLOW-F FLOW-G

17.450 0.0

VELJ

0.0

JUN NO

2

* * INTACT LOOP *

* * TYPE-II

* *.-STEAM GENERATOR *

*STEAM GENERATOR INLET*

REIF DRAWING: 414271

* ELEV = +73.969 IN.
2050000

NAME

J205

TYPE

SNGLJUN

*FROM TO JUN AREA

2050101 203010000 210000000 0.024629

F LOSS

6.0

R LOSS

0.0

VCAHS

000

I CTL FLOW-F

2050201 1 17.450

FLOW-G

0.0

VELJ

0.0

*STEAM GENERATOR JNLET PLENUM*

* REFERENCE - TYPE-Il (INTACT LOOP) STEAM GENERATOR PANT-LEG DRWG,

* AND PLENUM DRWG. 414271 (1,2) *NOTE - INLET PLENUM ENTRANCE IS CIRCULAR (DIA=2.125 IN),

* PLENUM TAPERS OUTWARD, NONUNIFORMLY, WITH RISE TO

* TUBE SHEET INLET (INLET PLENUM OUTLET).

* OUTLET IS RECTANGULAR WITH RADIUSED CORNERS.

* INLET ELEV = BOTTOM = + 73.969 IN.

* OUTLET ELEV = TOP = + 81.594 IN.

2100000.

2100101

NAME

C210

TYPE

SNOL VOL

AREA LENGTH VOLUME

0.0 0.6354167 0.0478680

HZ ANG

+90.0

VR ANG ELV CHI

+90.0 0.6354167

* ROUGH HlY DIA

2100102 6.667E-5 0.2805910

*CTL PRESS TEMP

2100200 3 2258.30 592.30

CIL

0

ZERO

0.0

*INTACT LOOP STEAM. GENERATOR TUBE SHEET INLET*

* REF DRAWING: 406416

* INLET ELEV = BOTTOM = + 81.594 IN. (BOTTOM OF TUBE SHEET)

* OUTLET ELEV = TOP = +102.594 IN. (TOP OF TUBE SHEET)

* NAME

2150000 - ILTS-IN BRANCH

IN CTL

2150001

*NO JUN

2

*AREA LENGTH VOLUME HZ ANG VR ANG ELV CHI

2150101 0.019757 1.7500 0.0 . 0.0 90.0 1.7500

2150102

2150200

ROUGH HY DIA *CTL

5.OOOE-6 .06475 0

GIL . PRESS

3 2258.30

TEMP

592.30
*FROM TO JUN AREA

2151101 210010000 215000000 0.019757

2152101 215010000 220000000 0.019757

F LOSS

1.0

0.0

R LOSS

0.0

0.0

VCAHS

100

000

2151201

2152201

FLOW-F

17.450

17.450

FLOW-G

0.0

0.0

VELJ

0.0

0.0

*STEAM GENERATOR TUBE BUNDLE*

* REF DRAWINGS: 413415 & 414271 *

*

*

*

*

*

INLET ELEV = OUTLET ELEV =+102.594 IN. (TOP OF TUBE SHEET)

ELEV

EIJEV

ELEV

LONG TUBE

MIDDLE TUBE

SHORT TUBE

391.24 IN.

364.86 IN.

336.99 IN.

ABOVE TOP OF TUBE SHEET

ABOVE TOP OF TUBE SHEET

ABOVE TOP OF TUBE SHEET

* ELEV MODEL TUBE = 364.490 IN. ABOVE TOP OF TUBE SHEET

*Z00

2200000

NAME

ISGTUB

NO VOL

8

TYPE

PIPE

*AREA VOL NO

2200101 0.019757 8 * 6 TUBES, ID = 0.777 IN

2200301

2200302

2200303

2200304

2200305

2200601

2200602

2200603

2200604

2200701

2200702

2200703

2200704

2200705

2200706

2200801

2200901

2200902

2200903

LENGTH

7.9525000

7.9108334

6. 6920292

7.9108334

7.95Z5000

VR ANG

+90.0

+88.6

-88.6

-90.0

VOL NO

1

3

5

7

8

VOL NO

3

4

5

8

VOL NO

1

3

4

5

7

8

*

*

*

8 VOLUMES AROUND U-TUBES; 4 UP AND

4 DOWN. LENGTHS ARE EQUIVALENT

TO SECONDARY SIDE LENGTHS (C600)

ELV CH

+7.9525000

+7.9108334

+6.5999883

-6.5999883

-7.9108334

-7.9525000

ROUGH HY DIA VOL NO

5.OOOE-6 .06475 8

F LOSS

0.0

0.0

0.0

R LOSS

0.0

0.0

0.0

JUN NO

3

4

7
2201001

2201101

2201201

2201202

2201203

2201204

2201215

2201216

2201217

2201218

2201300

2201301

CTL FLG VOL NO

0 8

CTL, FLG JUN NO

0 7

CTL

3

3

3

3

3

3

3

3

PRESS

2258.30

2258.30

2258.30

2258.30

2258.30

2258.30

2258.30

2258.30

CTL FLO

1

TEMP

592.30

592.30

592.30

592.30

531.30

531.30

531.30

531.30

ZERO

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

ZERO

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

AIR FLG

0

0

0

0

0

0

0

0

VOL NO

1

2

3

4

5

6

7

8

FLOW-F

17.450

FLOW-G

0.0

VELJ

0.0

JUN NO

7

*STEAD]I GENERATOR SECONDARY VOLUME

* REF DRAWINGS: 413463 - ASSEMBLY

* 413357 - FILLERS

406419 - SEPARATOR

413415 - BAFFLE PLATES *

*

*

*

INLET ELEV = 0.000 IN. ABOVE'TOP OF TUBE SHEET

OUTLET ELEV = 436.875 IN. ABOVE TOP OF TUBE SHEET

6000

6000000

60002001

6000101-

6000201

6000202

6000302

6000303

6000401

NAME

ISGSEC

NO VOL

5

TYPE

PIPE

AREA

0.0

AREA

.0583799

.0917866

LENGTH

7.9525000

7.9108334

7.4762500

5. 1558333

VOLUME

1.0038417

0.9402046

0. 8926058

1. 0017945

2. 2709806

VR ANG

+90.0

VOL NO

5

JUN NO

3

4

VOL NO

1

3

4

5

VOL NO

1

2

3

4

5

VOL NO

5

" SINGLE BAFFLE PLATE ALONG FLOW PATH

" BAFFLE PLATE WHICH SUPPORTS TC-TUBE

" VOL BEGINS ABOVE TOP OF TUBE SHEET.

" VOLUMES ARE SEPARATED BY JUNCTIONS

" AT BAFFLE PLATES. (NOT ALL PLATES ARE

" CONSIDERED - SOME ARE WITHIN VOLUMES)
6000701

6000702

6000703

6000704

6000801

6000802

6000803

6001001

6001101

6001201

6001202

6001203

6001204

6001205

6010

6001300

6001302

6001303

6001304

ELV CHI

7.9525000

7.9108334

7.4762500

5.1558333

ROUGH

6.667E-5

6.667E-5

6.667E-5

CTI, FLG

0

VCAHS

100

VOL NO

1

3

4

5

HY DIA

.0884737

.1058911

.6378870

VOL NO

5

JUN NO

4

QUALS

0.02054

0.04054

0.06054

0.06054

0.10000

VOL NO

3

4

5

* BAFFLE PLATES

CTIJ

2

2

2

2

2

PRESS

829.600

829. 600

829.600

829.600

829. 600

ZERO

0.0

0.0

0.0

0.0

0.0

ZERO

0.0

0.0

0.0

0.0.

0.0

AIR FIG

0

0

0

0

0

VOL NO

1

2

3

4

5

CIL- FLG

0

VEL-F

2.800

4.700

5.200

4.000

VEL-G

4.500

7.400

10. 500

11. 700

VELJ

0.0

0.0

0.0

0.0

JUN NO

1

2

3

4

4. + + 4-

*INTACT LOOP STEAM GENERATOR SECONDARY SEPARATOR

* REF DRAWING: 413463

* INLET ELEV =436.875 IN. ABOVE TOP OF TUBE SHEET

* OUTLET ELEV =446.375 IN. ABOVE TOP OF TUBE SHEET

*

6000

6010000

6010101

NAME

ISGDCT

NO JUN

3

TYPE

SEPARATR

CTL

0

AREA LENGTH VOLUM1E

0.0 .7916667 .4508175

HZ ANG VR ANG ELV CH

0.0 90.0 .7916667

* ROUGH

601010Z 6.667E-5

*CTL PRESS

6010200 2 829.600

HY DIA

0.0

QUALS

0.30

CTL

0

6011101

FROM1 TO

601010000 612000000

JUN AREA

.4690572

F LOSS R LOSS CAHS VOIDGF

0.0 0.0 1002 0.50
6012101 601000000 602000000 .4690572

6013101 600010000 601000000 .5353713

0.0 0.0 1002

0.0 0.0 1000

0.15

6011201

6012201

6013201

VEL-F

-2.500

1.000

1.600

VEL-G

1.600

0.0

1.600

VETJJ

0.0

0.0

0.0

*INTACT LOOP STEAD] GENERATOR SECONDARY STEAM] DOME*

* REF DRAWING: 413795

* INLET ELEV = 446.375 IN. ABOVE TOP OF TUJBE SHEET * OUTLET ELEV = 455.360 IN. ABOVE TOP OF TUBE.SHEET

6110000

6110101

6110102

NAME

ISGSD

TYPE

SNGL VOL

AREA LENGTH VOLUME

0.0 .748750 .4249623

HZ ANG VR ANG ELV CH

0.0 90.0 .748750

ROUGH HY DIA

6.667E-5 .5664365

CTL

0

ZERO

0.0 *CTL

6110200 2

PRESS

829 .600

QUALS

1.00

*INTACT LOOP STEAM] GENERATOR SECONDARY DOWNCODIER, (TOP)*

* REF DRAWING: 413463

* INLET ELEV =441.625 IN. ABOVE TOP OF TUBE SHEET * OUTLET ELEV = 375.005 IN. ABOVE TOP OF TUBE SHEET

6020000

6020001

6020101

NAME

ISGSD

NO JUN

1

TYPE

BRANCH

CTL

0

AREA LENGTH VOLUME

0.0 5.5516667 3.0085308

HZ ANG

0.0

VR ANG ELV CH

-90.0 -5.5516667

*ROUGH HY DIA

6020102 6.667E-5 .3369291

*CTL PRESS QUALS

6020200 2 829.600 0.00

CTL

0

*FROM TO JUN AREA

6021101 602010000 603000000- .0819087

F LOSS

0.0

R LOSS

0.0

VCAHS

0

6021201

VEL-F VEL-G

0.4300 -0.3400

VELJ

0.0
*INTACT LOOP STEAM GENERATOR SECONDARY SEPARATOR BYPASS*

* REF DRAWING: 413463

*

*

*

INLET ELEV = 441.625 IN. ABOVE TOP OF TUJBE SHEET

OUTLET ELEV = 460.110 IN. ABOVE TOP OF TUBE SHEET

6100

6120000

6120101

NAME

ISGBY

NO JUN

2

TYPE

BRANCH

CTL

0

AREA LENGTH VOLUME

0.0 1.5404167 .7816260

HZ ANG VR ANG ELV CH

0.0 90.0 1.5404167

*ROUGH HY DIA

6120102 6.667E-5 .6533449

CTL,

0

* CTL PRESS

6120200 2 829.600

QUALS

1.00

6121101

6122101

6121201

6122201

FROM

612010000

602000000

VEL-F

0.0

0.0

TO

611000000

612000000

VEL-G

0.0

0.0

JUN AREA

0.3139546

0.7880455

F LOSS

0.0

0.0

R LOSS

0.0

VCAHS

3

0

VELJ

0.0

0.0

*INTACT LOOP STEAM GENERATOR SECONDARY DOWNCOMER (BOTTOM)*

* REF DRAWINGS: 413363 - ASSEMBLY

414048 - FILLERS

*

*

INLET ELEV = 375.005 IN. ABOVE TOP OF TUBE SHEET

OUTLET ELEV = 0.000 IN. ABOVE TOP OF TUBE SHEET

6030000

6030001

6030101

6030201

6030301

6030302

6030303

6030401

NAME

ISGDCB

NO VOL

4

TYPE

PIPE

AREA

0.0

AREA

0.0292836

LENGTHI

7.4762500

7.9108334

7.9525000

VOLUME

.2211171

VOL NO

4

JUN NO

3

VOL NO

1

3

4

VOL NO

I
6030402

6030403

6030404

6030601

6030701

6030702

6030703

6030801

6030802

6030803

6031001

6031101

6031201

6031202

6031203

6031204

6031300

6031301

.2316581

.2316581

.3322701

VR PING

-90.0

ELV CH

-7.4762500

-7.9108334

-7.9525000

ROOGH

6.667E-5

6.667E-5

6.667E-5

2

3

4

VOL NO

4

VOL NO

1

3

4

HlY DIA

.0128227

.0126981

.02Z01639

VOL NO

1

3

4

CTL, FLG VOL NO

0 4

VCPIHS

0

CTL

2

2

2

2

PRESS

829.600

829.600

829.600

829.600

CTL FJ.G

0

JUN NO

3

QUALS

0.0

0.0

0.0

0.0

ZERO

0.0

.0.0

0.0

0.0

ZERO

0.0

0.0

0.0

0.0

AIR FLG

0

0

0

0

VOL NO

1

2

3

4

VEJL-F VEL-G

6.450 6.100

VELJ JUN NO

0.0 3

*DOWNCOMER - RISER JUNCTION (THRU FLOW DIVIDER)*

* REF DRAWING: 413979, FLOW RESTRICTOR, ADJUSTABLE AREA

* ELEV = 0.0 IN. ABOVE TOP OF TUBE SHEET

6040000

NAME

ISGFS

TYPE

SNGLJUN

* .FROM TO JUN AREA

.6040101 603010000 600000000 .0417818

F LOSS R LOSS VCAHS

0.0 0.0 100

*CTL VEL-F VEL-G

6040201 0 7.500 7.200

VELJ

0.0

*STEAM GENERATOR SECONDARY - TINE DEP FEEDWATER JUNCTION*

* ELEV =0.0 IN. ABOVE TOP OF TUBE SHEET

6100000

NAME

ISGFWJ

TYPE

TMDPJUN
*FROM TO JUN AREA

6100101 620000000 603010000 .012

*CTL FLO TRIP

*6100200 1 414

*6100

*6100201

*6100203

*610O020

TIME

-1.0

0.0

24.0

Z6. 0

FLOW-F

5.6034

5. 6034

5.6034

0.0

FLOW-G

0.0

0.0

0.0

0.0

VELJ

0.0

0.0

0.0

0.0

* FOR STEADY STATE - INPUT FOR KEEPING STEAM GENERATOR MASS CONSTANT,

" PUT IN WHAT GOES OUT STEAM VALVE - (COMMENT OUT CARDS 61002XX ABOVE)

6100200

6100

6100201

6100202

6100203

1 420 CNTRLVAR 610

TABLE TAKES INTO ACCOUNT CONVERSION OF KG TO LB

-10.0 -22.0462 0.0 0.0

0.0 0.0 0.0 0.0

0.1 0.22046 0.0 0.0

10.0 22.0462 0.0 0.0

*STEAM GENERATOR SECONDARY - TIME DEP FEEDWATER VOLUME*

* ELEV =0.0 IN. ABOVE TOP OF TUBE SHEET

6200000

6200101

6200102

6200200

6200201

NAME

ISGFWV

TYPE

TMDP VOL

AREA LENGTH

.012 10.00

VOLUME

0.0

HZ ANG

0.0

VR ANG ELV CH

0.0 0.0

ROUGH

0.0

HY DIA

0.0

CTL

0

CTh FLG

3

TIME PRESSURE

0.0 1250. 0

TEMP

450.0

*STEAM GENERATOR SECONDARY - TIME DEP AUX FEEDWATER JUNCTION*

* ELEV = 0.0 IN. ABOVE TOP OF TUBE SHEET

6150000

NAME

ISGAFWJ

TYPE

THDPJUN

*FROM TO

6150101 625000000 603010000

JUN AREA

.012

6150200

CTL FLO TRIP

1 416

TIME FLOW-F FLOW-G VELJ
6150201

615O020

6150203

-1.0

0.0

2000 .0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

*STEAM GENERATOR SECONDARY - TIME DEP AUX FEEDWATER VOLUME*

* ELEV = 0.0 IN. ABOVE TOP OF TUBE SHEET

6250000

6250101

6250102

6250200

NAME

ISGAFWV

TYPE

TMDP VOL

AREA LENGTH VOLUME

.012 10.00 0.0

HZ ANG

0.0

VR ANG ELV CH

0.0 0.0

ROUGH HY DIA

0.0 0.0

CTL

0

CTh FLG

3

*TIME PRESSURE TEMP

6250201 0.0 900.0 80.0

*STEAM GENERATOR SECONDARY - RELIEF VALVE*

* ELEV = 455.360 IN. ABOVE TOP OF TUBE SHEET

6340000

NAME

ISGRV

TYPE

VALVE * SIMULATE ADV

*FROM TO JUN AREA

6340101 611010000 640000000 .0002592

F LOSS

0.0

R LOSS

0.0

VCAHS

100

* CTL FLOW-F

6340201 1 0.0

FLOW-G

0.0

VELJ

0.0

* VLV TYPE

6340300 TRPVLV

* TRIP

6340301 661

*STEAM GENERATOR SECONDARY - TIME DEP RELIEF DISCHARGE VOLUME*

* ELEV = 455.360 IN. ABOVE TOP OF TUBE SHEET

*NAME TYPE

6400000 ISGRDV THDP VOL

6400101

6400102

AREA

.70584

LENGTH VOLUME

10.0 0.0

HZ ANG

0.0

VR ANG ELV CH

O.-o 0.0

ROUGH HY DIA

0.0 )0

CTL

0
6400200

6400201

CTL FLG

2

TIME

0.0

PRESSURE

12.3

QUALE

1.0

*STEAM GENERATOR SECONDARY - DISCHARGE JUNCTION VALVE*

* ELEV = 455.360,IN. ABOVE TOP OF TUBE SHEET

6350000

NAME

ISGDJ

TYPE

VALVE

*FROM TO

6350101 611010000 650000000

JUN AREA

.007

F LOSS R LOSS VCAHS

Z04.67 204.67 100

* CTL FLOW-F

6350201 1 0.0

FLOW-C

5.6034

VELJ

0.0

* VLV TYPE

*6350300 MTRVLV

* OP TRIP _CL TRIP

*6350301 403 410 --SLOPE INIT P05 - ..TABLE

.33333 0.294088 0

*INPUJT FOR SYSTEMS (COMMENT OUT CARDS 63503XX)

6350300

6350301

STEADY STATE CONTROL

SR VVL V

637

*STEAM GENERATOR SECONDARY - TIME DEP DISCHARGE VOLUME*

* ELEV = 455.360 IN. ABOVE TOP OF TUBE SHEET

6500000

6500101

6500102

6500200

6500201

NAME

ISGDV

TYPE

TIIDP VOL

AREA LENGTH VOLUME

.70584 10.0 0.0

HZ ANG

0.0

VR ANG ELV CH

0.0 0.0

ROUGH

0.0

HlY DIA

0.0

CTL

0

CTL FLG

2

TIME PRESSURE QUPILE

0.0 12.3 1.0

*CROSS CONNECTION - JUNCTION FROM IL STEAM DOME TO CONNECTI.ON PIPE*

* ELEV = 455.360 IN. ABOVE TOP OF TUBE SHEET

NAME TYPE
*6370000

*6370101

*6370201

ILCNJ SNGLJUN

FROM TO JUN AREA

611010000 647000000 0.003003

F LOSS

0.0

R LOSS VCAHS

0.0 000

CTL

0

VEL-F

0.0

VEL-G

0.0

VELJ

0.0

*INTACT LOOP STEAM DOME CROSS CONNECTION PIPE TO BL STEAM DOME*

*

*

*

*

*

*

*

*

*

*

*

INLT EEV 45.30 I. BOV TO O

OUTLET ELEV = 476.165 IN. ABOVE TOP OF

NOTE - CROSS-OVER PIPE SNAKES AROUND:

VERTICALLY DOWN 18.000 FT

HORIZONTALLY OVER 8.000 FT

HORIZONTALLY BACK 6.000 FT

VERTICALLY UP 19.730 FT

HORIZONTALLY OVER 5.000 FT,

HORIZONTALLY FORWARD 2.000 FT,

TUBE SHEET

TUBE SHEET

PART OF 746

PART OF 746

.*6470000

*6470001

*6470101

*6470301

*6470302

*6470303

*6470601

*6470602

*6470603

*6470701

*6470702

*640703

*6470801

**6471001

*6471101

*64712101

*6471202

*6471203

NAME

ILCNP

NO VOL

3

*AREA

.003003

LENGTH

18.0

14.0

19.7304167

VR ANG

-90.0

0.0

+90.0

ELV CH

-18.0

0.0

19.7304167

ROUGH

6.667E-5

CTL FLO

0

VCPAHS

0

TYPE

PIPE

VOL NO

3

VOL NO

1

2

3

VOL NO

1

2

3

VOL NO

3

HY DIA VOL NO

0.0 3

VOL NO

3

JUN NO

2

CTL

2

2

2

PRESS

829.600

829.600

829. 600

QUALS

0.0

0.0

0.0

ZERO

0.0

0.0

0.0

ZERO

0.0

0.0

0.0

AIR FLG

0

*0

0

T OL NO

1

2

3
*6471300

*6471301

CIL FLG

0

VEL-F VEL-G

0.0 0.0

VELJ JUN NO

0.0 2

*STEAM GENERATOR SECONDARY - CONNECTION VALVE TO BROKEN LOOP SECONDARY*

* ELEV = 455.36O-IN. ABOVE TOP OF TUBE SHEET

*6700000

NAME

ILBLC

TYPE

VALVE

**FROM TO JUN AREA

*6700101 647010000 746010000 0.000661

F LOSS

0.0

R LOSS VCAHS

0.0 100

** CTL FLOW-F

*6700201 1 0.0

** VLV TYPE

*6700300 MTRVLV

OP TRIP

*6700301 624

FLOW-G

0.0

VELJ

0.0

CL TRIP

425

SLOPE

1.0

* NTPOS

0.0

TABLE

0

* * -END OF*

* * STEAM GENERATOR *

* * SECONDARY *

*INTACT LOOP STEAM GENERATOR TUBE SHEET OUTLET*

* REF DRAWINGS: 406416 & 414271

*

*

*

INLET ELEV = +102.594 IN. (TOP OF TUBE SHEET)

OUTLET ELEV = + 81.594 IN. (BOTTOM OF TUBE SHEET)

2200

2250000

NAME

ILTS-OT

NO JUN

2

TYPE

BRANCH

CTL,

1

*AREA LENGTH VOLUME

2250101 0.019757 1.7500 0.0

HZ ANG VR ANG ELV CH

0.0 -90.0 -1.7500

*ROUGH HY DIA

2250102 5.OOOE-6 .06475

*CTL PRESS TEMP

2250200 3 2258.30 531.30

CTL

0

2251101

2252101

FROM

220010000

f225010000

TO

225000000

230000000

JUN AREA

0.019757

0.019757

F'LOSS

0.0

0.0

R LOSS

0.0

1.0

VCAHS

000

100
2251201

2252201

FLOW-F

17.450

17.450

FLOW-G

0.0

0.0

VEIJJ

0.0

0.0

*STEAM GENERATOR OUTLET PLENUM*

* REF DRAWING: 414271

* SEE NOTE FOR STEAM GENERATOR INLET PLENUM (C210) *

*

*

*

INLET ELEV = TOP

OUTLET ELEV = BOTTOP = + 81.594 IN.

I= + 73.969 IN.

TYPE

2300000 SNGL VOL

2300101

NAME

C230

AREA LENGTH VOLUME

0.0 0.6354167 0.0478680

HZ ANG

+90 .0

VR ANG ELV CH

-90.0 -0.6354167

*ROUGH HY DIA

2300102 6.667E-5 .2805910

*CTL PRESS TEMP

2300200 3 2258.30 531.30

CTL

0

ZERO

0.0

*STEAM GENERATOR OUTLET*

* ELEY = +73.969 IN.

2350000

NAME

J8

TYPE

SNGLJUN

*FROM TO JUN AREA

2350101 230010000 240000000 0.024629

F LOSS

0.0

R LOSS VCAHS

6.0 000

*CTh, FLOW-F FLOW-G VELJ

2350201 1 17.450 0.0 0.0

*PUMP SUCTION LEG*

*

*

*

*

*

*

*

*

*

*

*

*

*

*

*

REF DRAWINGS: INLET PLENUM -

2.5PC-1O (SP-8) -

2.5PC-11 (SP-9) -

2.5PC-12 (SP-1O) -

2.5PC-13 (SP-11) -

2.5PC-14 (SP-12) -

2.5PC-15 (SP-13) -

2.5PC-16 (SP-14) -

Z.5PC-17 (SP-15) -

2.5PC-18 (SP-16) -

+ 73.969 IN.

ELEV = -110.750 IN. - 9.850 IN.

414271

414428

414425-2

414426-2

414429

414025-1

414026

414027

4140.25-2

414028-

INLET ELEV =

U-BEND BOTTOM

OUTLET ELEV =
2400000

2400001

2400101

2400301

2400302

2400303

2400304

2400305

2400306

2400307

2400308

2400309

2400601

2400602

2400603

2400604

2400605

2400606

2400607

2400701

2400702

2400703

2400704

2400705

Z400706

2400707

2400708

2400709

2400801

2400901

2400902'

2400903

2400904

2401001

2401101

2401201

2401202

2401203

NAMNE

C240

TYPE

PIPE

NO VOL

9

AREA

0. 024629

LENGTH

1. 521784.7

3. 6662500

3.4475000

2. 8958333

3.5076302

1.5219271

1.5219271

3. 5076302

4.2083333

VR PING

-45.0

-90.0

-86.79

-30.0

+30.0

+86.79

+90.0

ELV CHI

-1.1836602

-3.6662500

-3.4475000

-2.8958333

-3.4733333

-0. 7266667

0.7266667

3.4733333

4.2083333

VOL NO

9

VOL NO

1

2

3

4

5

6

7

8

9

VOL NO

1

4

5

6

7

8

9

VOL NO

1

2

3

4

5

6

7

8

9

* 2.5 IN SCH-160

*

*

*

*

*

*

*

*

*

SPOOL PIECE

SP

SP

SP

SP

SP

SP

SP

SP

-8,9,10

-11,12

13 STRAIGHT + 30 DEG BEND

-14 60 DEG OF BEND -14 60 DEG OF BEND -14 STRAIGHT + 30 DEG BEND

-15, 16

ROUGH HY DIA

6.667E-5 0

F LOSS

0.0

0.0

0.0

0.3

R LOSS

0.0

0.0

0.0

0.3

VOL NO

9

JUN NO

1

4

7

8

CTL FLG VOL NO

0 9

CTI2

3

3

3

CTL FLO

0

PRESS

2258.30

2258.30

2258.30

JUN NO

8

TEMP'

531. 30

531.30

531.30

ZERO

0.0

0.0

0.0

ZERO

0-. 0

0.0

0.0

AIR FLG

0

0

0

VOL NO

1

2

3
2401204

2401205

2401206

2401207

2401208

2401209

2401300

2401301

3

3

3

3

3

3

2258.30

2258.30

2258.30

2258.30

2258.30

2258.30

GIL FlG

1

531.30

531.30

531.30

531.30

531.30

531.30

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0

0

0

0

0

0

4

5

6

7

8

9

FLOW-F

17.4,50

FLOW-G

0.0

VELJ

0.0

JUN NO

8

*INTACT LOOP PUMP*

*

*

*

*

INLET ELEV = BOTTOM = - 9.850 IN.

OUTLET ELEV = TOP = 0.000 IN. -- ELEVATION = 4773'-9.25"

2500000

2500101

2500102

NAME

IIJPUMP

TYPE

PUMP

AREA LENGTH

0.0 2.26167

CTL FLG

0

VOLUME

0..05584

HZ ANG

+169.102

VR ANG ELV CH

+90.00 0.8208334

* VOL NO JUN AREA

2500108 240010000 0.015578

* VOL NO JUN AREA

2500109 261000000 3.739E-3

F LOSS

0.0

F LOSS

0.0

R LOSS

0.0

R LOSS

0.0

JUN FLG

0

JUN FLO

20 * ORIFICE

2500200 3

PRESS

2258.30

TEMP

531. 30

* GL FLOW-F FLOW-G.

2500201 1 17.450 0.0

ZERO

0

VETLJ

0.0

VELJ

2500202 0.0

GIL FLOW-F FLOW-C

1 17.450 0.0

*INDEX TAB DATA PHASE DIF TAB

25003011 0 0 0

TOR TAB

-1

SP TAB

0

TRIP

0

REVER

1

M-IN

0.3 250*

2500302

*STOP DATA

2500310

R-SP ISP/RSP

22500.0 0.91843

R-FL

159.8

R-HD

397.0

R-TOR

9.34

R-DEN

62.3

R-M-TR FR-TR3 FR-TR1 FR-TR2 FR-TR4

0 0.0 0 0 0

ELS .TM MX-F-SP MN-R-SP

0.0 0.0 0.0

*CARD CCCXXOO-CCCXX99 SINGLE PHASE PUMP HEAD AND TORQUE CURE SET *SINGLE PHASE 4 QUADRANT HEAD TABLES (HOMOLOGOUS CURVESY

2501100 1 1
2501101 0.000, 1.409 0.174, 1.364

2501102 0.700, 1.224 0.884, 1.093

2501200 1 2

2501201 0.000,-0.650 0.250,-0.475

2501202 0.800, 0.400 0.900, 0.700

2501300 1 3

2501301 -1.000, 2.725 -0.888, 2.470

2501302 -0.257, 1.670 0.000, 1.409

2501400 1 4

2501401 -1.000, 2.725 -0.783, 2.050

2501402 -0.263, 1.270 0.000, 1.057

2501500 1 5,.

2501501 0.000, 0.619 0.226, 0.577

2501502 0.875, 0.759 1.000, 1.000

2501600 1 6

2501601 0.000, 1.057 0.190, 0.888

2501602 0.934, 0.921 1.000, 1.000

2501700 1 7

2501701 -1.000,-0.550 -0.879,-0.275

2501702 -0.117, 0.642 0.000, 0.619

2501800 1 8

2501801 -1.000,-0.550 -0.500,-0.600

*SINGLE PHASE 4 QUADRANT TORQUE TABLES

2501900 2 1

2501901 0.000, 0.540 0.200, 0.590

2501902 0.800, 0.950 0.900, 0.980

2502000 2 2

2502001 0.000,-0.150 0.200, 0.020

2502002 0.800, 0.710 0.900, 0.810

2502100 2 3

2502101 -1.000, 0.620 -0.800, 0.680

2502102 -0.200, 0.490 0.000, 0.540

2502200 2 4

2502201 -1.000, 0.62 -0.800, 0.530

2502202 -0.200, 0.390 0.000, 0.360

2502300 2 5

2502301 0.000,-0.630 0.200,-0.510 2502302 0.800,-0.200 0.900,-0.160

2502400 2 6

2502401 0.000, 0.360 0.200, 0.320

2502402 0.800, 0.050 1.000,-0.130

2502500 2 7

2502501 -1.000,-1.440 -0.800,-1.250

2502502 -0.200,-0.770 0.000,-0.630

2502600& 2 8

2502601 -1.000,-1.440 -0.800,-1.120

2502602 -0.200,-0.310 0.000,-0.150

0.349, 1.354

1.000, 1.000

0.500,-0. 194

1.000, 1.000

-0.739, 2.240

-0.658, 1.760

0.411, 0.569

0.325, 0.831

-0.762, 0.000

0.000,-0.650

0.495, 1.317

0.624, 0.000

-0.492, 1.880

-0.484, 1.500

0.654, 0.612

0.609, 0.807

-0.561, 0.367

0.400,

0.950,

0.400,

0.950,

-0.600,

0.650

0.960

0.220

0.850

0.530

0.600,

1.000,

0.600,

1.000,

-0.400,

0.770

0.870

0.460

0.870

0.460

-0.600, 0.460

0.400,-0.390

1.000,-0.130

0.400, 0.270

-0. 600,-i. 080

-0.600,-0.790

0.150, 0.050

0.600, 0.970

.1:000, 0.000.

0.006, 0:000

0.800, 0.560

-0.400, 0.420

0.600,-0.290

0.600, 0.180

-0.400,-0.920

-0.400,-0.520

0.240, 0.800

0.800, 0.900

MO10, 0.000

0.960, 0.450

*TWO PHASE HEAD MULTIPLIER TABLES

2503000 0

2503001 0.000, 0.000 0.100, 0.0(

2503002 0.300, 0.960 0.400, 0.9~

2503003 0.900, 0.800 0.960, 0.5(

2503100 0

2503101 0.000,-0.170 .0001,-0.l

2503102 0.150, 0.150 0.240, 0.5(

2503103 1.000, 0.000

00

80

00

70

60
*TWO PHASE HEAD DIFFERENCE TABLES

2504100 1 1

2504101 0.000, 0.000 0.100, 0.830

2504102 0.700, 1.010 0.900, 0.940

2504200 1 2

2504201 0.000, 0.000 0.100,-0.040

2504202 0.400, 0.210 0.800, 0.670

2504300 1 3

2504301 -1.000,-1.160 -0.900,-1.240

2504302 -0.600,-2.7,90 -0.500,-2.910

2504303 -0.100,-0.500 0.000, 0.000

2504400 1 4

2504401 -1.000,-1.160 -0.900,-0.780

2504402 -0.600,-0.170 -0.500,-0.080

2504403 -0.100, 0.080 0.000, 0.110

2504500 1 5

2504501 0.000, 0.000 0.200,-0.034

2504502 0.800,-1.190 1.000,-1.470

2504600 1 6

2504601 0.000, 0.110 0.100, 0.130

2504602 0.500, 0.070 0.600,-0.040

2504603 0.900,-0.910 1.000,-1.470

2504700 1 7

2504701 -1.000, 0.000 0.000, 0.000

2504800 1 8

2504801 -1.000, 0.000 0.000, 0.000

*TWO PHASE TORQUE DIFFERENCE TABLES

2504900 2 1

2504901 0.000, 0.540 0.200, 0.590

2504902 0.800, 0.950 0.900, 0.980

2505000 2 2

2505001 0.000,-0.150 0.200, 0.020

2505002 0.800, 0.710 0.900, 0.810

2505100 2 3

2505101 -1.000, 0.620 -0.800, 0.680

2505102 -0.200, 0.490 0.000, 0.540

2505200 2 4

2505201 -1.000, 0.620 -0.800, 0.530

2505202 -0.200, 0.390 0.000, 0.360

2505300 2 5

2505301 0.000,-0.630 0.200,-0.510

2505302 0.800,-0.200 0.900,-0.160

2505400* 2 6

2505401 0.000, 0.360 0.200, 0.320

2505402 0.800, 0.050 1.000,-0.130

2505500 2 7

2505501 -1.000,-1.440 -0.800,-1.250

2505502 -0.200,-0.770 0.000,-0.630

2505600 2 8

2505601 -1.000,-1.440 -0.800,-1.120

2505602 -0.200,-0.310 0.000,-0.150

" PUMP COAST DOWN TABLE IS GENERAL TAB

* USE CONTROL VARIABLES 250 AND 251 TO

*TRIP PARAMETER

0.200, 1.090

1.000, 1.000

0.200, 0.000

0.900, 0.800

-0.800,-1.770

-0.400,-Z.670

-0.800,-0.500

-0.350, 0.000

0.400, -0.650

0.250, 0.150

0.700,-0.Z30

0.500, 1.020

0.300, 0.100

1.000, 1.000

-0.700, -2. 360

-0.250,-1.690

-0.700,-0.310

-0.200, 0.050

0.600,-0.930

0.400, 0.130

0.800,-0.510

0.400,

0.950,

0.400,

0.950,

-0.600,

0.650

0.960

0.220

0.850

0.530

0.600,

1.000,

0.600,

1.000,

-0.400,

0.770

0.870

0.460

0.870

0.460

-0.600, 0.460

0.400,-0.390

1.000,-0.130

0.400, 0.270

-0.600-'-1.080

-0.600,-0.190

LE 250 ISET PUMP SPE-ED.

-0.400, 0.420

0.600, -0. 290

0.600, 0.180

-0.400, -0.920

-0.400, -0.520
2506100

*TABLE TAI(ES

2506101

2506102

2506103

2506104

2506105

2506106

2506107

420 CNTRL VAR 251

INTO ACCOUNT CONVERSION OF

-1.0 20665.000

0.0 0.000

1.0 9.549

100.0 954.930

500.0 4774.297

1000.0 9549.297

3000.0 28647.890

RAD/SEC TO REV/PlIN

*PRESSURIZER SPRAYi LINE TEE - TIM1E DEPENDENT JUNCTION*

* ELEV =0.0 IN.

2600000

2600101

2600200

2600201

2600202

2600203

NAME

PZRSPYT

TYPE

TMDPJUN

FROM TO

261000000 290000000

CTL FLG TRIP

1 418

JUN AREA

.012

*TIME-

-1.0

0.0

2000.0

* FLOW-F0.0

0.0

0.0

-FLOW-G

0.0

0.0

0.0

VELJ

0.0

0.0

0.0

*PRESSURIZER SPRAY LINE - TINE DEPENDENT VOLUME*

* ELEV = 0.0 IN.

2900000

2900101

2900102

2900200'

2900201

NAME

PZRSPYL

TYPE

TMDP VOL

AREA LENGTH

.012 10.00

VOLUME

0.0

HZ PING

0.0

VR ANG

0.0

ELV CH

0.0

ROUGH

0.0

HY DIA

0.0

CTL

0

CTI, FLG

3

TIME PRESSURE

0.0 12.3

TEMP

80.0

*COLD LEG.. .PUMP OUTLET TO ECC INJECTION POINT TEE*

*

*

*

*

*

*

REF DRAWINGS: 3PC-11A

3PC-12

3PC-13

3PC-19A

(SP-19)

(SP-20)

(SP-21)

(SP-22)

412544

404759

404794 OR 3PC-1A - 407718

414684-3
* INLET ELEV = OUTLET ELEV = 0.000 IN.

2610000

2610001

2610101

2610301

2610302

2610601

2610701

NAME

G261

TIPE

PIPE

NO VOL

2

AREA

.0375539

LENGT2H

2.0766667

2. 0766667

VOL NO

2

VOL NO

1

2

VOL NO

2

VOL NO

2

* 3 IN SCH-160 (IDI = 2.624 IN)

*SPOOL PIECE - 19,20 *SP -21 &TO EGG TAP IN SP-22

VR ANG

0.0

ELV GH

0.0

*ROUGH HY DIA VOL NO

2610801 6.667E-5 0 2

* GL FLG VOL NO

ý261-1001 - .0 2--

2611101

VGAHS JUN NO

000 1

* GL PRESS TEMP

2611201 3 2258.30 531.30

ZERO

0.0

ZERO

0.0

AIR FLG

0

VOL NO

2

2610

2611300

GIL FLG

1

FLOW-F FLOW-G

17.450 0.0

VELJ JUN NO

0.0 1

*EGG INJECTION TEE *

* REF DRAWING: 3PC-19A (SP-22) - 414684-3

* INLET ELEV = OUTLET ELEV = 0.000 IN.

262O000

2620001

NAME TYPE

C262 BRANCH

NO JUN

3

GIL

1

*AREA LENGTH

2620101 .0375539 2.0766667 *

*

2620102

*

*

VOLUME HZ ANG VR ANG ELV GH

0.0 202.5 0.0 0.0

GIL

0

ROUGH

6.667E-5

HY DIA

0.0

GIL PRESS TMEMP
2620200 3 2258.30 531.30

2621101

2622101

2623101

2621201

2622201

2623201

FROM

261010000

262010000

400010000

TO

262000000

263000000

2620O00000

JUN AREA

.0375539

.0375539

.004995Z

F LOSS

0.30

0.30

0.0

R LOSS

0.30

0.30

0.0

VCAHS

0

0

20121

FLOW-F

17 .450

17.450

0.0

FLOW-C

0.0

0.0

0.0

VELJ

0.0

0.0

0.0

*ECC LINE*

* INLET ELEV = OUTLET ELEV = 0.000 IN.

* NAME

4000000 ILECCPIPE

TYPE

PIPE

4000001

-4000101

4000301

4000601

4000701

NO VOL

1

AREA VOL NO

.0049952 1.

LENGTH

10.0

VR ANG

0.0

ELV CH

0.0

VOL NO

1

VOL NO

1

VOL NO

1

HY DIA VOL NO

0.0 1

* ROUGH

4000801 6.667E-5

4001001

4001201

CTL FLO

0

CTL PRESS

3 2258.30

VOL NO

1

TEMP

531. 30

ZERO

0.0

ZERO

0.0

AIR FLG VOL NO

0 1

*HPIS - TIME DEP JUNCTION*

* ELEV = 0.0 IN.

4100000

NAME

ILHPISJ

TYPE

TMDPJUN

*FROM .TO

4100101 420000000 400000000

JUN AREA

.0049952

TABLE VOLUJME

4100200 P 262010000

CTL FLO

1

TRIP

408
*PRES(PSIA) FLOW-F FLOW-G VELJ

4100201 -1.0 0.0000 0.0 0.0

4100202 0.0 0.0000 0.0 0.0

4100203 15.0 0.03219 0.0 0.0

4100204 332.25 0.02545 0.0 0.0

4100205 384.51 0.02434 0.0 0.0

4100206 431.70 0.02509 0.0 0.0

4100207 472.88 0.02400 0.0 0.0

4100208 510.39 0.02898 0.0 0.0

4100209 519.09 0.02371 0.0 0.0

4100210 561.93 0.02375 0.0 0.0

4100211 652.46 0.02531 0.0 0.0

4100212 729.93 0.02516 0.0 0.0

4100213 812.43 0.02329 0.0 0.0

4100214 820.29 0.01873 0.0 0.0

4100215 1123.66 0.01480 0.0 0.0

4100216 1158.0 0.01418 0.0 0.0

4100217 1258.0 0.01184 0.0 0.0

4100218 1348.0 0.00968 0.0 0.0

4100219 1407.0 0.00717 0.0 0.0

4100220 1455.0 0.00460 0.0 0.0

4100221 1560.0 0.00 0.0 0.0

4100222 1600.0 0.00 0.0 0.0

*HPIS TIME DEPENDENT VOLUME

* INLET ELEV = OUTLET ELEV =0.000 IN.

*NAKE TYPE

4200000 ILHPISV TMDP VOL

*AREA LENGTH VOL1

UME HZ ANG VR ANG ELV CH

4200101 10.0 10.0 0.0 0.0 0.0 0.0

*ROUGH HY DIA CTL

4200102 6.667E-5 0.0 0

* CTL FLO

4200200 3

*TIME PRESSURE TEMP

4200201 0.0 12.3 80.0

*AGCUMRfLATOR*

* INLET ELEV =BOTTOM = 0.000 IN.

* OUTLET ELEV = TOP =+ 43.066 IN.

*NAME TYPE

4300000 ILACC ACCUM

*AREA LENGTH VOLUME HZ ANG VR ANG ELV CHI

4300101 0.7085 3.5888 0.0 0.0 90.0 3.5888

*ROUGH HY DIA CTL

4300102 6.667E-5 0.0 10
4300200

4301101

4302200

PRESSURE

615 .0

TEMP

80.0

TO JUN AREA F LOSS

400000000 .004995 17227.44

R LOSS

17227.44

VCAHS

000

VLIQ

1. 582

LIQ LEV LNLEN ELEV THICK HTR-FLG TNKRHO TNKCP NIT-K

0 30.0 0 .0574 0 0 0 0

*COLD LEG... .ECC IN~JECTION POINT TO DOWNCOHER INLET*

*REF DRAWINGS: 407986 (DOWNCOMER COLD LEG NOZZLE)

* INLET ELEV = OUTLET ELEV = 0.000 IN.

Z600

2630000

2630001

2630701

NAME

C263

TYPE

PIPE

NO VOL

1

AREA VOL NO

.0396802 I1- 

LENGTH VOL NO

2.1535 1

3 IN.SCH-160 (ID = 2.624 IN)

* COLD LEG DOWNCOMER NOZZLE

VR ANG

0.0

VOL NO

I

ELV CH VOL NO

0.0 1

* ROUGH

2630801 6.667E-5

HY DIA VOL NO

0.0 1

2631001

CTL FLG VOL NO

0 1

*CTh PRESS TEHP

2631201 3 2258.30 531.30

ZERO

0.0

ZERO AIR FL6 VOL NO

0.0 0 1

* * REACTOR VESSEL *

* * SIMULATOR *

*COLD LEG INLET ANNUL US TO DOWNCOMER, TEE*

* REF DRAWINGS: ASSEMIBLY

INNER LINER

OUTER LINER

- 407986 - 407990

- 407991

*

*

INLET ELEV = TOP = + 12.000 IN.

OUTLET ELEV = BOTTOM = - 12.000 IN.
*NAME TYPE

1010000 COLDTEE BRANCH

*NO JUN CTL

1010001 4 1

*AREA LENGTH VOLUME HZ ANG VR ANG ELV CH

1010101 .1056970 2.0000 0.0 0.0 -90.0 -2.0000

*ROUGH HY DIA CTIJ

1010102 6.667E75 .142750 0

*CTL PRESS TEMP

1010200 3 2258.30 531.30

*FROM TO JUN AREA F LOSS R LOSS VCAHS

1011101 101000000 181000000 7.46674E-4 0.0 0.0 100

1012101 101010000 110000000 0.026039 0.0 0.0 0

1013101 263010000 101000000 0.045082 1.5 1.5 001

1014101 363010000 101000000 0.045082 1.5 1.5 001

*FLOW-F FLOW-G VtriJ

1011201 0.5908 0.0 0.0

1012201 22.900' 0.0 0.0

.1013201 17.450 0.0 0.0

1014201 5.840 0.0 0.0

*DOWNCOMER*

* INL~ET ELEV = TOP = - 12.000 IN.

* OUTLET ELEV = BOTTOM = -214.770 IN.

*NAME TYPE

1100000 DCOMER PIPE

* NO VOL

1100001 10

*AREA VOL NO

1100101 0.030975 1 * INCLUDES REDUCING SECTION OF ANNUJLUS

1100102 0.026039 8 * DOWNCONER PIPE

1100103 0.031502 9 * SLANTED PIPE + ENTRANCE HALF ANNULUS

1100104 0.0762104 10 * DISTRIBUTION ANNULUS

*LENGTH VOL NO

1100301 2.260833 1

1100302 1.000833 2

1100303 2.000000 7

1100304 1.465667 8

1100305 1.434751 9

1100306 0.962500 10

*VR PING VOL NO

1100601 -90.0 8

1100602 -55.75 9

1100603 -90.0 10
1100

1100701

1100702

1100703

1100704

1100705

1100706

1100801

1100802

1100803

1100901

11010902

1101090

1101090

11012001

1101101

1101201

1101202

11012103

1101204

1101205

ELV CHI

-2.260833

-1.000833

-2.000000

-1.465667

-1.207667

-0.962500

ROUGH

6.667E-5

6.667E-5

6.667E-5

F LOSS

0.0

1.35

0.0

0.0

CTL FLO

0

VOL NO

1

2

7

8

9

10

HY DIA

0.159535

0.0

0. 111833

R LOSS

0.0

1.35

0.0

0.0

VOL NO

1

9

10

JUN NO

6

7

8

9

* MASS FLOW MEASUREMENT STATION

VOL NO

10

VCAIIS JUN NO

0 9

CTL

3

3

3

3

3

3

3

3

3

3

. PRESS

2258.30

2258.30

2258.30

2258.*30

2258.30

2258.30

2258.30

2258.30

2258.30

2258.30

* TEMP

531. 30

531.30

531.30

531.30

531.30

531.30

531.30

531.30

531.30

531.30

ZERO

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

ZERO

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

AIR FLG -

0

0

0

0

0

0

0

0

0

0

--VOL -N

1

2

3

5

6

7

8

9

10

CTL FLG

1

FLOW-F

22. 900

FLOW-G

0.0

VELJ

0.0

JUN NO

9

*LOW4ER PLENUM*

*

*

*

INLET ELEV =TOP = -214.770 IN.

OUTLET ELEV = BOTTOM =-223.433 IN.

13 00000

1300001

NAME TYPE

LO-PLEN -BRANCH

NO -JUN

3

CTL

1

*AREA LENGTH

1300101 u'.322478 0.721917

VOLUME HZ ANG VR ANG ELV CM

0.0 0.0-- -90.0 -0.72'1917

*ROUGH HY DIA CTL
1300102 6.667E-5 0.229414 0

*CTL PRESS TEMP

1300200 3 2258.30 531.30

*FROM TO JUN AREA F LOSS R LOSS VCAHS

1301101 110010000 130000000 0.0762104 1.0 1.0 100

1302101 130000000 140000000 0.075189 0.0 0.0 100

1303101 130010000 120000000 0.322478 0.0 0.0 000

*FLOW-F FLOW-G VELJ

1301201 22.9,00 0.0 0.0

1302201 22.900 0.0 0.0

1303201 0.0 0.0 0.0

*LOW4ER PLENUM LOW4ER VOLUME*

* INLET ELEV = TOP = -223.433 IN.

* OUTLET ELEV = BOTTOM = -229.033 IN.

*NAME TYPE

1200000 LPLO VOL SNGL VOL

*AREA LENGTH VOLUME. HZ PING VR PING ELV CH

1200101 0.510379 0.466667 0.0 0.0 -90.0 -0.466667

*ROUGH HY DIA CIL

1200102 6.667E-5 0.381247. 0

C IL PRESS TEMP ZERO

1200200 3 2258.30 531.30 0.0

*CORE INLET*

* INLET ELEV = BOTTOM = -214.770 IN.

* OUTLET ELEV -TOP = -195.140 IN.

*NAME TYPE

1400000 CORE-IN SNGL VOL

*AREA LENGTH VOLUME HZ ANG VR ANG ELV CH

1400101 0.075189 1.635833 0.0 0.0 90.0 1.635833

*ROUGH HY DIA GIL

1400102 6.667E-5 0.278329 0

*CTL PRESS TEMP ZERO

1400200 3 2258.30 531.30 0.0

*CORE INLET-JUNCTION*

* ELEV = -195.140 IN.

*NAME TYPE
1450000 COREIN-JUN SNLU SNGLJUN

*FROM TO JUN AREA

1450101 140010000 150000000 0.026780

F LOSS

0.2

R LOSS

0.1

VCAHS

0

*CTL FLOW-F

1450201 1 22.900

FLU W-G

0.0

VELJ

0.0

*AVERAGE CHANNEL*

* INLET ELEV = OTT0M

* OUTLET ELEV = TOP

1500000

1500001

1500101

.1500201

1500301

1500601

1500701

1500801

1500901

1501001

1501101'

1501201

1501202

1501203

1501204

1501205

1501206

1501300

=-195.140 IN. =- 51.140 IN.

TYPE

PIPE

NAME

A-CHNEL

NO VOL

6

AREA VOL NO

0.030376 6

AREA

0.026780

LENGTH

2.0

VR ANG

+90.0

ELV CH

2.0

'JUN NO

5

VOL NO

6

VOL NO

6

VOL NO

6

ROUGH HY DIA

6.667E-5 0.032836

VOL NO

6

JUN NO

5

F LOSS

0.10

CTL FLG

0

R LOSS

0.10

VOL NO

6

VCAHS JUN NO

0 5

CTL

3

.3

3

3

3

3

PRESS

2258.30

2258.30

2258.30

2258.30

2258.30

2258.30

CTL FLG

1

TEMP

531.30

531.30

531.30

591.90

591.90

591.90

ZERO

0.0

.0.0

0.0

0.0

0.0

0.0

ZERO

0.0

0.0

0.0

0.0

0.0

0.0,

AIR FLG

0

0

0

0

0

0

VOL NO

1

2

3

4

5

6

FLOW-F FLOW-G' VELJ JUN NO
1501301 22.900 0.0 0.0 5

*UPPER CORE*

*

*

*

*

INLET ELV = BOTTOM = -51.140 IN

OUTLET ELV = TOP =-39.130 IN

1600

1610000

NAME

UP-CORE

NO JUN

4

TYPE

BRANCH

CTL

1

*AREA LENGTH VOLUME

1610101 0.057859 1.000833 0.0

HZ ANG VR ANG ELV CH

0.0 90.0 1.000833

* ROUGH HY DIlA

1610102 6.667E-5 0.07561

CTL

0

* CTL PRESS

1610200 3 2258.30

TEMP

591.90

'1611101

1612101

1613101

1614101

1611201

1612201

1613201

1614201

150010000

161010000

182010000

186010000

TO

161000000

1620O00000

161010000

161010000

FLOW-G

0.0

0.0

0.0

0.0

JUN AREA

0.026780-

0. 017Z08

0.0016085

0. 004606

F LOSS

0.8

0.0

0.0

.43613

R LOSS

0.8

0.0

0.0

.43613

VCAHS

-000

100

100

100

FLOW-F

22.900

21. 000

0.0

-1.900

VELJ

0.0

0.0

0.0

0.0 *

* CORE OUTLET *

* CORE OUTLET

* INLET ELEV = BOTTOM = - 39.130 IN.

* OUTLET ELEV = TOP = - 6.000 IN.

162O000

1620001

NAME

COREOUT

NO JUN

1

TYPE

BRANCH

CTL

1

*AREA LENGTH VOLUME

1620101 0.045640 -2.760833 0.0

HZ ANG VR ANG ELV CH

0.0 90.0 2.760833

*ROUGH BY DIA

1620102 6.667-E-5 0.120892

CIL

0

* CTL PRESS

1620200 3 2258.30

TEMP

591.90

*FROM TO JUN AREA

1621101 186000000 1620000.00 .0.075341

F LOSS R LOSS VCAHS

.92664 .77720 00003
*FLOW-F FLOW-G VELJ

1621201 0.500 0.0 0.0

*HOT LEG OUTLET TEE*

*

*

*

INLET ELEV = BOTTOM = - 6.000 IN.

OUTLET ELEV = TOP = + 23.000 IN.

1600

1630000

NAME

HOTOUT

NO JUN

4

TYPE

BRANCH

CTL

I

*AREA LENGTH

1630101 0.050621 2.416667

* ROUGH HY DIPI

1630102 6.667E-5 0.143638

VOLUME

0.0

HZ ANG

0.0

VR PiNG ELV CH

90.0 2.416667

CTL

0

16 ,3020 ,0

1631101

1632101

1633101

1634101

1631201

1632201

1633201

1634201

CTL PRESS TEMP

3 2258.30 592.'30

FROM

163000000

163000000

162010000

163010000

FLOW-F

17.450

5.840

21. 500

-2.360

TO

201000000

301000000

163000000

164000000

FLOW-G

0.0

0.0

0.0

0.0

JUN AREA

0. 045082

0.045082

0. 037583

0.056700

*F LOSS

2.5

2.5

0.0

R LOSS

2.5

2.5

3.0

0.0

VCAHS

002

002

000

000

VELJ

0.0

0.0

0.0

0.0

*TOP OF UPPER PLENUMN

*

*

*

*

INLET ELEV = BOTTOM = + 203.000 IN.

OUTLET ELEV = TOP = + 53.600 IN.

1640000

NAME

UPPLEN

TYPE

SNGJJVOL

*AREA LENGTH VOLUME

1640101 0.056700 2.5500 0.0

HZ PING VR PING ELV CHI

0.0 90.0 2.5500

1640102

ROUGH HY DIA

6.667E-5 0.168707

CTL

0

ZERO

0.0 * CTL PRESS

1640200 3 2258.30

TEMP

588.00

*UPPER HEAD TOP VOLUME*
*

*

*

*

INLET ELEV = TOP = +166.760 IN.

OUTLET ELEV = BOTTOM = +132.190 iN.

*GEOMETRY WITH UHI*

* TUBE REMOVED *

1900

1940000

1940101

NAME

UPHUPY

NO JUN

2

AREA

0.061685

TYPE

BRANCH

CTL

1

LENGTH VOLUME HZ PING VR PING ELV CH

2.880833 0.0 0.0 -90.0 -2.880833

*ROUGH HY DIA

1940102 6.667E-5 0.280250

CTL

0

*CTh PRESS

1940200 3 2258.30

* FROM

1941101 194010000 J

1942101 194010000

TEMP

531.30

1941201

1942201

FLOW-F

-0.5908

TO

[83000000

[93000000

FLOW-G

*0.0

.0,0

JUN AREA

2. 19233E-3

0.053694

F LOSS

0.0

0.0

R LOSS VCAHS

0.0

0.0

100

000

VELJJ

*0.0

.0.0

*UPPER HEAD -TOP MID VOLUME*

* * GEOMETRY WITH UHI*

* INLET ELEV = TOP = +132.190 IN. * TUBE REMOVED *

* OUTLET EIJEV = BOTTOM = + 90.750 IN.

1900

1930000

1930101

NAME

TMUPHD

NO JUN

2

TYPE

BRANCH

CmL

I

AREA LENGTH VOLUME

.053694 3.453333 0.0

HZ PING VR PING ELV CH

0.0 -90.0 -3.453333

*ROUGH HY DIA

1930102 6.667E-5 0.206333

CTL

0

. CTL PRESS

1930200 3 2258.30

TEMP

531.30

1931101

1932101

1931201

1932201

FROM

193010000

181010000

FLOW-F

0.0

0.5908

TO

192000000

1930 10000.

FLOW-G

0.0

0.0

JUN AREA

0.052330

7. 46674E-4

F LOSS

0.0

0.0

R LOSS

0.0

0.0

VCAHS

000

100

VELJ

0.0

0.0

*UPPER HEAD MIDDLE VOLUME*
*

*

*

*

INLET ELEV = TOP = + 90.750 IN.

OUTLET ELEV = BOTTOM = + 67.160 IN.

*GEOMETRY WITH UHI*

* TUBE REMOVED *

1900

1920000

NAME

LO -PLEN

NO JUN

2

TYPE

BRANCH

CTL

1

LENGTH

1.965833

* AREA

1920101 0.0523,30

VOLUME

0.0

HZ ANG VR ANG ELV CH

0.0 -90.0 -1.965833

*ROUGH HY DIA

1920102 6.66*7E-5 0.178630

CTL

0

*CIL PRESS

1920200 3 2258.30

TEMP

592. 30

1921101

1922101

1921201

-.1922201;

FROM

192010000

192010000

FLOW-F -0:.0

*0.0

TO

191000000

182000000

FLOW-G

0.0

0.0

JUN AREA

0.049603

0.0016085

F LOSS.

0.0

5000.0

R LOSS

0.0

5000.0

VCAHS

000

000

*VELJ

0.0

0.0

*UPPERHEAD LOW4ER VOLUME*

*

*

INLET ELEV = TOP = + 67.160 IN.

OUTLET ELEV = BOTTOM = + 61.440 IN.

1910000

1910001

1910101

1910301

1910601

1910701

1910801

1911001

NAME

UPHLOV

NO VOL

1

TYPE

PIPE

AREA

0. 049603

LENGTH

0.476667

VR ANG

-90.0

ELV CH

-0. 476667

VOL NO

1

VOL NO

1

VOL NO

1

VOL NO

ROUGH HYlIlA

6.667E-5 0.138401

CTL FLG VOL NO

0 1

VOL NO

1

* CTL PRESS TEMP

1911201 3 2258.30 592.30

ZERO

0.0

ZERO AIR FLG

0.0 0

VOL NO

1
*BYPASS LINE FROM DC UPPER INLET ANNULUS TO UPPER HEAD*

* INL

* OUTI

1810000

1810001

1810101

1810201

1810301

1810302

1810501

1810601

1810701

1810702

1810801

1810901

1811001

1811101

1811201

1811202

1811300

1811301

'T ELEV = BOTTOM + 12.000 IN.

IjET ELEV = TOP = + 90.750 IN.

NAME

BPLINE

NO VOL

2

TYPE

PIPE

AREA

7. 46674E-4

AREA

1. 09978E-4

LENGTH

3 .421917

4.390583

HZ ANG

0.0

VR ANG

90.0

ELV CH

3.421917

3. 140583

VOL NO

2

JUN NO

1

VOL NO

N1O 

2

VOL NO

2

VOL NO

1

2

* INCLUDES HORIZONTAL SECTION

ROUGH HY DIA

5.OOOE-6 0.0

F LOSS R LOSS

2.5700 2.5700

CTL FLG VOL NO

0 2

VCAHS JUN NO

000 1

VOL NO

2

JUN NO

1 * ADJUST TO GET 0.9%

CTL PRESS

3 2258.30

3 2258.30

TEMP

531.30

531.30

ZERO

0.0

0.0

ZERO

0.0

0.0

AIR FLO

0

0

VOL NO

1

2

CTL FLG

1

FLOW-F .FLOW-G

0.5908 0.0

VELJ

0.; 0*

JUN NO

1

*CORE SUPPORT COLUMN(S) - BOTH MODELED AS SINGLE F.LOW. PATH*
* INLET ELEV = TOP = + 67.160 IN.

* OUTLET ELEV = BOTTOM = - 39.130 IN.

*NAME TYPE

1820000 SUPTUB PIPE

* NO VOL

1820001 1

*AREA VOL NO

1820101 0.0016085 1

*LENGTH VOL NO

1820301 8.85750 1

*VR ANG VOL NO

1820601 -90.0 1

*ELV CH VOL NO

1820701 -8.85750 1

*ROUGH HY DIA VOL NO

1820801 5.OOOE-6 01

*CTL FLG VOL NO

1821001 - 0 1

*CTL PRESS TEMP ZERO ZERO AIR FLG VOL NO

1821201 3 2258.30 592.30 0.0 0.0 01

*CONTROL ROD GUIDE TUBE (TOP)*

* INLET ELEV = TOP = +132.190 IN. *OUTLET ELEV = BOTTOM = + 84.200 IN.

*NAME TYPE

1830000 GUITUBI PIPE

* NO VOL

1830001 1

*AREA VOL NO

1830101 2.19233E-3 1

*LENGTH VOL NO

1830301 3.999167 1

*VR ANG VOL NO

1830601 -90.0 1

*ELV CH VOL NO

.1830701 -3.999167 1

*ROUGH HY DIA VOL NO

1830801 5.OOOE-6 0.01

*CTL FLO VOL NO

1831001 0 1
* CTL PRESS

1831201 3 2258.30

TEMP

592.30

ZERO

0.0

ZERO

0.0

AIR FLG

0

VOL NO

1

*CROSS-FLOW VOLUME IN GUIDE TUBE THROUGH DRILL HOLES TO UPPER PLENUM*

*

*

*

INLET ELEV =TOP =+ 84.200 IN.

OUTLET ELEV = BOTTOM = + 23.000 IN.

1800

1840000

NAME

GUITUb2

NO JUN

3

TYPE

BRANCH

CTL

I

* AREA

1840101 2. 19233E-3

LENGTH VOLUME

5.1000 0.0

HZ ANG VR ANG ELV CH

0.0 -90.0 -5.1000

*ROUGH HY DIA

1840102 5.OOOE-6 0.0

CTL

0

* CIL PRESS

1840200 3 2258.30

TEMP

600.00

1841101

1842101

1843101

1841201

1842201

1843201

FROM TO

183010000 184000000

184010000 185000000

184000000 164010000

5/16 IN. DIAMETER HOLES

JUN AREA F LOSS

2.19233E-3 0.0

2.19233E-3 0.0

4.26106E-3 5000.0

CONNECT GUIDE TUBE

R LOSS VCAHS

0.0 0

0.0 0

0.0 2

TO UPPER PLENUM (164)

FLOW-F

2. 3600

2.3600

-1. 4000

FLOW-G

0.0

0.0

0.0

VELJ

0.0

0.0

0.0

*MIDDLE PART OF GUIDE TUBE*

*

*

*

INLET ELEV = TOP = + 23.000 IN.

OUTLET ELEV = BOTTOM = - 6.000 IN.

1850000

1850001

1850101

1850301

1850601

NAME

GUITUB3

NO VOL

1

TYPE

PIPE

AREA

2. 19233E-3

LENGTH

2. 416667

VR ANG

-90.0

VOL NO

1

VOL NO

1

VOL NO

1

ELV CHI VOL NO
1850701 -2.416667 1

*ROUGH HY DIA VOL NO

1850801 5.OOOE-6 0.0 1

*CTL FLG VOL NO

1851001 0 1

*CTL PRESS TEMP ZERO ZERO AIR FLG VOL NO

1851201 3 2258.30 591.90 0.0 0.0 01

*LOWER PART OF GUIDE TUBE (SLOTTED SECTION)*

* REF DRAWING: 408010

* INLET ELEV = TOP = - 6.000 IN.

* OUTLET ELEV = BOTTOM = - 39.130 IN.

*NAME TYPE

1860000 GUISLOT BRANCH

*NO JUN CIL

186000111

*AREA LENGTH VOLUME HZ ANG VR ANG ELV CH

1860101 0.010809 2.760833 0.0 0.0 -90.0 -2.760833

*ROUGH HY DIA CTL

1860102 5.OOOE-6 0.120415 0

*CTL PRESS TEMP

1860200 3 2258.30 591.90

*FROM TO JUN AREA F LOSS R LOSS VCAHS

1861101 185010000 186000000 2.19233E-3 .43613 .43613 100

*FLOW-F FLOW-G VELJ

1861201 -1.4000 0.0 0.0

* * BROKEN *

* * LOOP *

*HOT LEG*

* REF DRAWINGS: HOT LEG NOZZLE - 407975

*1.5ABL-1 (SP-50) - 407670

*1.5ABL-14A (SP-55) - 414670 *1.5ABL-30 (SP-56) - 414671 *1.5ABL-31 (SP-57) - 414672

*. 1.5ABL-32 (SP-58) - 414673

*1.5ABL-33 (SP-59) - 414674

*INLET PLENUM - 414272

* INLET ELEV = + 8.500 IN.

* O'UTLET ELEV = + 71.969 IN.

*NAME TYPE
3010000

3010001

3010101

3010102

3010301

3010302

3010303

3010304

3010305

3010501

3010601

3010602

3010603

3010.604

3010701

3010702

3010703

3010704

3010801

3010901

3010902

3010903

3010904

3011001

3011101

3011201

3011202

3011203

3011204

3011205

3011206

3011300

3011301

BL-HL

NO VOL

6

PIPE

AREA

0.0268943

0.0097643

LENGTH

2. 1725000

2.2101267

2.7245M~3

2.3580833

1. 9753140

HZ ANG

0.0

VR ANG

0.0

+45.0

+90.0

+45.0

ELV CHl

0.0

1.4025000

2.3580833

1.5284935

VOL NO

1

6

VOL NO

1

3

4

5

6

VOL NO

6

VOL NO

3

4

5

6

VOL NO

3

4

5

6

* 3 IN. SCH-160

* 1.5 IN SCH-160

*

*

*

*

*

HOT LEG NOZZLE

SPOOL PIECE -50

SP.-55

SP-56,57,58 &90 BEND OF 55

SP-59, AND INLET PLENUM

ROUGH HY DIA

6.667E-5 0.0

F LOSS R LOSS

0.3 0.3

0.1 0.1

0.8 0.8

0.8 0.8

VOL NO

6

JUN NO

1

2

3

5

CTL

3

3

3

3

3

13

CTL FLG

0

VCPIHS

0

PRESS

2258.30

2258.30

2258.30

2258.30

2258.30

2258.30

CTL FLG

1

VOL NO

6

JUN NO

5

TEMP

592. 30

592.30

592.30

592.30

592. 30

592. 30

ZERO

0.0

0.0

0.0

0.0

0.0

0.0

VELJ

0.0

ZERO

0.0

0.0

0.0

0.0

0.0

0.0

AIR FLG

0

0

0-

0

0

0

VOL NO

3

4

5

6

FLOW-F FLOtq-G

5.8401 0.0

JUN NO

5
*STEAM GENERATOR INLET*

*REF DRAWING: 414272 SH.2

* ELEV = +71.969 IN.

3050000

NAME

J305

TYPE

SNGLJUN

*FROM TO JUN AREA

3050101 301010060 310000000 0.0097643

F LOSS

0.0

R LOSS

0.0

VCAHS

000

* CTL FLOW-F

3050201 1 5.840

FLOW-G

0.0

VELJ

0.0

*STEAM GENERATOR INLET PLENUM

*

*

*

*

*

*

*

*

*

*

*

REFERENCE - TYPE-I I (BROKEN LOOP) STEAM GENERATOR PANT-LEG URWO,

AND PLENUM DRWG. 414272 (1,2)

NOTE - INLET PLENUM ENTRANCE IS CIRCULAR (DIA=1.388 IN),

PLENUM TAPERS OUTWARD, NONUNIF0RMILY, WITH RISE TO

TUBE--SHEET INLET (INLET PLENUM OUTLET).

OUTLET IS RECTANGULAR WITH RADIUSED CORNERS.

INLET ELEV =+ 71.969 IN.

OUTLET ELEV =+ 81.594 IN.

3100000

3100101

NAME

BLSGIP

TYPE

SNGL VOL

AREA LENGTH VOLUME

0.0 0.8020833 .0495847

HZ ANG VR ANG ELV CH

0.0 90.0 0.8020833

*ROUGH HY DIA CTL

3100102 6.667E-5 0.2600218 0

*CTL PRESS TEMP ZERO

3100200 3 2258.30 592.30 0.0

*BROKEN LOOP STEAM GENERATOR TUBE SHEET*

* REF DRAWING: 418972

* INLET ELEV = + 81.594 IN. (BOTTOM OF TUBE SHEET)

* OUTLET ELEV = +102.604 IN. (TOP OF TUBE SHEET)

3100

3150000

NAME

BLTS-IN

NO JUN

2

TYPE

BRANCH

CTh

1

*AREA' LENGTH VOLUME HZ ANG VR PING ELV CH

3150101 0.0060544 1.751830 0.0 0.0 88.07 1.7508333
* ROUGH HlY DIA

3150102 5.OOOE-6 .0620833

*CTL PRESS TEM~P

3150200 3 2250.00 548.00

CTL

0

ZERO

3151101

3152101

3151201

3152201

FROM

310010000

315010000

TO

315000000

320O000000

JUN AREA

0.0060544

0.0060544

F LOSS

0.0

0.0

R LOSS

0.0

0.0

VCAHS

100

000

FLOW-F

7.31.0

7.310

FLOW-G

0.0

0.0

VELJ

0.0

0.0

*STEAM GENERATOR TUBE BUNDLE*

* REF DRAWINGS: 418977 & 418980

* INLET ELEY = OUTLET ELEV = +102.604 IN. (TOP OF TUBE SHEET)

* ELEV LONG TUBE

* ELEV SHORT TUBE

* ELEV MODEL TUBE

= 391.00 IN. ABOVE

= 336.00 IN. ABOVE

TOP OF TUBE SHEET

TOP OF TUBE SHEET

= 363.50 IN. ABOVE TOP OF TUBE SHEET

3200

3200000

NAME

*BSGTUB

NO VOL

8

TYPE

PIPE

* AREA

3200101 6.0544E-3

* LENGTH

3200301 7. 7916667

3200302 7.5000000

3200303 7.5428097

3200304 7. 5000000

3200305 7.7916667

* HZ ANG

3200501 -90.0

* VR ANG

3200601 +90.0

3200602 -90.0

* ELV CH

3200701 +7.7916667

3200702 +7.5000000

3200703 +7.5000000

3200704 -7.5000000

3200705 -7.5000000

3200706 -7.7916667

VOL NO

8

VOL NO

1

3

5

7

8

VOL NO

8

VOL NO

4

8

VOL NO

1

3

4

5

7

8

*

*

*

*

*

VOLUMES 2 & 3, 6 & 7 HAVE LENGTHS

AND ELEVATIONS EQUAL TO THEIR CORRESPONDING SECONDARY SIDE VOLUMES.

VOLUMES 4 & 5 ARE EACH HALF OF THE

180 DEGREE BEND.

*

* ROUGH HY DIA VOL NO
3200801 5.OOOE-6 .06208338 8

3200901

3201001

3201101

3201201

3201202

3201300

3201301

F LOSS R LOSS

0.34 0.34

CTL FLG VOL NO

0 8

CTL FLG JUN NO

0 7

CTL PRESS TEMP

3 2250:00 548.00

3 2250.00 548.00

CTL FLG

1

FLOW-F FLOW-G

7.310 0.0

JUN NO

7

ZERO

0.0

0.0

ZERO

0.0

0.0

AIR FLG

.0

0

VOL NO

4

8

VELJ

0.0

JUN NO

7

*STEAM GENERATOR.. SECONDARY.VOLUME*

REF DRAWINGS: -.ASSEMBLY -. $$$ *SEPARATOR - $$$

.BAFFLE PLATES 7.$$$

*

*

*

INLET ELEV

OUTLET ELEV = 13.000 IN. ABOVE TOP OF TUBE SHEET = 445.375 IN. ABOVE TOP OF TUBE SHEET

7000

7000000

7000001

7000101

7000201

7000202

7000301

7000405

7000401

NAME

BSGSEC

NO VOL

5

TYPE

PIPE

AREA

0.0

AREA

0.0242668

0.0203190

LENGTH

6.7083333

7.5000000

6. 8229167

VOLUME

0.2213819

0.2476839

0.2461911

0.2649840

0.3268035

VR PING

+90.0

VOL NO

5

JUN NO

3

4

VOL NO

1

4

5

VOL NO

1

2

3

4

5

VOL NO

5

* BAFFLE PLATES

* 180 DEG RETURN - TOP OF SHORT TUBE

ELV CH VOL NO
7000701

7000702

7000703

7000802

7000803

7000804

7001001

7001101

7001102

6.7083333

7.5000000

6.8229167

ROUGH

6.667E-5

6.667E-5

6.667E-5

CTL FLO

0

AIgS

100

100

1

4

5

HY DIA

0.0659845

0. 0753070

0. 1934227

VOL NO

3

4

5

VOL NO

5

JUN NO

3

4

QUALS

0.00880

* BAFFLE PLATES

* 180 DEG RETURN

ZERO ZERO AIR FLG VOL NO

0.0 0.0 0 5

* CTL PRESS

7001201 2 876.000

7010

7001300

7001302

.-7001303

7001304

CTL FLG

0

VEL-F

2.4000

3.5000

4-.0000

3.4000

VEL-G

3.4000

4.8000

6.4000

7.6000

VELJ

0.0

0.0

0.0

JUN NO

1

2

3.

4

*BROKEN LOOP STEAM GENERATOR SECONDARY RISER (TOP) (SWIRL VANE) .-

* REF DRAWING: $$$$$$

* INLET ELEV = 445.375 IN. ABOVE TOP OF TUBE SHEET

* OUTLET ELEV = 461.375 IN. ABOVE TOP OF TUBE SHEET

7000

7010000

7010101

NAME TYPE

SWIRL BRANCH

NO JUN

2

CTL

0

AREA LENGTH VOLUME HZ ANG VR ANG ELV CH

0.0 1.3333333 .5794734 0.0 90.0 1.3333333

*ROUGH HY DIA

7010102 6.667E-5 .6944443

*CTL PRESS QUALS

7010200 2 876.000 1.00

CmL

0

ZERO

*FROM TO JUN AREA

7011101 700010000 701000000 .0458694

7012101 701000000 711000000 .0205061

F LOSS R LOSS

50.0 50.0

1.5 1.5

VCAHS

100

00000

7011201

7012201

VEL-F

0.3500

0.0

VEL-G

0. 3300

0.0

VELJ

0.0

0.0
*BROKEN LOOP STEAM GENERATOR PRELIMINARY SEPARATOR*

* REF DRAWING: $$$$$$

*

*

*

INLET ELEV = 461.375 IN. ABOVE TOP OF TUBE SHEET

OUTLET ELEV = 465.875 IN. ABOVE TOP OF TUBE SHEET

7000

7030000

7030101

NAME

BLSGPSP

NO JUN

I

TYPE

BRANCH

CTL

0

AREA LENGTH VOLUME

0.0 0.375 .1534235

HZ ANG

0.0

VR PiNG ELV CH

90.0 0.375

*ROUGH HY DIA

7030102 6.667E-5 .2429779

CTL

0

* CTL PRESS ZERO

7030200 2 876.000

QUALS

1.0

*FROM TO JUN AREA -F.LOSS

..7031101 701010000.:703000000 *...3477297--... 0.0

R LOSS-

..0.0.

VGA AS

-100.

7031201

VEL-F VEL-G

0.3500 0.3500

VELJ

0.0

*BROKEN LOOP STEAM GENERATOR SECONDARY SEPARATOR*

* REF DRAWING: $$$$$$

* INLET ELEV =461.370' IN. ABOVE TOP OF TUBE SHEET * OUTLET ELEV = 465.875 IN. ABOVE TOP OF TUBE SHEET

7040000

NAME TYPE

BSGSEP SEPARATR

* NO JUN

7040001 3

* AREA

7040101. 0.0

* ROUGH

7040102 6.667E-5

CTL

0

LENGTH VOLUME~

0.375 .1002201

HZ ANG VR ANG ELV CH

0.0 90.0 0.375

HY DIA

0.0

CTL

0

ZERO

7040200

7041101

7042101

7043101

CTL PRESS QUALS

2 876.000 1.00

FROM TO

704010000 705000000

704000000 712000000

703000000 704000000

JUN AREA

.0796875

.0032519

.2672536

F LOSS

0.0

50.0

0.0

R LOSS

0.0

50.0

0.0

CAHS

1000

1000

1003

VOIDGF

1.00

0.15

VEL-F VEL-G VELJ
7041201

7042201

7043201

0.3500

0.3500

0.3500

0.3500

0.3500

0. 3500

0.0

0.0

0.0

*BROKEN LOOP STEAN GENERATOR STEAN DONE*

* REF DRAWING: $$$$$$

*

*

*

INLET ELEV = 465.875 IN. ABOVE TOP OF

OUTLET ELEV = 476.125 IN. ABOVE TOP OF

TUBE SHEET

TUBE SHEET

7050000

7050101

NAME

BLSGSD

TYPE

SNGL VOL

AREA LENGTH VOLUME

0.0 .8541667 .0680664

HZ ANG VR ANG ELV CH

0.0 90.0 .8541667

* ROUGH HlY DIA

7050102 6.667E-5 .3836702

CTL

0

7050200

CTL PRESS

2 876.000

QUALS ZERO

1.00 0.0

*BROKEN LOOP STEAM GENERATOR RISER TO DOWNCOMER PIPE - MUFFLER*

*REF DRAWING: ASSEMBY - A *

*

*

*

INLET ELEV = 445.375 IN. ABOVE TOP OF TUBE SHEET

OUTLET ELEV = 411.500 IN. ABOVE TOP OF TUBE SHEET

7100

7110000

7110001

7110101

7110301

NAME

BSGMIJF

NO VOL

1

TYPE

PIPE

AREA

0.0

LENGTH

5.5088494

VOLUME

0.6232431

VR ANG

-30.0

ELY CH

-2.8229167

VOL NO

VOL NO

VOL NO

1

VOL NO

1

*ROUGH HY DIA VOL NO

7110801 6.667E-5 .3989363 1

7111001

CTL FLG

0

VOL NO

1
7111201

CTL PRESS

2 876.000

QIJALS

0.0

ZERO ZERO AIR FLG VOL NO

0.0 0.0 0 1

*BROKEN LOOP STEAD] GENERATOR RISER TO DOWNCODIER PIPE - DRAINS*

*REF DRAWING: ASSEMBY - $$$ *

*

*

INLET ELEV = 461.375 IN. ABOVE

OUTLET ELEV = 411.500 IN. ABOVE

TOP OF TUBE SHEET

TOP OF TUBE SHEET

7120000

7120001

7120101

7120301

71* 0

7120401

7120601

7120701

71210801

7121201

NAME

BSGDRN

NO VOL

1

TYPE

PIPE

AREA

0.0

LENGTH

8.9387346

VOL NO

1

VOL NO

1

*VOLUME ..-,VOL .-NO

0.071834Z 1

VR ANG

-30.0

ELV CH

-4 .15625

VOL NO

1

VOL NO

I

ROUGH HY DIA VOL NO

6.667E-5 .0751667 1

CTIL FLG VOL NO

0 1

CTL PRESS

2 876.000

QUALS

0.0

ZERO ZERO AIR FLG

0.0 0.0 0

VOL NO

1

*BROKEN LOOP STEAM GENERATOR SECONDARY DOWNCOMER (TOP - HORIZONTAL) *

* REF DRAWING: $$$$$$ *

*

*

INLET ELEV = 411.500 IN. ABOVE TOP OF TUBE SHEET

OUTLET ELEV = 411.500 IN. ABOVE TOP OF TUBE SHEET

7130000

7130001

7130101

NAME

BSGDN

NO JUN

3

TYPE

BRANCH

CTL

0

AREA LENGTH VOLUMEL

.0.0 3.1426389 .0366917

HZ ANG

0.0

VR ANG .ELV CH

0.0 0.0
*ROUGH BY DIA

7130102 6.667E-5 .1316182

CTL

0

* CTL PRESS

7130200 2 876.000

7131101

7132101

7133101

7131201

7132201

7133201

FROM

711010000

712010000

713010000

VEL-F

0. 3500

0.0

0.3500

QUALS

1.00

TO

713000000

713000000

714000000

VEL-G

0. 3300

0.0

0.3300

ZERO

JUN AREA

.0120117

.0080362

.0103869

F LOSS

3.5

50.0

0.0

R LOSS

3.5

50.0

0.0

VCAHS

000

000

0

VELJ

0.0

0.0

0.0

*BROKEN LOOP STEAM GENERATOR SECONDARY DOWNCOMER*

* REF DRAWING: ASSEMBLY - $$$

*FILLERS - $$$

* INLET ELEV = 411.500 .* OUTLET ELEV = 6.500

* NAME

7140000 BSGDNC

* NO VOL

7140001 5

*AREA V(

7140101 .0103869

*AREA JI

7140201 .0103869

*LENGTH V(

7140301 4.0891869

7140302 7.5000000

7140303 7. 3391869

IN. ABOVE TOP OF TUBE SHEET

IN. ABOVE TOP OF-TUBE SHEET

TYPE

PIPE

)L NO

5

IN NO

4

)L NO

1

4

5

7140601

7140701

7140702

7140703

7140801

7141001

7141101

VR ANG

-90.0

ELV CHI

-4. 0000

-7.5000

-7.2500

VOL NO

5

VOL NO

1

4

5

ROUGH BY lIlA VOL NO

6.667E-5 0.115 5

CTL FLG

0

AilS

0

VOL NO

5

JUN NO

4
* CTL PRESS

7141201 2 876.000

QUALS

0.0

ZERO ZERO AIR FLG VOL NO

0.0 0.0 0 5

7110

7141300

CTL FLG

0

VEL-F VEL-G

6.9000 6.5900

VEjJJ

0.0

JUN NO

4

*BROKEN LOOP STEAM GENERATOR SECONDARY DOWNCOMER (BOTTOM - HORIZONTAL)*

* REF DRAWING: $$$$$$

INE*LV=650I.ABV O FTB HE

* OINLET ELEV = 6.500 IN. ABOVE TOP OF TUBE SHEET

7100

7150000

7150101

NAME

BSGDNB

NO JUN

3

TYPE

BRANCH

Clih

0

.AREA LENGTH VOLUME

0.0 7.8734167 .0972227

HZ ANG - VR ANG ELV CH0.0 0.0 .0.0

* ROUGH HlY DIA

7150102 6.667E-5 .1302273

*CTL PRESS QUALS

7150200 2 876.000 0.00

CmL

0

ZERO

7151101

7152101

7153101

7151201

7152201

7153201

FROM

714010000

715010000

715000000

VEL-F

0. 3500

0.3500

0.0

TO

715000000

716000000

720010000

VEL-G

0.3300

0.3300

0.0

JUN AREA

.0103869

.0513379

.0103869

F LOSS

0.0

50.0

0.0

R LOSS

0.0

50.0

0.0

VCAHS

000

00001

20002

VELJ

0.0

0.0

0.0

*BROKEN LOOP STEAM GENERATOR RISER BOTTOM VOLUME BELOW FEEDWATER INLET*

* REF DRAWING: $$$$$$

* INLET ELEV = 0.000 IN. ABOVE TOP OF TUBE SHEET

* OUTLET ELEV =13.000 IN. ABOVE TOP OF TUBE SHEET

7100

7160000

NAME

BSGRSB

NO JUN

1

TYPE

BRANCH

CTL

0

AREA LENGTH VOLUME HZ ANG VR-ANG ELV CH
7160101 7160101 0.0 1.083333 .0344994 0.0 9001033 90.0 1.083333

*ROUGH HlY DIA

7160102 6.667E-5 .0659845

CTL

0

*CTIJ PRESS

7160200 2 876.000

QUALS

0.00

ZERO

*FROM TO

7161101 716010000 700000000

JUN AREA

.0242668

F LOSS R LOSS VCAHS

0.0 0.0 100

7161201

VEL-F VEL-G

0.3500 0.3300

VELJJ

0.0

*BROKEN LOOP STEAM GENERATOR BOTTOM FEEDWATER PIPE*

* REF DRAWING: ASSEMBLY - $$$

*

*

*

INLET ELEV = -3.500 IN. ABOVE TOP OF TUBE SHEET

OUTLET ELEV = 6.500 IN. ABOVE TOP OF TUBE SHEET

7200

7200000

7200101

NAME

BSGFED

NO VOL

1

TYPE

PIPE

AREA

.0103869

* LENGTH

7200301 .8333333

VOL NO

1

VOL NO

1

VOL NO

1

VOL NO

1

7200

7200601

VR ANG

90.0

ELV CHI

.8333333

*ROUGH HY DIA VOL NO

7200801 6.667E-5 0.1151

7201001

CTL FLG VOL NO

0 1

*CTL PRESS QUALS

7201201 2 876.000 0.0

ZERO ZERO

0.0 0.0

AIR FLG VOL NO

0 1

*STEAM GENERATOR SECONDARY - MAIN FEEDWATER JUNCTION*

* LV=415I.AOETPO TB HE O ED(O76

*ELEV = 41.5 IN. ABOVE TOP OF TUBE SHEET - BOTOP FEED (TO 726)

7220000

NAME

BSGFWJ

TYPE

TMDPJUN
*FROM TO

7220101 724000000 720000000

*CTL FLG TRIP

*7220200 1 415

JUN AREA

0.004 * BOT FEED

*7200

*7220202

*7220202

*7220204

TIME

-1.0

0.0

24.0

26.0

FLOW-F

0.56119

0. 56119

0. 56119

0.0

FLOW-G

0.0

0.0

0.0

0.0

VELJ

0.0

0.0

0.0

0.0

* FOR STEADY STATE'- INPUT FOR KEEPING STEAM GENERATOR MASS CONSTANT,

* PUT IN WHAT GOES OUT STEAM VALVE - (COMMENT OUT CARDS 71002XX ABOVE)

7200

7220200

7200

7220201

7220202

1 420 CNTRLVAR 710

TABLE TAKES INTO ACCOUNT CONVERSION OF KG TO LB

-10.0 -22.046 0.0 0.0

0.0 0.0 0.0 0.0

0.1 0.22046 0.0 0.0

10.0 22.046 0.0 0.0

*STEAM GENERATOR SECONDARY - MAIN FEEDWATER VOLUME *

7240000

7240101

7240102

7240200

7240201

NAME

BSGFWV

TYPE

TMDP VOL

AREA LENGTH

10.00 10.00

VOLUME

0.0

HZ ANG

0.0

VR ANG ELV CH

0.0 0.0

ROUGH

0.0

HY DIA

0.0

CIL

0

CTL FLG

3

TIME PRESSURE

0.0 1250.0

TEMP

450.0

*BREAK VALVE*

*

*

*

*

TOP FEEDLINE BREAK CONNECTS FROM 727 INLET

BOTTOM FEEDLINE BREAK CONNECTS FROM 720 INLET

*7250000

NAME

BRK-VLV

TYPE

VALVE

**FROM TO JUN AREA

*7250101 720000000 790000000 0.0097643

F LOSS R LOSS VCAHS

0.0 0.0 000

*7250102

*7250201

CD1

0.90

CD2

0.80

CTL FLOW-F

1 0.0

FLOW-G VELJ

0.0 0.0
** VLV TYPE

*7250300 TRPVLV

*7250301

TRIP

402

*CONTAINMENT

* ELEV = 0.000 IN.

*7900000

*7900101

*7900102

*7900200

*7900201

NAME

FEEDCTN

TYPE

TMDP VOL

AREA LENGTH VOLUME HZ ANG

10.0 10.0 0.0 0.0

VR ANG ELV CH

0.0 0.0

ROUGH

0.0

HY DIA

0.0

CTL

0

CIL FLO

2

TIKE PRESSURE -QUALE

0.0 12.3 1.0

*BROKEN LOOP STEAM GENERATOR TOP FEEDWATER PIPE*

* REF DRAWING: $$$$$$

* INLET ELEV =411.500 IN. ABOVE TOP OF TUBE SHEET

* OUTLET ELEV =411.500 IN. ABOVE TOP OF TUBE SHEET

7260000

7260101

NAME

BSGXFD

NO JUN

2

TYPE

BRANCH

CTL

0

AREA LENGTH VOLIME

.0103869 2.0 0.0

HZ ANG

0.0

VR ANG ELV CH

0.0 0.0

* .ROUGH flY DIA

7260102 6.667E-5 0.115

*CIL PRESS QUALS

7260200 2 876.000 0.00

CTL

0

ZERO

* FROM TO JUN AREA F LOSS R LOSS VCAHS

7261101 726010000 714000000

7262101 726000000 727010000

.0103869

.0103869

0.0

0.0

0.0

0.0

000

20002

72GI201

7262201

VEL-F

0.0

0.0

VEL-G

0.0

0.0

VELJ

0.0

0.0
*BROKEN LOOP STEAM GENERATOR TOP FEEDWATER BREAK( PIPE*

*REF DRAWING: ASSEMBLY - $$$ *

*

*

*

INLET ELEV = 411.500 IN.

OUTLET ELEV = 401.500 IN.

ABOVE TOP OF TUBE SHEET

ABOVE TOP OF TUBE SHEET

7200

7270000

7270001

7270101

NAME

BSGTBK

NO VOL

1

TYPE

PIPE

AREA VOL NO

0.0103869 1

LENGTH

0.8333333

VR ANG

+90.0

ELV CH - --+0.8333333

VOL NO

1

VOL NO'

1

VOL NO

1

*ROUGH HY DIA

7270801 6.667E-5 0.115

VOL NO

1

7271001

CTL FLG

0

VOL NO

1

QUALS

0.0 * CTL PRESS

7271201 2 876.000

ZERO ZERO

0.0 0.0

AIR FLG VOL NO

0 1

*STEAM GENERATOR SECONDARY - AUXILARY FEEDWATER JUNCTION*

* ELEV = 411.500 IN. ABOVE TOP OF TUBE SHEET

7280000

NAME

BSGAFWJ

TYPE

TMDPJUN

*FROM TO

7280101 729000000 726000000

JUN AREA

.004

72* O

7280200

7280202

7280206

CTL FLG

1

TIME

-1.0

0.0

2000.0

TRIP

417

FLOW-F

0.0

0.0

0.0

FLOW-G

0.0

0.0

0.0

VELJ

0.0

0.0

0.0

*STEAM GENERATOR SECONDARY - AUXILARY FEEDWATER VOLUME*
* ELEV = 411.500 IN. ABOVE TOP OF TUBE SHEET

7290000

7290101

7290102

7290200

7290201

NAME

BSGAFWV

TYPE

TMDP VOL

AREA LENGTH

10.00 10.00

VOLUME

0.0

HZ ANG

0.0

VR ANG ELV CH

0.0 0.0

ROUGH

0.0

HlY DIA

0.0

CTL

0

CTL FLO

3

TIME PRESSURE

0.0 900.0

TEMP

80.0

*STEAM GENERATOR SECONDARY - RELIEF VALVE

* ELEV = 476.125 IN. ABOVE TOP OF TUBE SHEET

7340000

NAME

BSGRV

TYPE

VALVE

*FROM TO JUN AREA

7340101 705010000 740000000 .007

F LOSS

0.0

R LOSS

0.0

VCAHS

100

*CTh FLOW-F FLOW-G

7340201 1 0.0 0.0

VELJ

0.0

7300

7340300

VLV TYPE

TRPVLV

TRIP

671

*STEAM GENERATOR SECONDARY - TIME DEP RELIEF DISCHARGE VOLUME

*

*

*

ELEV = 476.125 IN. ABOVE TOP OF TUBE SHEET

7400000

7400101

7400102

7400200

7400201

NAME

BSGRDV

TYPE

TMDP VOL

AREA LENGTH VOLUME

10.00 0.0

HZ ANG

0.0

VR ANG ELV CHI

10.0 0.0 0.0

ROUGH

0.0

HY DIA

0.0

CTh

0

CTL FLG

2

TIME

0.0

PRESSURE

12.3

QUALS

1.0
*STEAM GENERATOR SECONDARY - DISCHARGE JUNCTION VALVE*

* ELEV = 476.125 IN. ABOVE TOP OF TUBE SHEET

7350000

NAME

BSGDJ

TYPE

VALVE

*FROM TO

7350101 705010000 750000000

JUN AREA

0.007

F LOSS R LOSS

1022.36 1022.36

VCAHS

100

* ~CTL FLOtI-F

7350201 1 0.0

FLOW-G

0.56119

VELJ

0.0

*7350300

VLV TYPE

1ITRVLV

*OP TRIP CL TRIP SLOPE INIT POS TABLE

*7350301 403 411 0.2 .04367422 0

*INPUTf FOR

7350300

7350301

STEADY STATE CONTROL

SR VVT2V

737.

SYSTEMS (COMMENT OUT CARDS 73503XX ABOVE)

*STEAM-GENERATOR SECONDARY - TIME DEP DISCHARGE VOLUME*

*ELEV = 476.125 -IN.:. ABOVE, TOP OF -TUBE SHEET

7500000

7500101

7500102

7500200

7500201

NAME

BSGDV

TYPE

TM1DP VOL

AREA LENGTH VOLUME

10.0 10.00 0.0

HIZ ANG

0.0

VR ANG

0.0

ELV CH

0.0

ROUGH

0.0

HY DIA

0.0

CIL

0

CTL FLG

2

TIME PRESSURE

0.0 12.3

QUALS

1.0

*CROSS CONNECTION - JUNCTION TO CROSS CONNECTION PIPE FROM BLSG*

* ELEV = 476.125 IN. ABOVE TOP OF TUBE SHEET

*7370000

NAME

BLCNJ

TPYE

SNGIJJUN

**FROM TO

*7370101 705010000 746000000

**CTL VEL-F VEL-G

*7370201 0 0.0 0.0

JUN AREA

0.003003

F ItOSS

0.0

R LOSS VCAHS

0.0 100

VELJ

0.0
*BROKEN LOOP STEAM DOME CROSS CONNECTION PIPE TO IL STEAM DOME*

* INLET ELEV = OUTLET ELEV = 476.125 IN. ABOVE TOP OF TUBE SHEET *

*

*

*

*

*

*

*

NOTE - CROSS-OVER PIPE SNAKES AROUND:

HORIZONTALLY BACK 2.000 FT

HORIZONTALLY OVER 5.000 FT

VERTICALLY DOWN 18.000 FT,

HORIZONTALLY FORWARD 6.000 FT,

HORIZONTALLY OVER 8.000 FT,

VERTICALLY UP 19.730 FT,

PART

PART

PART

PART

OF

OF

OF

OF

647

647

647

647

*7460000

*7460001

*746010 1

*7460301

*7460601

*7460701

*7460801

*7461001

NAME

BLCNP

TYPE

PIPE

NO VOL

1

AREA VOL NO

.003003 1

LENGTH

7.0

VR ANG

0.0

ELV CH

0.0

ROUGH

6.667E-5

*VOL NO

VOL NO

1

VOL NO

1

HY DIA

0.0

VOL NO

1

CTIL FLG VOL NO

0 1

**CTL PRESS QUALS

*7461201 2 675.900 0.0

ZERO

0.0

ZERO

0.0

AIR FLG

0

VOL NO

1

*BROKEN LOOP STEAM GENERATOR TUBE SHEET OUTLET*

* REF .DRAWING: 418972 *

*

*

*

INLET ELEV = +102.604 IN. (TOP OF TUBE SHEET)

OUTLET ELEV = + 81.594 IN. (BOTTOM OF TUBE SHEET)

3200

3250000

NAME

BLTS-OT

NO JUN

2

TYPE

BRANCH

CTL

I

*AREA LENGTH

3250101 6.0544E-3 1.751830

VOLUME

0.0

HZ ANG VR ANG 'ELV CHI

0.0 -88.07 -1.7508333
*ROUGH HY DIA

3250102 5.OOOE-6 .06208333

GIL

0

* CTL PRESS ZERO

3250200 3 2250.00

TEMP

547.00

3251101

3252101

3252201

FROM

320010000

325010000

TO

325000000

330000000

JUN AREA

6. 0544E-3

6. 0544E-3

F LOSS

0.0

0.0

R LOSS

0.0

0.0

VCAHS

000

100

FLOW-F

7.310

7.310

FLOW-G

0.0

0.0

VEILJ

0.0

0.0

*STEAM GENERATOR OUTLET PLENUM*

* REF DRAWING: 414272, SH.2, SEE NOTE FOR SG INLET PLENUM (C310)

* INLET ELEV = TOP = + 81.594 IN.

* OUTLET ELEV = BOTTOM = + 71.969 IN.

* NAME

3300000 ST-OUTPL

TYPE

SNGL VOL

3300101

AREA LENGTH

0.0 0.8020833

VOLUME

.0495847

HZ PING VR ANG ELV CH

0.0 -90.0 -0.8020833

*ROUGH IiY DIA

3300102 6.667E-5 0.2600218

*CTL PRESS TEMP

3300200 3 2258.30 531.30

GIL

0

ZERO

0.0

*STEAM GENERATOR OUTLET*

* ELEV = +71.969 IN.

* NAME

3350000 SG-TO-PS

TYPE

SNGLJUN

*FROM TO JUN AREA

3350101 330010000 340000000 0.0097643

F LOSS R LOSS VCAHS

0.0 0.0 000

* GL FLOW-F FLOW-G

3350201 1 5.840 0.0

VELJ

0.0 *

*PUMP SUCTION LEG

* REF DRAWINGS:

*

INLET PLENUM

1.5ABL-34 (SP-60)

1.5ABL-35 (SP-61)

1.5ABL-36 (SP-6Z)

1.5ABL-37 (SP-63)

1.5ABL-6A (SP-64)

414272

414675-1

414676-1

414672-2

414673-2

414677-1
* INLf

* U-TI

* OUTI

3400000

3400001

3400101

3400301

3400302

3400303

3400304

3400305

3400306

3400307

3400308

3400309

3400501

3400601

3400602

3400603

3400604

3400605

3400701

3400702

3400703

3400704

3400705

3400706

3400707

3400708.

3400709

3400801

3400901

3400902

3400903

3400904

3401001

1.-5ABL-7

1. 5ABL-9

1.5ABL-11

(SP-65) - 407384-1

(SP-72) - 407380-1

(SP-73) - 407673-1

~T ELEV = + 71.969 IN.

JBE BOTTOM ELEV = -110.155 IN.

1ET ELEV = - 10.640 IN.

NAME

BL-PS

NO VOL.9

TYPE

PIPE

AREA

0.0097643

LENGTH

1.6054810

2.3393333

1.6437500

4.9431250

4.2964583

1.0157816

1.0157816

5.3495833

2.2966667

HZ ANG

0.0

VR ANG

-45.0

-90.0

-45.0

+45.0

+90.0

ELV CH

-1.3076602

-2. 3393333

-1.6437500

-4. 9431250

-4.2964583

-0.6466667

+0.6466667

+5.3495833

+2.Z2966667

.ROUGH

6.667E-5

VOL NO

9

VOL NO

1

2

3

4

5

6

7

8

9

VOL NO

9

VOL NO

1

5

6

7

9

VOL NO

1

2

3

4

5

6

7

8

9

HY DIA

0.0

R LOSS

0.0

0.0

0.0

1.3

* 1 1/2 IN SCH-160

*

*

*

*

*

*

*

*

*

SPOOL PIECE-6O AND INLET PLENUM

SP-61,6Z

SP-63 & 64 TO PRESSURE TAP

SP-64

SP-64 & 65 TO BEND OF U

SP-65 1/2 OF BEND

SP-65 1/2 OF BEND

..SP-65,72

SP-73

F LOSS

0.0

0.0

0.0

1. 3

VOL NO

9

JUN NO

7

8

CTL FLG' VOL NO

0 9
3401101

3401201

3401202

3401203

3401204

3401205

3401206

3401207

3401208

3401209

3401300

3401301

CTL FLG JUN NO

0 8

CTJJ

3

3

3

3

3

3

3

3

3

PRESS

2258.30

2258.30

2258.30

2258.30

2258.30

2258.30

2258.30

22581.30

2258.30

TEMP

531.30

531.30

531.30

531.30

531.30

531.30

531.30

531.30

531.30

ZERO

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

ZERO

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

AIR FLG

0

0

0

.0

0

0

0

0

0

VOL NO

1

2

3

4

5

6

7

8

9

CIL FLG

1

FLOW-F FLOW-G

5.840 0.0

VELJ

0.0

JUN NO

8

*BROKEN LOOP PUMP*

--INLET ELEV =BOTTOM

* OUTLET ELEV = TOP

10.64Oa.IN. -

=0.000 IN. -- ELEVATION = 47731-9.25't

3500000

3500101

3500102

3500108

3500109

3500200

3500201

3500202

* INDEX

3500301

3500302

3500303

NAME

BLPUMP

TYPE -- PUMP

AREA LENGTH VOLUME

0.0 1.9635 0.03035

HZ ANG VR ANG ELV CH

0.0 90.0 0.8866667

CTL FLG

0

VOL NO JUN AREA F LOSS

340010000 0.0097643 0.0

VOL NO JUN AREA F LOSS

361000000 0.0011946 0.0

R LOSS

0.0

R LOSS

0.0

JUN FLO

0

JUN FLG

20

CTL

3

PRESS

2258.30

CTL FLOW-F

1 5.840

CTL FLOW-F

1 5.840

TEMP

531.30

FLOW-G

0.0

FLOW-G

0.0

ZERO

0

VELJ

0.0

VELJ

0.0

TAB DATA PHASE

0 0

R-SP -ISP/RSP

15250.0 0.90079

DIF TAB TOR TAB SP TAB TRIP

0 -1 - 0 0

RE'JER

1

M-IN

0.22

R-FL R-HD

51.3 261.0Q

R-TOR

2.2

R-DEN

62.3

R-M-TR FR-TR3

0 0.0

FR-TR1 FR-TR.' FR-TR4

0 0 - 0
*STO~P DATA ELS TM MX-F-SP MNl-R-SP

3500310 0.0 0.0 0.0

*CARD CCCXXOO-CCCXX99 SINGLE PHASE PUMP HEAD AND TORQUE CURVE SET *SINGLE PHASE 4 QUADRANT HEAD TABLES (HOMOLOGOUS CURVES)

3501100 1 1

3501101 0.000,1.7821 .2845,1.7059

3501102 1.000, 1.000

3501200 1 2

3501201 0.000,-1.6359 0.713, 0.000

3501300 1 3'

3501301 -1.000, 1.500 -0.800, 1.275

3501302 0.000, 1.200

3501400 1 4

3501401 -1.000, 1.500 -0.800, 1.150

3501402 -0.200, 0.775 0.000, 0.725

3501500 1 5

3501501 0.000, 0.975 0.500, 1.350

3501600 1 6

3501601 0.000, 0.725 0.200, 0.725

3501602 1.000, 1.950

3501700 1 7

3501701,-1.000, 0.175 -0.500, 0.650

3501800- .1. 8

3501801 -1.000, 0.175 -0.750,-0.150

3501802 0.000,-0.350

*SINGLE PHASE 4 QUADRANT TORQUE TABLES

3501900 2 1

3501901 0.000, 0.540 0.200, 0.590

3501902 0.800, 0.950 0.900, 0.980

3502000 2 2

3502001 0.000,-0.150 0.200, 0.020

3502002 0.800, 0.710 0.900, 0.810

3502100 2 3

3502101 -1.000, 0.620 -0.800, 0.680

3502102--0.200, 0.490 0.000, 0.540

3502200 2 4

3502201 -1.000, 0.62 -0.800, 0.530

3502202 -0.200, 0.390 0.000, 0.360

3502300 2 5

3502301 0.000,-0.630 0.200,-0.510

3502302 0.800,-0.200 0.900,-0.160

3502400. 2 6

3502401 0.000, 0.360 0.200, 0.320

3502402 0.800, 0.050 1.000,-0.130

3502500 2 7

3502501 -1.000,-1.440 -0.800,-1.250

3502502 -0.200,-0.770 0.000,-0.630

3502600 2 8

3502601 -1.000,-1.440 -0.800,-1.120

3502602 -0.200,-0.310 0.000,-0.150

*TWO PHASE HEAD MlULTIPLIER TABLES

3503000 0

3503001 0.000, 0.000 0'.100, 0.000

0.569, 1.627 ..8535,1.1878

.8271,

-0.600,

.2959

1.375

1.000,

-0.400,

1.000

1.375

-0.600, 0.950

1.000,

0.400,

1.950

0.800

-0.400, 0.830

0.600, 1.025

-0. 275,-0.400

0.000, 0.975

0O.550,-0.300

0.400,

0.950,

0.400,

0.950,

-0.600,

0.650

0.960

0.220

0.850

0.530

0.600,

1.000,

0.600,

1.000,

-0.400,

0.770

0.870

0.460

0.870

0.460

-0.600, 0.460

0.400,-0.390

1.000,-0. 130

0.400, 0.270

-0.600,-1.080

-0.600,-0.790

-0.400, 0.420

0.600,-0.290

0.600, 0.180

-0.400,-0.920

-0.400,-0.520

0.150, 0.050 020.240, 0.800 .0
3503002

3503003

3503100

3503101

3503102

3503103

0.300, 0.960

0.900, 0.800

0

0.000,-0.170

0.150, 0.150

1.000, 0.000

0.400, 0.980

0.960, 0.500

.0001,-0.170

0.240, 0.560

0.600, 0.970

1.000, 0.000

0.006, 0.000

0.800, 0.560

0.800, 0.900

0.100, 0.000

0.960, 0.450

*TWO PHASE HEAD DIFFERENCE TABLES

3504100 1 1

3504101

3504102

3504200

3504201

3504202

3504300

3504301

3504302

3504303

3504400

3504401

3504402

3504403

3504500

3504501

.3504502

3504600

3504601

3504602

3504603

3504700

3504701

3504800

3504801

0.000, 0.000

0.700, 1.010

1 2'

0.000, 0.000

0.400, 0.210

1 3

-1.000,-1.160

-0.600,-2.790

-0.100,-0.500

1 4

-1.000,-1.160

-0.600,-0.170

-0.100, 0.080

1 5

0.000, 0.000

0.800,-1.190

1 6

0.000, 0.110

0.500, 0.070

0.900,-0.910

1 7

-1.000, 0.000

1 8

-1.000, 0.000

0.100, 0.830

0.900, 0.940

0.100,-0.040

0.800, 0.670

-0. 900,-1. 240

-0.500,-2.910

0.000, 0.000

-0.900,-0.780

-0.500,-0.080

0.000, 0.110

0.200,-0.034

0.100, 0.130

0.600,-0.040

1.000,-1.470

0.000, 0.000

0.000, 0.000

0.200, 1.090

1.000, 1.000

0.200, 0.000

0.900, 0.800

-0.800,-1.770

-0.400, -2.670

-0.800, -0. 500

-0.350, 0.000

0.400,-0.650

0.250, 0.150

0.700, -0. 230

0.500, 1.020

0.300, 0.100

1.000, 1.000

-0.700,-2.360

-0.250,-1.690

-0.700,-0.310

-0.200, 0.050

0.600,-0.930

0.400, 0.130

0.800,-0.510

*TWO PHASE TORQUE DIFFERENCE TABLES

3504900 2 1

3504901. 0.000, 0.540

3504902 0.800, 0.950

3505000 2 2

3505001 0.000, -0.150

3505002 0.800, 0.710

3505100 2 3

3505101 -1.000, 0.620

3505102 -0.200, 0.490

3505200. 2 4

3505201 -1.000, 0.620

3505202 -0.200, 0.390

3505300 2 5

3505301 0.000,-0.630

3505302 0.800, -0.200

3505400 2 6

3505401 0.000, 0.360

3505402 0.800, 0.050

3505500 2 7

3505501 -1.000, -1.440

3505502 -0.200,-0.7,70

35056GO 2 8

3505601 -1.000,-1.440

0.200, 0.590

0.900, 0.980

0.200, 0.020

0.900, 0.810

-0.800, 0.680

0.000, 0.540

-0.800, 0.530

0.000, 0.360

0.200,-0.510

0.900,-0.160

0.200, 0.320

1.000,-0.130

-0.800,-1;250

0.000,-0.630

0.400, 0.650

0.950, 0.960

0.400, 0.220

0.950, 0.850

-0.600, 0.530

-0.600, 0.460

0.400,-0.390

1.000,-0.130

0.400, 0.270

-0.600,-1.080

0.600, 0.770

1.000, 0.870

0.600, 0.460

1.000, 0.870

-0.400, 0.460

-0.400, 0.420

0.600,-0.290

0.600, 0.180

-0.400, -0. 920

-0.800,-1.120 -0.600,-0.790 *-0.400,-0..520
3505602 -0.200,-0.310 OO0-.5 0.000,-0.150

* PUMP COASTDO14N TABLE IS GENERALJ TABLE 350

* USE CONTROL VARIABLES 350 AND 351 TO SET PUMP SPEED.

3506100

*TABLE TAKES

3506101

3506102

3506103

3506104

3506105

3506106

3506107

TRIP PARAMETER

420 CNTRLVAR 351

INTO ACCOUNT CONVERSION OF

-1.0 16560.000

0.0 0.000

1.0 9.549

100.0 954.930

500.0 4774.297

1000.0 9549.297

3000.0 28647.890

RAP/SEC TO REV/MIN

*PUMP DISCHARGE PIPE AND ECC INJECTION TEE*

* REF DRAWING: 1.5ABL-12 (SP-74) - 407674

* INLET ELEV =OUTLET ELEV = 0.000 IN.

*NAME TYPE

3610000 .PiIP-DISC BRANCH.

3610001

3610101

3610102

NO JUN

2,

cmL

1

AREA LENGTH VOLUME

0.0097643 1.9700 0.0

HZ ANG

0.0

VR ANG

0.0

ELV CH

0.0

ROUGH

6.667E-5

HY DIA

0.0

CIL

0

* GL PRESS TEMP

3610200 3 2258.30 531.30

* FROM TO JUN AREA F LOSS R LOSS VCAHS

3611101 361010000 3620O00000

3612101 500010000 361000000

.0097643

.002695

1.2

0.0

1.2

0.0

000

20121

3611201

3612201

FLOW-F

5.840

0.0

FLOW-G

0.0

0.0

VELJ

0.0

0.0

*ECC LINE*

* INLET ELEV = OUTLET ELEV = 0.000 IN.

* NAME

5000000 BLECCPIPE

TYPE

PIPE

5000001

NO VOL

1

AREA VOL NO
5000101 0.002695 1 * 0.703 IN. ID

*LENGTH VOL NO

5000301 10.0 1

* VR PING VOL NO

5000601 0.0 1

* ELV CHI VOL NO

5000701 0.0 1

*ROUGH HY DIA VOL NO

5000801 6.6679-5 0.0 1

*CTL FLG VOL NO

5001001 0 1

*CTL PRESS TEMP ZERO ZERO AIR FLG VOL NO

5001201 3 2258.30 531.30 0.0 0.0 01

*HPIS INJECTION JUNCTION*

* ELEV = 0.000 IN.

*NAME TYPE

5100000 BLHPISJ TMDPJUN

*FROM -- TO JUN=AREA

5100101 520000000 500000000 0.002695

*CIL FLG TRIP TABLE VOLUME

5100200 1 408 P 361010000

*PRES(PSIA) FLOW-F FLOW-G VELJ

5100201 -1.0 0.00 0.0 0.0

5100202 0.0 0.00 0.0 0.0

5100203 15.0 0.0125 0.0 0.0

5100204 333.57 0.01113 0.0 0.0

5100205 581.36 0.01000 0.0 0.0

5100206 609.77 0.00974 0.0 0.0

5100207 770.0 0.00868 0.0 0.0

5100208 881.0 0.00795 0.0 0.0

5100209 1007.23 0.00705 0.0 0.0

5100210 1024 *0 0.00683 0.0 0.0

5100211 1158:0 0.0059 0.0 0.0

5100212 1258.0 0.0051 0.0 0.0

5100213 1348.0 0.0039 0.0 0.0

5100214 1407.'0 0.*0031 0.0 0.0

5100215 1455.0 0.0019 0.0 0.0

5100216 11560.0 0.00 0.0 0.0

5100217 1600.0 0.00 0.0 0.0

*HPIS VOLUME*

* ELEV = 0.000 IN.
5200000

5200101

5200102

5200200

5200201

NAME

BLHPISV

AREA

10.0

TYPE

THDP VOL

LENGTH

10.0

VOLUME

0.0

HZ ANG

0.0

VR ANG

0.0

EIJV CH

0.0

ROUGH HY DIA

0.0 0.0

CTL

0

CTL FLG

3

TI'E

0.0

PRESSURE

12.3

TEMP

80.0

*ACCUMULATOR*

*

*

*

INLET ELEV = BOTTOM

OUTLET ELEV = TOP0.000 IN.

+ 13.757 IN.

5300000

5300101

--5300102

5300200

NAME

BLACC

TYPE

ACCUM

-*'AREA- -LENGTH.- VOLUME

0.7085 1.1464 0.0

HZ ANG

0.0 - VR ANG. ELV GiL.-

90.0 1.1464

ROUGH

0.0

HY DIlA

0.0

CTL

10

PRESSURE

615.0

TEMP

80.0

5301101

* VLIQ

5302200 0.565

TO JUN AREA F LOSS

500000000 0.002695 50149.59

R LOSS

50149.59

VCAHS

000

LIQ LEV LNLEN ELEV THICK HTR-FLG TNKRIIO TNKCP NIT-K

.0 20.00 0 .0417 0 0 0 0ý

*BROKEN LOOP GOLD LEG BREAK TEE*

*REF DRAWING: 1.5ABL-17 OR 1.5ABL26A (SP-76) - 407875

* INLET ELEV = OUTLET ELEV = 0.000 IN.

3600

3620000

NAME

BRK-TEE

NO JUN

I

TYPE

BRANCH

GTL

1

*AREA LENGTH

3620101 0.0097643 1.647500

VOLUME HZ ANG

0.0 0.0

VR ANG ..ELV GH

0.0 '10.0

3620102

ROUGH

6.667E-5

HY DIA

0.0

GTL

0
* CTL PRESS

3620200 3 2258.30

TEMP

531. 30

*FROM TO JUN AREA

3621101 362010000 363000000 .0097643

F LOSS R LOSS VCAHS

1.2 1.2 000

3621201

FLOW-F

5.840

FLOW-G

0.0

VELJ

0.0

*BROKEN LOOP COLD LEG (DOWNSTREAMl OF BREAK)*

* REF DRAWINGS: 1.5ABL-17 (SP-76) - 407875

* 1.5ABL-15 (SP-79) - 407675 *COLD LEG NOZZLE - 407986

3630000

3630001

3630101

3630102..

3630301

3630302

3630601

3630701

NAMIE

BL-CL

NO VOL

2

TYPE

PIPE

AREA --.0097643

.M0375539

LENGTH

2. 3341667

1.2761677

VOL NO

1

2

VOL NO

I

2

* 1 1/2 IN'SCH-160 PIPE

* DOWNCOMER hINLET'ANNULUS NOZZLE

* SP-79

* COLD LEG NOZZLE

VR ANG VOL NO

0.0 2

ELV CH VOL NO

0.0 2

* ROUGH

3630801 6.667E-5

HY DIA

0.0

VOL NO

2

3631001

3631101

3631201

3631300

CTL FLG VOL NO

0 2

VCAHS JUN NO

0 1

-CTL PRESS

3 2258.30

TEMP

531.30

ZERO

0.0

ZERO AIR FLG VOL NO

0.0 0 2

CTL FLG

1

*FLOW-F FLOW-G VELJ JUN NO

3631301 5.840 0.0 0.0 1

*BREAK JUNCTION*

* ELEV = 0.000 IN.
*

*

*

*

*

*

*

*

*

3750000

*

BREAK SIZES:

0.5% - 0.00001279

Z.1% - 0.00005116

2.5Z - 0.00006175

5.0% - 0.00012079

10.07% - 0.000247

(NOMINAL)

(NOMINAL)

(NOMINAL)

(NOMINAL)

(NOMINAL)

NAME

BRK-VLV

TYPE

VALVE

*FROM TO JUN AREA

3750101 362010000 900000000 0.00001279

F LOSS

0.0

R LOSS 'VCAHS

0.0 100 * (90.9.28)

3750102

CD1

0.90

CD2

0.90

*CTL FLOW-F

3750201 1 0.0

FLOW-G

0.0

VELJ

0.0

3700

3750300

VLV TYPE

TRPVLV

TRIP

402

*CONTIAINMENT*

* ELEV = 0.000 IN.

9000000

9000101

9000102

9000200

9000201

NAME

CONTAIN

TYPE

TMDP VOL

AREA LENGTH VOLUME

10.0 10.0 0.0

HZ ANG

0.0

VR ANG ELV CH

0.0 0.0

ROUGH

0.0

HY DIA

0.0

CTL

0

CTL FLG

2

TIME

0.0

PRESSURE

12.3

QUALE

1.0

++4-1 .. . . . . .414--+4-441+4ý. . . .

* HEAT LOSS AMBIENT VOLUMES *

8000000

8000101

8000102

NAME

ILSG

TYPE

TMDP VOL

AREA LENGTH VOLUME

10.0 1.0 .0..0

HZ ANG

0.0

VR ANG ELV CH

0.0 0.0

ROUGH

0.0

HY DIA

0.0

CTL

0
* ~CTJ2 FLG

8000200

8000201

8010000

8010101

8010102

8010200

8010201

I

TIME

0.0

TEMP QUALE

80.0 1.0

NAME

IBHL

ARE A

10.0

TYPE

TMDP VOL

LENGTH VOLUME

1.0 0.0

HZ PiNG

0.0

VR ANG ELV CH

0.0 0.0

ROUGH HY DIA

0.0 0.0

cmL

0

CTL FLG

1

TIME

0.0

TEMP QUALE

80.0 1.0

8020000

8020101 -1

8020102

8020200

8020201

.--NAME.. ...ý-TYPE .BLPS "TMDP VOL

AREA

.10.0

LENGTH

1.0

VOLUME

0.0

HZ PiNG

0.0

VR PiNG

0.0

ELV CH

0.0

ROUGH HIY DIA

0.0 0.0

CTL

0

CTL FLG

1

TIME

0.0

NAME

IBOL

TEMP QUATJE

80.0 1.0

8030000

8030101.

8030102

8030200

8030201

TYPE

TMJP VOL

AREA LENGTH VOLUME

10.0 1.0 0.0

HZ ANG VR PiNG ELV CH

0.0 0.0 0.0

ROUGH

0.0*

CTL FLG

1

HY DIA

0.0

CTL

0

TIME

0.0

TEMP QUALE

80.0 1.0

* NAME TYPE
8040000

8040101

8040102

8040200

8040201

8050000

8050101

8050102

8050Z00

8050201

ILT'S TNIDP VOL

AREA

10.0

ROUGH

0.0

LENGTH VOLUME HZ PING VR PING

1.0 0.0 0.0 0.0

ELV CH

0.0

HY DIPI

0.0

CTL

0

CTL FLG

1

TIME

0Y. 0

TEMP QUALE

80.0 1.0

NAME

VSLDNC

TYPE

TMDP VOL

AREA LENGTH VOLUME

10.0 1.0 0.0

HZ PING

0.0

VR PING ELV CHI

0.0 0.0

ROUGH

0.0

.CTL FLG

1

HlY DIA

0.0

TEMP

80.0

CTL

0

QIJALE

1.0

TINE

0.0

NAME

PZRCAP

AREA

10.0

ROUGH

0.0

CTL FLG

1

TYPE

TNDP VOL

LENGTH

1.0

HY D~I

0.0

VOLUME

0.0

HZ PING

0.0

VR PING

0.0

ELV CH

0.0

CmL

0

TIME

0.0

TEMP' QUALE

80.0 1.0

*

8070000

8070101

8070102

NAME TYPE

PZRSL TMDP VOL

AREA LENGTH VOLUME

10.0 1.0 0.0

HZ PING

0.0

VR PING ELV CH

0.0 0.0

ROUGH

0.0

HlY DIA

0.0

CTL

0

CTL FLG
8070200 1

*TIME TEMP QUALE

8070201 0.0 80.0 1.0

*NAME TYPE

8080000 TBSHT TMDP VOL

*AREA LENGTH VOLUME HZ ANG VR ANG ELV CH

8080101 10.0 1.0 0.0 0.0 0.0 0.0

*ROUGH HY DIA CTL

8080102 0.0 0.0 0

*CTL FIG

8080200 1

*TIME TEMP QUALE

8080201 0.0 80.0 1.0

*NAME TYPE

8090000. - BLSG -TMDPVOL-

*AREA LENGTH VOLUME HZ PING VR PING ELV CH

8090101 10.0 1.0 0.0 0.0 0.0 0.0

*ROUGH HY DIA CTL

8090102 0.0 0.0 0

*CTL FLG

8090200 1

*TIME TEMP QUALE

8090201 0.0 80.0 1.0

*NAME TYPE

8110000 IBHLH TMDPVOL

*AREA LENGTH VOLUME HZ PING VR PING ELV CH

8110101 10.0 1.0 0.0 0.0 0.0 0.0

*ROUGH HY DIA CTJL

8110102 0.0 0.0 0

*CTL FIG

8110200 1

*TIMlE TEMP QUALE

8110201 0.0 80.0 1.0

*NAME TYPE

8120000 BLPSH TMDP VOL
8120101

8120102

8120200

8120201

8130000

8130101

8130102

8130200

8130201

8140000

8140101

8140102

8140200

8140201

8150000

8150101

8150102

8150200

AREA

10.0

LENGTH VOLUME

1.0 0.0

HZ ANG

0.0

yR ANG ELV CH

0.0 0.0

ROUGH HY DIA

0.0 0.0

CTL

0

CTL FLO

1

TIME

0..,0

NAME

IBCLH

AREA

10.0

ROUGH

0.0

TEMP QUALE

80.0 1.0

TYPE

TMDP VOL

LENGTH

1.0

HY DII\

0.0

TEMP

80.0

VOLUME

0.0

CTL

0

QUALE

1.0

HZ ANG

0.0

VR ANG

0.0

ELV CH

0.0

CTL FLG

1

TIME

0.0

NAME TYPE

ILPSH TMDP VOL

AREA

10.0

ROUGH

0.0

LENGTH VOLUME

1.0 0.0

HZ ANG VR ANG

0.0 0.0

ELV CH

0.0

HY DIA

0.0

GIL

0

CTL FLG

1

TIME

0.0

TEMP

80.0

QUALE

1.0

NAME TYPE

VSLDNH TMDP VOL

AREA

10.0

ROUGH

0.0

LENGTH VOLUME

1.0 0.0

HZ ANG VR ANG . 0.0 0.0

ELV CH

0.0

HY DIA

0.0

CTL

0

CTL FLO

1
8150201

8160000

8160101

8160102

8160200

8160201

TIME

0.0

TEMP QUALE

80.0 1.0

NAME TYPE

PZRH TMDP VOL

AREA LENGTH VOLUME HZ ANG VR ANG ELV CH

10.0 1.0 0.0 0.0 0.0 0.0

R0UbH

0.0

HY DIA

0.0

CTL

0

CTL FLG

1

TIME

0.0

TEMP QUALE

80.0 1.0

***************************************HEAT STRUCTURE*

*INFORIATION *

* ** *******   **  ** * **** ***   ** **   ** ****** * *

*DOWNCOMER INLET ANNULUS HEAT LOSS (ABOVE COLD LEG NOZZLE)*

*LEFT BOUNDARY = COMPONENT 101 *RIGHT BOUNDARY = AMBIENT VOLUME (805)

*GL DATA

11010000

*MESH

11010100

*GEOMETRY

11010101

11010102

*MIATERIALS

11010201

11010202

*SOURCE DIS

11010301

*INIT TEMP

11010400

NH

1

NP

8

TYPE S-FLG L-COR

2 1 0.271375

LOC FLG FRII FLO

0 1

NO ITV R-COR

2 0.279708

2 0.526042

NO ITV R-COR

1 0.283850

NO ITV R-COR

2 0.359375

CMP NO

1

8

SOURCE

0.0

ITV NO

2

7

ITV NO

7

CMP NO

2

ITV NO

3

CMP NO

1

ITV NO

5

FLG

0

* TEMP MESH

11010401 542.3 3

*L-BNDY HY-VOL

11010501 101010000

TEMP MESH

301.9 6

TEMP MESH TEMP MESH

232.6 7- 175.7 8

INC

0

B-CDT A-CODE CY-LENGTH HT-STR-NO

1 1 0.875000 1
*R-BNDY HY-VOL

11010601 805010000

INC B-COT A-CODE CY-LENGTH HT-STR-NO

0 4100 1 0.875000 1

*SOURCE

11010701

TYPE IS-MPLR

0 0

L-DR-HT

0

R-DR-}IT

0

HT-STR-NO

1

4L-H-ST CHF-HTR

11010801 0

HY-DIA

0.0

HY-DIA

0.0

H-EQ-DIA CU-LENGTH HT-STR-NO

0.247955 1.875000 1

*R-H-ST

11010901

CHF-HTR

0

H-EQ-DIA

0.0

CU-LENGTH

1.875000

HT-STR-NO

1

*DOWNCOMER INLET ANNULUS HOLLOW CENTER (ABOVE COLD LEG NOZZLE)*

" LEFT BOUNDARY = ADIABATIC

* RIGHT BOUNDARY = COMPONENT 101

*GL DATA

11011000

*M1ESH

11011100

*GEOMETRY

11011101

*MA~TERIALS

11011201

*SOURCE 018

11011301

*INIT TEMP

11011400

NH

1

NP

6

TYPE S-FLG L-COR

2 1 0.12500

LOG FLG

0

FRM FLG

1

NO ITV R-COR NO ITV R-COR

2 0.18750 1 0.191667

NO ITV R-COR

2 0.20000

CHP NO

1

SOURCE

0.0

ITV NO

2

ITV NO

5

CMP NO

2

ITV NO

3

Clip NO

1

ITV NO

5

FIG

0

* ~TEMP MlESH

11011401 550.0 3

TEMP MESH

549.7 6

*L-BNDY

11011501

HY-VOL

0

INC B-.CDT

0 0

A-CODE

1

CY-LENGTH

0.87500

HT-STR-NO

*R-BNDY NY-VOL

11011601 101010000

INC B-CDT A-CODE CY-LENGTH HT-STR-NO

0 1 1 0.87500 1

*SOURCE

11011701

4L-H-ST

11011801

*R-H-ST

11011901

TYPE IS-MPLR

0 0

CHF-HTR HY-DIA

0 0.0

L-DR-HT

0

R-DR-HT HT-STR-NO

0 1

H-EQ-DIA CH-LENGTH

0.0 0.0o

HT-STR-NO

1

HT-STR-NO

1

CHF-HTR

0

HY-DIA

0.0

H-EQ-DIA

0.336444

CU-LENGTH

1.87500

*DOWNCOMER INLET ANNULUS HEAT LOSS (BELOW COLD LEG NOZZLE)*
" LEFT BOUNDARY =COMPONENT 102

" RIGHT BOUNDARY = AMBIENT VOLUME (805)

*GL DATA

11020000

NH

1

NP

8

TYPE S-FLG L-COR

2 1 0.271375

*MESH LOC FLG FRM FLG

11020100 01

*GEOMETRY

11020101

11020102

*MATERIAL2S

11020201

11020202

*SOUJRCE DIS

11020301

*INIT TEMP

11020400

NO ITV R-COR

2 0.279708

2 0.526042

NO ITV

1

CMP NO

2

R-COR

0.283850

ITV NO

3

NO ITV R-COR

2 0.359375

CMP NO

SOURCE

0.0

ITV NO

7

ITV NO

7

CMP NO

1

ITV NO

5

FLG

0

* TEMP MESH

11020401 549.0 3

*L'-BNDY BlY-VOL

11020501 101010000

*R-BNDY HY-VOL

11020601 805010000

TEMP MESH

308.0 5

TEMP MESH TEMP MESH

Z99.6 ,6 "Z34.6 7

TEMP MESH

176.9 8

INC B-CDT A-CODE CY-LENGTH -IT-STR-N0

0 1 1 .1.0000 1

INC B-CDT A-CODE CY-LENGTH HT-STR-NO

0 4100 1 1.0000 1

*SOURCE

11020701

TYPE IS-MPLR

0 0

L-DR-IIT

0

R-DR-HT

0

HT-STR-NO

1

*11-f-ST CHF-HTR HY-DIA

11020801 0 0.0

H-EQ-DIA CH-LENGTH HT-STR-NO

0.2a47955 1.87500 1

* OWNCOMER INLET ANNULUS HOLLOW CENTER (BELOW COLD LEG NOZZLE)*

" LEFT BOUNDARY = ADIABATIC

" RIGHT BOUNDARY = COMPONENT 102

*GL DATA

11021000ý

*MESH

11021100

NH

1

NP

6

TYPE S-FLG L-COR

2 1 0.12500

LOC FIJG

0

FRI1 FLG

1

*GEOMETRY NO ITV R-COR NO ITV R-COR NO ITV R-COR

11021101 2 0.18750 1 0.191667 2. 0.20000

*MAJTERIALS

11021201

*SOURCE DIS

11021301

CMP NO ITV NO CMP NO ITV NO CMP NO

1 2 2 3 1

ITV NO

5

SOURCE

0.0

ITV NO

5
*INIT TEMP

11021400

11021401

*L-BNDY

11021501

*R-BNDY

11021601

*SOURCE

11021701

*L-H-ST

11021801

*R-H-ST

11021901

FLG

0

TEMP MESH

350.0 3

HY-VOL

0

HY-VOL

101010000

TYPE

0

TEMP MESH

550.3 6

INC

0

INC

0

IS-MPLR

0

HY-DIA

0.0

B -CDT

0

A-CODE CY-LENGTH

1 1.000000

HT-STR-NO

1

B-CDT A-CODE CY-LENGTH HT-STR-NO

1 1 1.000000 1

L-DR-HT

0

H-EQ-DIA

0.0

R-DR-HT

0

HT-STR-NO

1

CHF-HTR

0

CH-LENGTH HT-STR-NO

0.0 1

CHF-HTR HY-DIA

0 0.0

H-EQ-DIA CH-LENGTH HT-STR-NO

0.336444 1 .87500 1

*DOWNCOMER PIPE (HEAT LOSS TO ENVIRONMENT) -UNHEATED*

*LEFT BOUNDARY = COMPONENT 110 (VOLUMES -1,2,3,4;4 --- 7-89

*RIGHT BOUNDARY =AMBIENT VOLUME (805). .... 6789

*GL DATA

11100000

*MESH

11100100

*GEOMETRY

11100101

11100102

*MATERIALS

11100201

11100202

*SOURCE DIS

11100301

*INIT TEMP

11100400

NH

9

LOG FLO

0

NP

10

TYPE

2.

S-FLG L-COR

1 .091041667

FRM FLG

1

NO ITV R-COR

1 .092541667

3 .145833333

NO ITV

2

2

CMP NO

12

8

R-COR NO ITV

.107825000. 1

.312500000

R-COR

10932500

ITV NO

4

CMP NO

10

1

SOURCE

0.0

ITV NO

1

7

ITV NO

9

ITV NO

3

9

CMP NO

10

FJ G

0

* TEMP MESH

11100401 549.9 2

TEMP MESH

395.0 3

TEMP MESH

249.3 8

*L-BNDY

11100501

11100502

11100503

11100504

11100505

11100506

11100507

11100508

HY-VOL

110010900

110020000

110030000

110040000

110050000

110060000

110070000

110080000

INC

0

0

0

0

0

0

0

0

B-CDT

1

1

1

1

1

1

1

1

A-CODE

1

.1

1

1

1

1

1

1

TEMP MESH

189.7 9

CY-LENGTH

1. 715159

0.273268

1. 272435

1. 272435

1.272435

1.272435

1.272435

1.465667

TEMP MESH

149.3 10

HT-STR-NO

1

2

3

4

5

6

7

8
11100509 110090000 0 1 111059 100000 1.434751 11 9

*R-BNDY

11100601

11100602

11100603

11100604

11100605

11100606

11100607

11100608

11100609

*SOURCE

11100701

*L-H-ST

11100801

11100901

flY-VOL

805010000

805010000

805010000

805010000

805010000

805010000

805010000

805010000

8050 10000

TYPE

0

INC

0

0

0

0

0

0

0

0

0

IS-MPLR

0

B-CDT

4100

4100

4100

4100

4100

4100

4100

4100

4100

A-CODE1

1

1

1

1

1

1

1

1

CY-LENGTH

1. 715159

0. 273268

1. 272435

1. 272435

1. 272435

1. 272435

1.272435

1.465667

1.434751

HT-STR-NO

1

2

3

4

5

6

7

8

9

L-DR-IIT

0

R-DR-HT fiT-SIR-NO

0 9

CHE-HTR HY-DIA

0 0.0

CHF-HTR HY-DIA

0 0.0

H-EQ-DIA CH-LENGTH fiT-STR-NO

0.0 16.244581 9

H-EQ-DIA CH-LENGTH

0.0 1.0

fiT-SIR-NO

9

*DOWNCOMER PIPE (EXTERNAL HEATERS)*

* LEFT BOUNDARY

* RIGHT BOUNDARY

*GL DATA

11101000

*MESH LOG I

11101100

*GEOMETRY NO

11101101

11101102

11101103

*MATERIALS CMP

11101201

11101202

11101203'

*SOURCE DIS SOUl

11101301

= COMPONENT 110 (VOLUMES = AMBIENT VOLUME (815)

1, 2,3,4, 5,6,7)

NH

7

'LG

0

[TV

1

3

2

NO

10

1

8

RCE

NP

13

TYPE S-FLG L-COR

2 1 .091041667

FRM FLG

1

R-COR .092541667

.145833333

.3230167

ITV NO

1

7

12

ITV NO

8

NO ITV

2

CMP NO

12

13

SOURCE

1.0

R-COR

.107825000

.145933333

ITV NO

3

8

ITV NO

10

NO ITV

1

2

CMP NO

10

9

SOURCE

0.0

R-COR

.109325000

.15635

ITV NO

4

10

ITV NO

12

*INIT TEMP

11101400

* TEMP

11101401 549.6

11101402 152.6

FLG

0

MESH

2

13

TEMP MIESH

401.5 3

TEMP MESH

263.9 8

TEMP MESH

277.5 11

*L-BNDY

11101501

11101502

11101503

11101504

fly-VOL 110010000

110020000

110030000

110040000

INC

0

0

0

0

B-CDT

1

1

1

1

A-CODE CY-LENGTH

1 0.545674

1 0.727565

1 0.727565

1 0.727565

-TEMP MESH

198.5 12

HI-STR-NO

1

2

3

4
11101505

11101506

11101507

*R-BNDY

11101601

11101602

11101603

11101604

11101605

11101606

11101607

*SOURCE

11101701

11101702

11101703

11101704

11101705

11101706

11101707

*L--T

111.01801

11101901

110050000

110060000

110070000

HY-VOL

815010000

815010000

815010000

815010000

815010000

815010000

815010000

TYPE

10225

10225

10225

10225

10225

10225

10225

0

0

0

1

1

1

1

I

1

INC

0

0

0

0

0

0

0

IS-NPLR

.026003

.035114

.035114

.035114

.035114

.035114

.035114

B-CDT

4100

4100

4100

4100

4100

4100

4100

A-CODE

1

1

1

1

1

1

1

0.727565

0.727565

0.727565

CY-LENGTH

0. 545674

0.727565

0. 727565

0.727565

0.727565

0. 727565

0.727565

R-DR-IIT

0

0

0

0

0

0

0

5

6

7

HT-STR-NO

1

2

3

4

5

6

7

IIT-STR-NO

1.

2

3

4

5

6

7

L-DR-HT

0

0

0

0

0

0

0

CHFE-HTR. HY-DIA.

0 .0.0

H-EQ-DIA CH-LENGTH HT-STR-NO

0.0 16.244581 7

CHt-HTR

0

,HY-DIA

0.0

H-EQ-DIA CH-LENGTH

0.0 16.244581 7

*LOWER DOWNCOMER DISTRIBUTION ANNUJLUS HEAT LOSS (WITH HONEYCOMB)

*LEFT BOUNDARY = COMPONENT 110 (VOLUME 10)

*RIGHT BOUNDARY = AMBIENT VOLUME (805)

*GL DATA

11102000

*MESH

11102100

* GEOMETRY

11102101

11102102

*MATERIALS

11102201

11102202

*SOURCE DIS

11102301

*INlT TEMP

11102400

NH

1

NP

10

TYPE S-FLG L-COR

2 1 0.244875

LOG FLG

0

FRM FLG

1

NO ITV R-COR

1 ..246541667

3 .411541667

NO ITV

2

2

CMP NO

11

8

R-COR NO ITV

.2569583133 1

.578208333

R-COR

.2586Z50

ITV NO

4

CMP NO

10

1

ITV NO

1

7

ITV NO

3

9

CMP NO

10

SOURCE ITV NO

0.0 9

FLG

0

* TEMP MESH

11102401 549.3 2

*L-BNDY HY-VOL

11102501 110100000

TEMP MESH

440.6 3

TEMP MESH

323.7 8

TEMP MESH

241.6 *9

TEMP MESH

181.1 10

HT-STR-NO

1

INC

0

B-CDT A-CODE 'CY-LENIGTH

1 1 0.704681
*R-BNDY HY-VOL

11102601 805010000

INC B-CDT A-CODE CY-LENGTH HT-STR-NO

0 4100 1 0.704681 1

*SOURCE

11102701

*L-H-ST

11102801

*R-H-ST

11102901

TYPE IS-MPLR

0 0

CHF-HTR

0

CHF-HTR

A 0

HY-DIA

0.0

HY-DIA

0.0

L-DR-HT

0

H-EQ-DIA

0. 198130

H-EQ-DIA

0.0

R-DR-HT

0

CH-LENGTH

0. 96250

CH-LENGTH

0. 96250

HT-STR-NO

1

HT-STR-NO

1

HT-STR-NO

1

*LOWER DOWNCOMER DISTRIBUTION ANNULUS - EXTERNAL HEATERS*

" LEFT BOUNDARY = COMPONENT 110 (VOLUME 10)

" RIGHT BOUNDARY = AMBIENT VOLUME (815)

*GL DATA

11103000

*MESH

11103100

*GEOMETRY

11103101

11103102

11103103

*MATERIALS

11103201

11103202

11103203

*SOUJRCE DIS

11103301

*INIT TEMP

11103400

NH

1

NP

13

TYPE S-FLG L-COR

2 1 .244875

LOC FLG

0

NO ITV

1

3

2

CHP NO

10

1

8

SOURCE

0.0

FRM -FLG

1

R-COR

.Z246541667

.411541667

.592725000

ITV NO

1

7

12

ITV NO

8

NO ITV

2

ClIP NO

11

13

SOURCE

1.0

R-COR NO ITV

.256958333 1

.411641667 2

ITV NO

3

8

ITV NO

10

ClIP NO

10

9

SOURCE

0.0

Rý-COR .25862500

.42605833

ITV NO

4

10

ITV NO

12

FJLG

0

MESH

2

13

11030

11103401

TEMP

549.3

182.9

TEMP MESH

444.1 3

TEMP MESH

331.6 8

TEMP MESH

335.1 11

TEMP MESH

247.6 12

HT-STR-NO

1

*L-BNDYs HY-VOL

11103501 110100000

INC

0

B-CDT A-CODE CY-LENGTH

1 1 0.257819

*R-BNDY

11103601

*SOURCE

11103701

*L-H-ST

11103801

*R-H-ST

11103901

HY-VOL

815010000

INC B-CDT A-CODE CY-LENGTH HT-STR-NO

0 4100 1 0.257819 1

TYPE IS-MPLR

10225 .035114

L-DR-HT

0

H-EQ-DIA

0.198130

R-DR-HT

0

HT-STR-NO

1

CHF-HTR

0

CHF-HTR

0

HY-DIA

0

HY-DIA

0

CH-JLENGTH HT-STR-NO

0.96250 1

H-EQ-DIA CH-LENGTH HT-STR-NO

0.0 0.96250 1
*DOWNCOMER DISTRIBUTION ANNULUS TO CORE INLET (THRU LOWER EXTENSION)*

*LEFT BOUNDARY =COMPONENT 140

RIGHT BOUNDARY = COMPONENT 110 (VOLUME 10)

*GL DATA

11140000

*MS

11140100

NH

1

LOC F~LG

0

NP

3

TYPE

2

S-FLG L-COR

1 0.1796667

FRM FLG

1

*GEOMETRY NO ITV R-COR

11140101 2 0.188958

*MATERIALS

11140201

*SOURCE DIS

11140301

*INIT TEMP

.11140400

CMP NO

I

SOURCE

0.0

ITV NO

2

ITV NO

2

FLG

0

* TEMP MESH

11140401 550.0 3

*L-BNDY

11140501

*R-BNDY

11140601

*SOURCE

11140701

11140801

*R-H-ST

11140901

HY-VOL

140010000

HY-VOL

110100000

IN..:B-M~T A-CODE CY-LENGTH HT-STR-NO

0 1 1 0.96250 1

INC B-CDT A-CODE CY-LENGTH HT-STR-NO

0 1 1 0.96Z50 1

TYPE IS-MPLR

0 0

L-DR-HT

0

R-DR-HT HT-STR-NO

0 1

CHF-HTR

0

HY-DIA

0.0

H-EQ-DIA Gil-LENGTH HT-STR-NO

0.0 0.96250 1

CHF-HTR HY-DIA

0 0.0

H-EQ-DIA Gil-LENGTH

0.256760 0.96250

HT-STR-NO

1

*CORE INLET HEAT LOSS (CORE HOUS'G LOWER EXT'N ABOVE DNWCR ANLUS) *

*LEFT BOUNDARY = COMPONENT 140' *RIGHT BOUNDARY =AMBIENT VOLUME (805)

*GL DATA NH NP TYPE S-FLG L-COR

11400000O 1 6 2 1 .14934039

11400100

*GEOMETRY

11400101

*MATERIALS

0 1

NO ITVI R-COR

3 .4826737

NO ITV R-COR

2 .64934039

CMP NO ITV NO CMP NO ITV NO
11400201

*SOURCE DIS

11400301

*INIT TEMP

11400400

13 8 5

SOURCE

0.0

ITV NO

5

FLG

0

MESH

6

11000

11400401

*L-BNDY

11400501

TEMP

547.6

232.4

TEMP MESH

494.2 2

TEMP MESH

459.0 3

TEMP MESH

432.7 4

TEMP MESH

328.3 5

flY-VOL

140010000

INC B-CDT A-CODE CY-LENGTH IIT-STR-NO

0 1 1 0.6258333 1

*R-BNDY flY-VOL

11400601 805010000

INC B-CDT

0 4100

A-CODE CY-LENGTH

1 0.6258333

HT-STR-NO

1

*SOURCE

11400701

*11-H-ST

11400801

TYPE IS-MPLR

0 0

CHF-HTR HY-DIA

0 0.0

F-DR-fiT

0

H-EQ-DIA

-0.0

R-DR-HT HT-STR-NO

0 1

CH-LENGTH fiT-STR-NO

0.0 1

*R-H-ST CHF-HTR IYDA

11400901" 0 - 0.0

H-EQ-DIA CH-LENGTH

0.0 0.0

HT-STR-NO

I1-

*VESSEL BOTTOM HEAD (WITH HONEYCOMB)*

" LEFT BOUNDARY =COMPONENT 120

" RIGHT BOUNDARY =AMBIENT VOLUME (805)

*GL DATA

11200000

*MESHI

11200100

*GEOMETRY

11200101

11200102

*MATERIALS

11200201

11200202

*SOURCE DIS

11200301

*INIT TEMP

11200400

NH

1

NP

9

TYPE S-FLG L-COR

2 1 0.412500

LOC FLG FRII FLG

0 1

NO ITV R-COR

1 .414166667

2 .740416666

NO ITV

2

2

CMP NO

R-COR

.424583333

.90708333

ITV NO

3

8

NO ITV

1

CMP NO

10

R-COR

.426250000

ITV NO

4

CW NO

10

1

SOURCE

0.0

ITV NO

1

6

ITV NO

8

11200401

11200402

TEMP

540.1

237.0

FL6

0

MESH

2

8

TEMP

441.3

179.5

MESH

3

9

TEMP MESH

.343.5 5

TEMP MESH

317.0O 6

TEMP MESH

296.6 7

HT-STR-NO

1

*L-BNDY flY-VOL

11200501 120010000

INC0 B-CDT A-CODE CY-FENGTH

1 1 0.466667
*R-BNDY HY-VOL

Il200601 805010000

INC B-CDT

0 4100

A- CODE CY-LENGTH HT-STR-N0

1 0.466667 1

*SOURCE

11200701

TYPE IS-MPLR

0 0

L-DR-HT

0

R-DR-HT

0

HT-STR-NO

I

*L-H-ST CHF-HTR. HY-DIA

11200801 0 0.0

H-EQ-DIA CH-LENGTH HT-STR-NO

0.0 0.466667 1

*R-ll-ST CIIF-HTR HY-DIA H-EQ-DIA CH-LENGTH HT-STR-NO

11200901 00 0.0 0.0 0.466667 1

*VESSEL LOWER PLENUM WALL (WITH HONEYCOMB)*

* LEFT BOUNDARY = COMPONENT 130

* RIGHT BOUNDARY = AMBIENT VOLUME (805)

*GL DATA

11300000

*MIESH

11300100

*GEOMiETRY

11300101

11300102

*MATERIALS

11300201

11300202

*SOURCE DIS

11300301

*INIT TEMP

11300400

Nil

1

NP

9

TYPE S-FLG L-COR

2 1 .363403395

LOG FLG

0

FRI FLG

1

NO ITV R-COR

1 .365070062

2 .691320063

NO ITV

2

2

CMP NO

R-COR

.375486729

.857986730

NoITV R-COR

1 .37715339

CMP NO

10

1

SOURCE

0.0

ITV NO

1

6

ITV NO

8

ITV NO

3

8

CfIP NO

10

ITV NO

4

11300401

11300402

TEMP

540. .8

232.2

FLG

0

MESH

2

8

TEMP

438.3

176.5

MESH

3

9

TEMP MESH

337.1 5

TEMP MESH

310.3 6

TEMP MESH

290.3 7

*L-BNDY HY-VOL

11300501 130010000

*R-BNDY HY-VOL

11300601 805010000

INC B-CDT A-CODE CY-LENGTH HT-STR-NO

0 1 1 0.721917 1

INC B-CDT A-CODE CY-LENGTH IIT-STR-NO

0 4100 1 0.721917 1

*SOURCE

11300701

*L-H-ST

11300801

*R-H -ST

11300901

TYPE 1S-MPLR

0 0

L-DR-HT

0

R-DR-HT HT-STR-NO

0 1

CHF-HTR

0

HY-DIA

0.0

H-EQ-DIA CH-LENGTH HT-STR-NO

0..0 0.721917 1

CHF-HTR HY-DIA

0 0.0

H-EQ-DIA

0.0

CH-LENGTH HT-STR-NO

0.721917 1
*HEATED CORE (ACTIVE LENGTH)*

*LEFT BOUNDARY = ADIABATIC *RIGHT BOUNDARY = COMPONENT 150

*NOTE: THE MOD-2A CORE IS A 5 X 5 ROD MATRIX WITH

* TWO (2) UNPOWERED RODS IN OPPOSING CORNERS. *EACH ROD HAS AN OD = 0.422 IN. EACH POWER

* STEP (TWO PER HYDRODYNAMIC VOLUME) IS

* MODELED INDIVIDUALLY.

*GL DATA NH NP TYPE S-FLG L-COR

11500000 12 18 2 1 0.0

*MESH LOG FLG FRI FLG

11500100 0 1

*GEOMETRY NO ITV R-COR NO ITV R-COR NO ITV R-COR

11500101 1 0.002917 4 0.009375 4 0.014500

11500102 4 0.015500 4 0.017583

*MATERIALS CMP NO ITV NO CMI' NO ITV NO CMP NO ITV NO

11500201 3 1 4 5 3 9

-11500202 1 13 1 17

*SOURCE DIS SOURCE ITV NO SOURCE ITV NO SOURCE ITV NO

11500301 0.0 1 1.0 5 0.0 17

*INIT TEMP FLG

11500400 -1

*TEtIP DISTRIBUTION

11500401 692.4 692.4 689.8 683.2 673.1 659.6 638.3 619.6 602.9

+ 587.8 585.7 583.7 581.7 579.7 575.7 571.7 567.9 564.2

11500402 822.4 822.4 817.5 804.9 785.6 760.1 717.9 681.2 648.7

+ 619.6 615.7 611.9 608.1 604.3 596.7 589.3 582.1 575.2

11500403 979.3 979.3 971.9 952.9 923.8 885.2 818.5 760.9 710.4

+ 665.5 659.7 654.1 648.5 642.9 631.6 620.7 610.0 599.5

11500404 1143.1 1143.1 1133.1 1107.0 1067.1 1014.2 917.8 835.8 764.6

+ 701.8 694.0 686.3 678.8 671.3 656.0 641.1 626.6 612.4

11500405 1275.5 1275.5 1263.7 1232.9 1185.7 1123.4 1004.1 903.7 817.4

+ 741.8 732.7 723 .8 715.0 706.3 688.5 671.2 654.3 637.7

11500406 1333.6 1333.6 1320.8 1287.7 1236.9 1169.8 1038.8 929.3 835.4

+ 753.5 743.8 734.3 724.9 715.5 696.5 677.9 659.7 641.9

11500407 1350.8 1350.8 1338.1 1304.9 1254.2 1187.] 1055.0 944.6 850.1

+ 767.7 758.0 748.6 739.2 729.9 711.0 692.5 674.5 656.8

11500408 1293.2 1293.2 1281.4 1250.6 1203.4 1141.1 1020.7 919.6 832.6

+ 756.6 747.6 738.7 730.0 721.3 703.7 686.5 669.6 653.2

11500409 1190.8 1190.8 1180.7 1154.6 1114.7 1061.9. 963.3 879.5 806.9

+ 743.0 735.4 727.9 720.4 713.1 698.1 683.5 660.2 655.3

11500410 1026.1 1026.1 1018.7 999.7 970.6 932.0 863.9 805.2 753.7

+ 707.9 702.3 696.7 691.2 685.8 674.7 663.'9. 653.5 643.3

11500411 886.2 886.2 881.3 868.7 849.4 823.9 780.6 742.;9 709.5

+ 679.7 675.9 672.1 668.4 664.8 657.7 650.2 643.2 636.4

11500412 755.6 755.6 753.0 746.4 736.2 722.8 .700.9 681.7 664.6

+ 649.1 647.1 645.1 643.1 641.2 637.3 633.5 629.8 626.2

*L-BNDY HY-VOL INC B-CDT A-CODE SURF-AREA HT-STR-NO
11500501 0 00000 0 0 0.0 12

*R-BNDY

11500601

11500602

11500603

11500604

11500605

11500606

11500607

11500608

11500609

11500610

11500611

11500612

*SOURCE

11500701

11500702

11500703

11500704

11500705

11500706

11500707

11500708

11500709

11500710

11500711

11500712

flY-VOL

150010000

150010000

150020000

150020000

150030000

150030000

150040000

150040000

150050000

1500500'00

150060000

150060000

INC

0

0

0

0

0

0

0

0

0

0

0

0

B-CDT

1

1

1

1

I

1

1

I

1

1

1

1

A-CODE

0

0

0

0

0

0

0

0

0

0

0

0

SURF-AREA

2.5410249

2.5410249

2.5410249

2.5410249

2.5410249

2.5410249

2.5410249

2.5410249

2.5410249

2.5410249

2.5410249

2. 5410249

R-DR-HT

0

0

0.

0

0

0

0

0

0.

0

0

0

HT-STR-NO

1

2

3

4

5

6

7

8

9

10

11

12

HT-STR-NO

1

2

3

4

5

6

7

8

.9

10

11

12

TYPE

10151

10151

10151

10151

10151

10151

10151

10151

10151

10151

10151

10151

IS-MPrR

0. 02584

0.04917

0.07416

0.10166

0. 12001

0. 12916

0.12916

0. 12001

0.10166

0.07416

0.04917

0.02584

L-DR-HT

0

0

0

0

0

0

0

0

--0*

0

0

0

4-11-ST CHF-HTR HY-DIA

11500801 0 0.0

il-EQ-DIA CH-ILENGTH HT-STR-NO

0.0 12.0 12

*R-H-ST

11500901

CHF-HTR

0

HY-DIA

0.0

H -EQ-DI A

0.043992

CU-LENGTH

12.0

HT-STR-NO

12

*VESSEL CORE BARREL WALL (MOD-3 "STEAM-GAP") - UNHEATED*

*LEFT BOUNDARY =COMPONENT 150 *RIGHT BOUNDARY =AMBIENT VOLUME (805)

*GL DATA

11501000

*MS

11501100

*GEOMETRY

11501101

11501102

*MATERIALS

11501201

11501202

*SOURCE DIS

11501301

Nil

6

NP

13

TYPE S-FLG L-COR

2 1 0.132114

LOC FLG

0

FRI FLG

1

NO ITV R-COR

2 .133964

3 .200256

NO ITV R-COR

1 .135531

2 .272256

NO ITV R-COR

2 .143864

2 .438956

CMP NO

SOURCE

0.0

ITV NO

2

8

ITV NO

12

ClIP NO

.1

ITV NO

3

10

ClIP NO

8

ITV NO

5

12
*INIT TEMP

11501400

FLG

-1

*TEMP DISTRIBUTION

11501401 551.6 551.3

+ 334.4 328.0

11501402 564.4 564.1

+ 340.7 334.0

11501403 581.9 581.5

+ 349.3 342.4

11501404 598.5 598.1

+ 357.6 350.5

11501405 609.7 609.3

+ 363.3 356.0

11501406 614.2 613.8

+ 364.8 357.4

*L-BNDY

11501501

11501502

11501503

11501504

11501505

11501506

*R-BNDY

11501601

11501602

11501603

11501604

11501605

11501606

*SOURCE

11501701

*L-H-ST

11501801

HY-VOL

150010000

150020000

150030000

150040000

150050000

..150060000

... lY-VOL

80501.0000

805010000

805010000

.805010000.

805010000

805010000

551.0

257.4

563.7

261.6

581.2

267.4

597:* 8

273.1

609.0

276.9

613.5

277.9

INC

0

0

0

0

0

0

0IN

0

0

0

0

0

360.7 3~

186.8

367.8 3(

189.2

377.5 3'

192.4

386.9 3~

195.6

393.4 3~

197.8

395.2 3~

198.3

B-CDT

1

1

1

1

1

1

..-B-CDT

4100

4100

4100

4100

4100

4100

66.3 364.8 358.7 353

75.5 374.4 368.1 362

35.3 383.7 377.1 371

)1.7 390.0 383.3 377

)3.5 391.8 384.9 378

59.2 357.8 351.9 346

A-CODE

1

CY-LENGTH

0. 635984

0.635984

0.830843

0. 830843

0.830843

0.M65984

CY-LENGTH

0.635984

0. 635984

0.830843

0. 830843

0.830843

0.635984

.7 342.1

.4 348.6

.5 357.5

.3 366.1

.3 372.0

.9 373.6

HT-STR-NO

1

2

3

4

5

6

IIT-STR-NO

1

2

3

4

5

6

TYPE IS-MPLR

0 0

L-DR-HT

0

R-DR-HT HT-STR-NO

0 6

CHF-HTR

0

HY-DIA

0.0

H-EQ-DIA CH-LENGTH HT-STR-NO

0.129489 12.0 6

H-EQ-DIA CH-LENGTH HT-STR-NO

S0.0 12.0 6

*R-H-ST CHF-HTR HY-DIA

11501901 0 0.0

*VESSEL CORE BARREL WALL - EXTERNAL HEATERS*

*LEFT BOUNDARY =COMPONENT 150 *RIGHT BOUNDARY AMBIENT VOLUME (815)

*G3L DATA

11502000

*MESH

11502100

*GEOM1ETRY

11502101

11502102

11502103

NH

6

NP

16

*TYPE

2

S-FLG L-COR

1P 0. 132114

LOC FLG FRN FLG

0 1

NO ITV

2

3

2

R-COR

.133964

.200256

.2827727

NO ITV

1

2

2

R-COR

.135531

.272256

.4494394

NO ITV R-COR

2 .143864

1 .272355
*MJATERIALS

11502201

11502202

11502203

*SOURCE DIS

11502301

*INIT TEMP

11502400

CMP NO

1

1

9

SOURCE

0.0

ITV NO

2

8

13

ITV NO

11

CM.P NO

SOURCE

1.0

ITV NO

3

10

15

ITV NO

13

ClIP NO

1

13

SOURCE

0.0

ITV NO

5

11

ITV NO

15

FLG

-1

*TENP DISTRIBUTION,

11502401 637.7 637.5

+ 473.8 470.2

11502402 643.0 642.8

+ 478.3 474.6

11502403 648.7 648.5

+ 484.3 480.4

11502404 653.2 653.0

+ 489.4 485.5

11502405 653.3 653.1

+ 492.0 488.1

11502406 653.4 653.1

+ 492.9 488.9

.*L-BNIJY HY-VOL

11502501 150010000

11502502 150020000

11502503 150030000

11502504 150040000

11502505 150050000

11502506 150060000

*R-BNDY HY-VOL

11502601 815010000

11502602 815010000

11502603 815010000

11502604 815010000

11502605 815010000

11502606 815010000

637.2

466.8

642.6

471.1

648.2

476.8

652.8

481.7

652.9

484.3

*65Z.9

485.1

INC

0

0

0

0

0

0

INC

0

0

0

0

0

0

492.3

461.8

497.0

465.9

503.1

471.5

508.3

476.3

510.7

478.7

511.5

479.5

491.2

453.4

495.9

457.4

502.0

462.8

507.0

467.4

509.6

469.8

510.4

470.6

490.1

344.5

494.8

347.3

500.9

351.0

506.1

354.2

508.6

355.8

509.4

356.4

-B-CDT

410

410

410

4100

4100

4100

*A-CODE

1

1

1

1

1

1

A-CODE

1

1

1

1

1

1

485.7 4~

235.6

490.3 4~

237.1

496.4 4~

239.1

501.7 4~

240.9

504.2 5(

241.8

505.0 5(

242.1

CY-LENGTH

1. 364016

1.364016

1. 169157

1. 169157

1. 169157

1.364016

CY-LENGTH

1.364016

1. 364016

1. 169157

1. 169157

1.169157

1. 364016

97.9

00.4

01.3 498.0

HI-SIR-NO

1

2

3

4

5

6

Hi-SIR-NO

1

2

3

4

5

6

Hi-STR-NO

1

2

3

4

5

6

81.9 478.7

86.5 483.3

92.6 489.4

494.6

497.2

* SOURCE

11502701

11502702

11502703

11502704

11502705

11502706

*L-H-ST

11502801

*R-H -ST

11502901

TYPE

10225

10225

10225

10225

10225

10225

IS-MPLR

.122878

.122878

.105342

.105342

.105342

.122878

L-DR-HT

0

0

0

0

0

0

R-DR-HT

0

0

0

0

0

0

CHF-HTR HY-DIA

0 0.0

H-EQ-DIA CH-LENGTH Hi-SIR-NO

0.129489 12.0 6

CHF-HTR

0

HY-DIA

0.0

H -EQ-D IA

.0.0

CH-LENGTH HI-SIR-NO

12.0 6

*VESSEL UPPER CORE WALL (NO HONEYCOMB) - UNHEATED*

*LEFT BOUNDARY = COMIPONENT 161
*RIGHT BOUNDARY = AMBIENT VOLUME (805)

*GL DATA

11610000

*MESH

11610100

* GEOMETRY

11610101

11610102

*MATERIALS

11610201

11610202

*SOURCE DIS

11610301

*INIT TEMP

11610400

NH

1

NP

13

TYPE

2

S-FLG L-COR

1 0. 132114

LOG FLG FRM FLG

0 1

NO ITV R-COR

2 .133964

3 .200256

NO ITV R-COR

1 .135531

2 .560256

NO ITV R-COR

2 .143864

2 .7269227

CMP NO

SOURCE

0.0

ITV NO

2

8

ITV NO

12

CMP NO

2

1

ITV NO

3

10

CMP NO

1

8

ITV NO

5

12

FLG

0

MESH

3 11100

11610401

.TEMP

609.7

286.0

TEMP

371.4

22.8..0

MESH

*6

12

TEMP

362.1

173.8

MESH

7

13

TEMP MESH TEMP MESH

353.0 9" 310..4 1 10

*L-BNDY HY-VOL

11610501 161010000

INC

0

B-CDT A-CODE CY-LENGTH

1 1 0.764104

*R-BNDY

11610601

*SOURCE

11610701

4L-H-ST

11610801

*R-H-ST

11610901

HT-STR-NO

1

.HT-STR-NO

1

HY-VOL

805010000

INC *B-CDT A-ýCODE -CY4-ENGTH0 4100 1 0.764104

TYPE IS-MPLR

0 0

L-DR-HT

0

H-EQ-T)IA

0. 173513

R-DR-HT HT-STR-NO

0 1

CHF-HTR

0

HY-DIA

0.0

CH-LENGTH

1. 00083

HT-STR-NO

1

CHF-HTR HY-DIA

0 0.0

H-EQ-DIA CH-LENGTH HT-STR-NO

0.0ý 1.00083 1

*VESSEL UPPER CORE WALL - EXTERNAL HEATERS*

" LEFT BOUNDARY =COMPONENT 161

" RIGHT BOUNDARY = AMBIENT VOLUME (815)

*GL DATA

11611000

*MESH

11611100

*GEOMETRY

11611101

11611102

11611103

*MATERIALS

NH

1

NP

16

TYPE S-FLG L-COR

2 1 0.132114

LOG FLG FRfl FLG

0 1

NO ITV

2

3

2

R-COR

.133964

.200256

.5707727

NO ITV

2~

R-COR

.135531

.560256..

.7374394

NO 1TV R-COR

2 .143864

1 .560356

CM1P NO ITV NO C~lP NO liT NO CNP"NO 'I TV NO
11611201

11611202

11611203

*SOURCE DIS

11611301

*INIT TEMP

11611400

9

2

8

13

2

1

8

3

10

15

1

13

SOURCE

0.0

5

11

ITV NO

15

SOURCE ITV NO SOURCE

0.0 11 1.0

ITV NO

13

FLG

0

MESH

.3

14

11110

11611401

TEMP

609.7

313.1

TEMP MESH

376.5 6

238.5 15

TEMP MESH

360.8 9

178.0 16

TEMP MESH

309.5 11

TEMP MESH

315.1 13

*L-BNDY HY-VOL

11611501 161010000

*R-BNDY HY-VOL

11611601 815010000

ING

0

B-CDT A-CODE CY-LENGTH HT-STR-NO

1 1 0.236729 1

INC B-CDT A-CODE CY-LENGTH

0 4100 1 0.236729

*SOURCE

11611701

*L-H-ST

11611801.

*R-H-ST

11611901

TYPE IS-MPLR

10225 .043539

CHF-HTR HY-DIA

0 0..

CHF-HTR HY-DIA

0 0.0

L-DR-HT

0

H-EQ-VIA

0. 173513'

R-DR-HT

0

HT-STR-NO

1

HT-STR-NO

CH-LENGTH- HT-STRzNO

.1.00083.

H-EQ-VIA CH-JLENGTH HT-STR-NO

0.0 1.00083 1

*VESSEL UPPER PLENUM WALL - UNHEATED*

*LEFT BOUNDARY = COMPONENTS 162,163,164 *RIGHT BOUNDARY = AMBIENT VOLUME (805)

*GL DATA

11600000

NH

3

NP

13

TYPE S-FLG L-COR

2 1 0.133854

*MESH LOC FLG FR!I FLG

11600100 0 1

*GEOM4ETRY

11600101

11600102

*MA~TERIALS

11600201

11600202

*SOURCE DIS

11600301

*INIT TEMP

11600400

NO ITV R-COR

2 0. 142184

4 0.422392

NO ITV R-COR

1 0.146351

2 0.589059

NO ITV R-COR

3 .200518

CMP NO,

1

1

SOURCE

0.0

ITV NO0

2

10

ITV NO

12

CMP NO

2

8

ITV NO

3

12

CMP NO

1

ITV NO

6

FLG

0

11000

11600401

TEMP

600.0

232.0

MESH

3

11

TEMP MESH

270.0 4

188.0 12

TEMP

266.0

150.0

MESH

13

TEMP MESH

2.60.0 7

TEMP MESH

245.0 9
*L-BNDY

11600501

11600502

11600503

*R-BNDY

11600601

11600602

11600603

*SOURCE

11600701

*L-H-ST

11600801

11600802

11600803

*R-H-ST

11600901

HY-VOL

162010000

163010000

164010000

HY-VOL

805010000

805010000

805010000

TYPE

CHF-HTR

0

0

0

INC

0

0

0

INC

.0

0

0

IS-MPLR

0

HY-DIA

0.0

0.0

0.0

B-CDT

B-CDT

4100

4100

4100

A-CODE

A-CODE

CY-LENGTH

1. 756048

1.411882

1. 796411

CY-LENGTH

1. 756048

1.411882

1.796411

R-DR-HT

0

CH-LENGTH

2.760833

2 .416667

2. 550000

HT-STR-NO

1

2

3

HT-STR-NO

1

2

3

HT-STR-NO

3

HT-STR-NO

1

2

3

HT-STR-NO

3

L-DR-HT

0

H-EQ-DIA

.0. 201536

0.244660

0. 255926

CHF-HTR HY-DIA

0 0.0

H-EQ-DIA CU-LENGTH

0.0 0.0.

*VESSEL UPPER.PLENUM WALL -. EXTERNAL-HEATERS .

IEFT L BOUNDARY ýGOMPQNENTW:162;163 164

*RIGHT BOUNDARY '_AMBIENT VOLUME (815)

*GL DATA NH

11601000 3

NP

16

TYPE

2

S-FLG L-COR

1 0.133854

*MESH LOC FLO FRN FLG

11601100 01

*GEOMETRY

11601101

11601102

11601103

*MIATERIALS

11601201

11601202

11601203

*SOURCE DIS

11601301

*INIT TEMP

11601400

NO ITV

2

4

2

CMP NO

8

SOURCE

0.0

R-COR

0.142184

0.422392

0. 5995754

ITV NO

2

10

15

NO ITV R-COR

1 0.146351

1 0.422492

NO ITV R-COR

3 0., 200518

2 0.4329087

CNP NO

2

13

SOURCE

.1.0

ITV NO

3

11

ITV NO

13

CMP NO

1

9

SOURCE

0.0

ITV NO

6

13

ITV NO

15

ITV NO

11

FLG

0

MESH

3

14

11010

11601401

*L-BNDY

11601501

11601502

11601503

TEMP

600.0

264.2

TEMP

275. 0

200.3

MESH

4

15

TEMP

267.4

155.0

MESH

7

16

TEMP MESH

248.7 10

CY-LENGTH

1.004785

1. 004785

0.753589

HY-VOL

162010000

163010000

164010000

INC

0

0

0

B -CDT

1

A-CODE

TEMP MESH

260.0 13

HT-STR-NO

1

2

3

*R-BNDY HY-VOL *RBNY INC Y-OL B-CDT A-CODE.- CY-LENGTH HT-STR-NO
11601601

11601602

11601603

*SOURCE

11601701

11601702

11601703

*L-H-ST

11601801

11601802

11601803

815010000

815010000

815010000

TYPE

10217

10217

10212

CHF-HTR

0

0

0

0

0

0

IS-MPLR

.500072

.499928

1.0

HY-DIA

0.0

0.0

0.0

4100

4100

4100

L-DR-HT

0

0

0

H-EQ-D IA

0.201536

0.244660

0. 255926

H-EQ-DIA

0.0

1

1

1

1.004785

1. 004785

0. 753589

1

2

3

R-DR-HT

0

0

0

CH-LENGTH

2. 760833

2.416667

2. 550000

CH-LENGTH

0.0

HT-STR-NO

1

2

3

HT-STR-NO

1

2

3

HT-STR-NO

3

*R-H-ST CHF-HTR HY-DIA

11601901 0 -0.0

.*

* UPPER CORE SUPPORT PLATE (SEPARATES UPPER PLENUM AND UPPER HEAD) *

" LEFT BOUNDARY =COMPONENT 164

" RIGHT BOUNDARY = COMPONENT 191

*GL DATA

12690000

NHI NP TYPE S-FLG L-COR

4......1 1 .0.0

*MESH LOG FLG FRM FLG

11690100 0 1

*GEOMETRY NO ITV R-COR

11690101 3 0.654

*MATERIA~LS

11690201

*SOURCE DIS

11690301

*INIT TEMP

11690400

CMP NO

1

ITV NO

3

SOURCE ITV NO

0.0 3

FLG

0

* TEMP MESH

11690401 602.9 1

*L-BNDY HY-VOL

11690501 164010000

TEMP MESH

611.9 2

TEM[P MESH

612.0 3

TEMP MESH

611.2 4

*R-BNDY

11690601

*SOURCE

11690701

*L-H-ST

11690801

*R-H -ST

11690901

INC

0

INC

0

B-CDT

1

A-CODE SURF-AREA

1 0.1263155

HT-STR-NO

1

HY-VOL

191010000

B-CDT A-CODE SURF-AREA HT-STR-NO

1 1 0.1263155 1

TYPE IS-MPLR

0 0

CHF-HTR HY-DIA

0 0.0

L-DR-HT

0

R-DR-HT HT-STR-NO

0 1

H-EQ-DIA .CH-LENGTH HT-STR-NO

0.0 0.0 1

H-EQ-DIA CH-LENGTH HT-STR- NO

0,10 0.0 1

CHF-HTR

0

HY-DIA

0.0
*VESSEL UPPER HEAD WALL - TOP & BOTTOM - UNHEATED*

*LEFT BOUNDARY = COMPONENTS 191 & 194 *RIGHT BOUNDARY = AMBIENT VOLUME (805)

*GL DATA

11901000

NH

2

NP

13

TYPE

2

S-FLG L-COR

1 0.133854

*M1ESH LOC FLG

11901100 ,0

FRM FLG

1

*GEOMETRY

11901101

11901102

*MATERIALS

11901201

11901202

*SOUJRCE DIS

11901301

*INIT TEMP

11901400

NO ITV R-COR

2 0.142184

4 0.348434

NO ITV R-COR

1 0.146351

2 0.5151007

NO ITV

3

R-COR

0.200518

CMP NO

SOURCE

0.0

ITV NO

2

10

ITV NO

12

CMP NO

2

8

ITV NO

3

12

CMP NO ITV NO

1 6

FLG

11010

11901401,

11901402.

*L-BNDY

11901501

11901502

11901601

11901602

TEMP

577.5

197.7

MESH

3

12

TEMP MESH

276.9 4

155.3 13

INC

0

0

TEMP MESH

271.0 6

HY-VOL

191010000

194010000

HY-VOL

805010000

805010000

B-CDT A-CODE

A-CODE

TEMP MESH

263.0 8

CY-LENGTH

0.172152

2.424058

CY-LENGTH

0.172152

2.424058

INC B-CDT

O 4100

O 4100

TEMP MESH

250.9 11

HT-STR-NO

1

2

IIT-STR-NO

2

HT-STR-NO

1

2

TYPE

0

CHF-HTR

0

0

IS-MPLR

0

HY-DIA

0.0

0.0

L-DR-HT

0

H-EQ-DIA

0. 209097

0.255470

R-DR-HT

0

CH-LENGTH

8.776667

8.7716667

*R-H-ST CHF-HTR HY-DIA

11901901 0 0.0

H-EQ-DIA CH-LENGTH HT-STR-NO

0.0 8.776667 2

*VESSEL UPPER HEAD WALL -MIDDLE - UNHEATED*

*LEFT BOUNDARY =COMPONENTS 192 & 193 *RIGHT BOUNDARY = AMBIENT VOLUME (805)

*GL DATA NH .NP TYPE S-FLG L-COR.

11902000 2 13 2 1 0.133854

*MESH *MSHLOG FLO FRM FLG
11902100

*GEOMETRY

11902101

11902102

*MATERIALS

11902201

11902202

0 1

NO ITV

2

4

CMP NO

1

1

R-COR

0.142184

0.274476

ITV NO

2

10

NO ITV R-COR

1 0.146351

2 0.441143

NO ITV

3

CMP NO

1

R-COR

0. 200518

ITV.NO

6

CMP NO

2

8

ITV NO

3

12

*SOURCE DIS S(

11902301

*INIT TEMP

11902400

* TEMP

11902401 573.1

11902402 272.0

)URCE

0. 0

ITV NO

12

FLG

0

MESH

3

11

TEMP

289.2

211.0

MESH

4

12

TEMP MESH

285.4 5

162.8 13

TEMP MESH

282.0 6

*L-BNDY

11902501

11902502

*R-BNDY

11902601

11902602

*SOURCE

11902701

*L-H-ST

11902801

11902802

HY-VOL

192010000

193010000

MY-VOL

805010000

805010000

INC

0

0

B-CDT A-CODE CY-LENGTH

1 1 1.579266

1 1 2.486916

TEMP MESH

279.0 7

HT-STR-NO

1

.2

-HT-STR-NO

1*

INC B-CDT - "'0_ 4100 ..0 4100

A-CODE .CY-LENGTH

..1.57-9266

2.486916

TYPE IS-MPLR

0 .0

L-DR-HT

0

H-EQ-DIA

0. 222013

0.228473

R-DR-IIT HT-STR-N0

0. 2

CHF-HTR

0

0

HY-DIA

0.0

0.0

CH-LENGTH

8.776667

8.776667

HT-STR-NO

1

2

*R-H-ST CHF-HTR HY-DIA H-EQ-DIAi CH-LENGTH HT-STR-NO

11902901 0 0.0 0.0 0.0 2

*VESSEL UPPER HEAD WALL - MIDDLE - EXTERNAL HEATERS*

* LEFT BOUNDARY = COMPONENTS 192 & 193

* RIGHT BOUNDARY = AMBIENT VOLUME (815)

*GL DATA

11903000

*MESH

11903100

*GEOMETRY

11903101

11903102

11903103

*MATERIALS

11903201

11903202

11903203

NH

2

NP

16

TYPE S-FLG L-COR

2 1 0.133854

LOG FLG FRM FLG

0 1

NO ITV

2

4-

2

CMP NO

8

R-COR

0.142184

0. 274476

0.4516594

ITV NO

2

10

15

NO ITV R-COR

1 0.146351

1 .0.274576

NO ITV R-COR

3 0.200518

2 0.2849927

ClIP NO

2.

13

ITV NO

3

11

ClIP NO

1

-9

ITV NO

6

13
*SOUJRCE DIS

11903301

*INIT TEMP

11903400

SOURCE

0.0

ITV NO

11

SOURCE

1.0

ITV NO

13

SOURCE

0.0

ITV NO

15

11030

11903401

11903402

11903403

*L-BNDY

11903501

11903502

11903601

11903602

11903701

11903702

TEMP

573.1

284.0

221.6

FLG

0

MESH

3

10

15

TEMP

295.6

288.0

166.4

MESH

4

11

16

TEMP

292.0

297.5

MESH

5

12

flY-VOL

192010000

193010000

flY-VOL

815010000

815010000

TYPE

10208

10208

CHF-HIR

-0

0

INC

0

0

B-CDT A-CODE

INC B-CDT A-CODE

0 4100

0 4100

TEMP MESH

289.0 6

301.7 13

CY-LENGIH

* 0.386567

* 0.966417

CY-LENGTH

0. 386567

0.966417

R-DR-HT

0

0

CH-LENGTH

8.776667

8.776667

TEMP

286.8

299.0

HT-STR-NO

1

2

HT-STR-NO

1

2

HT-STR-NO

1

2

HT-STR-NO

MESH

7

14

IS-MPLR

.166667

.416667

HY-DIA

0.0

0.0

L-DR-HT

0

0

H-EQ-DIAý

0. 222013

0.228473

*R-H-S'f CHF-HTR HY-DIA

11903901 0 0.0

H-EQ-DIA CH-LENGTH HT-STR-NO

0.0 0.0 2

*VESSEL UPPER HEAD WALL - TOP & BOTTOM - EXTERiNAL HEATERS*

*LEFT BOUNDARY = COMPONENTS 191 & 194 *RIGHT BOUNDARY = AMBIENT VOLUME (815)

*GL DATA

11904000

*MESH

11904100

*GEOMETRY

11904101

11904102

11904103

*MATERIALS

11904201

11904202

11904203

*SOURCE DIS

11904301

*INIT TEMP

11904400

NH

2

NP

16

TYPE

2

S-FLG L-COR

1 0.133854

LOC FLG

0

NO ITV

2

4

2

CMP NO

8

SOURCE

0.0

*FRM FLG

1

R-COR

0.142184

0. 348434

0.5256174

ITV NO

2

10

15

NO ITV R -COR

1 0.146351

1 0.348534

NO ITV R-COR

3 0.200518

2 0.3589507

CMP NO

2

13

ITV NO

3

11

ITV NO

13

CMP NO

1

9

ITV NO

6

13

ITV NO SOURCE

11 1.0

SOURCE ITV NO

0.0 15

FLG

0
11040

11904401

11904402

11904503

*L-BNDY

11904501

11904502

11904601

11904602

11904701

11904702

*L-H-ST

11904801

TEMP

577.9

262.0

209.0

MESH

3

10

15

TEMP

282.0

264.6

159.9

MESH

4

11

16

TEMP

278.1

275.4

HY-VOL

191010000

194010000

HY-VOL

815010000

815010000

INC B-CDT

0 1

0 1

INC B-CUT

0 4100

0 4100

MESH

5

12

A-CODE

A-CODE

TEMP

274.8

280.4

MESH

6

13

CY-LENGTH

0. 304515

0.456772

CY-LENGTH

0. 304515

0.456772

R-DR-HT

0

0

CH-LENGTH

8.776667

8.776667-

TEMP MESH

271.7 7

278.4 14

HT-STR-NO

1

2

HT-STR-NO

1

2

HT-STR-NO

1

2

HT-STR-NO

1

2

TYPE IS-MPLR

10208 .166667

10208 .250000

CHF-HTR HY-DIA

0 0.0

0 0.0

CHF-HTR HY-DIA

0 0.0

L-DR-HT

0

0

H-EQ-DIA

0.209097

0. 255470

H-EQ-DIA

0.0

CH-LENGTH HT-STR-NO

8.776667 2 *

*HEAT SLAB.. .STEAM GENERATOR TUBE BUNDLE (INTACT LOOP)

(RISING PRIMARY COOLANT... .FIRST HALF OF U-TUBE)

*

*

"* ETBUDR TA EEAO RMR OLN

" LEFHT BOUNDARY = STEAM GENERATOR PRIMNARY COOLANT (COMPONENT 220)

(COMPONENT 600)

*GL DATA

12200000

NH

4

NP

5

TYPE S-FLG L-COR

2 1 0.032375

*MESH LOC FIJO FRI FLO

12200100 0 1

*GEOMETRY NO ITV R-COR

12200101 4 0.036458333

*MATERIALS

12200201

*SOURCE DIS

12200301

*INIT TEMP

12200400

CMP? NO

5

ITV NO

4

SOURCE ITV NO

0.0 4

FLG

-1

*TEM1P DISTRIBUTION

12200401 575.9 565.1

12200402 567.9 558.9

12200403 561.0 553.5

12200404 556.5 550.3

554.5

550.1

546.3

544.3

544.2

541.6

541.6

538.4

534.2

533.3

533.3

532.7

*L-BNDY

12200501

12200502

12200503

HY-VOL'

220010000

220020000

220040000

INC

0

10000

0

B-CDT A-CODE CY-LENGTH

11 47.7150600

11 47.465000

11 40.152175

HT-STR-INO

1

.3

4
*R-BNDY

12200601

12200602

12200603

*SOURCE

12200701

*L-H-ST

12200801

*R-H-ST

12200901

12200902

HY-VOL

600010000

600020000

600040000

INC

0

10000

0

B-CDT A-CODE

1

1

1

CY-LENGTH

47.715000

47.465000

40.152175

HT-STR-NO

1

3

4

TYPE IS-NPLR

0 0

CHF-HTR HY-DIA

0 0.064750

L-DR-HT

0

H-EQ-DIA

0.064750

H-EQ-DIA

.3115210

.4104615

R-DR-HT HT-STR-NO

0 4

CH-LENGTH

29.5

CH-LENGTH

29.5

29.5

HT-STR-NO

4

HT-STR-NO

3

4

CHF-HTIR

0

0

HY-DIA

.0887292

.1077433

*HEAT SLAB... STEAM GENERATOR TUBE BUNDLE (INTACT LOOP)*

* ~(DECENDING PRIMARY COOLANT ... SECOND HALF OF U-TUBE)

"* ETBUDR TA EEAO RMR OLN

" LEFHT BOUNDARY = STEAM GENERATOR SERONDARY COOLANT (COMPONENT 220)

(COMPONENT 600)

* *GL DATA

12201000

*MESH

12201100

*GEOMETRY

12201101

*MATERIALS

12201201

*SOURCE DIlS

12201301

*INIT TENP

12201400

NH

4

NP

5

TYPE S-FLG L-COR

2 1 0.032375

LOG FLG FRM FLO

0 1

NO ITV - R-COR

4 0.0364583333

CNP NO

5

SOURCE

0.0

ITV NO

4

ITV NO

4

* INCONEL 600

FLG

-1

*TEMP DISTRIBUTION

12201401 551.9 546.5

12201402 546.5 541.7

12201403 542.2 538.1

12201404 538.5 535.0

*L-BNDY

12201501

12201502

12201503

*R-BNDY

12201601

12201602

12201603

12201604

*SOURCE

12201701

HY-VOL

220050000

220060000

220080000

HY-VOL

600040000

600030000

600020000

600010000

541.2

537.0

534.1

531.5

INC

0

10000

INC

0

0

0

0

538.4

532.5

530.2

528.3

532.7

528.1

526.4

525.1

B-CDT A-CODE

B-CDT *A- CODE

L-DR-HT

0

CY-LENGTH

40. 152175

47.465000

47.715000

CY-LENGTH

40.152175

47.465000

47.465000

47.715000

R-DR-HT

0*

HT-STR-NO

1

3

4

HT-STR-NO

i

2

3

4

TYPE IS-?.PLR HT-STR-NO

0 0
*L-H-ST

12201801

*R-H-S'f

12201901

12201902

CUF-HIR HY-DIA

0 .0647500

H-EQ-DIA CH-LENGTH HT-STR-NO

.0647500 29.5 4

CHF-IITR

0

0

HY-DIA

.1077433

.0887292

H-EQ-DIA

.4104615

.3115210

Cl-LENGTH

29.5

29.5

IIT-STR-NO

1

4

*HEAT SLAB... INTACT LOOP ST. GENERATOR HEAT TRANSFER FROM*

* ~THE RISER TO THE DOWNCOMER*

" LEFT BOUNDARY ='COMPONENT 600

* RIGHT BOUNDARY = COMPONENT 602 & 603

*GL DATA

16000000

*MESH

16000100

NH

5

NP

6

TYPE S-FLG L-COR

2 1 .2680135

LOC FLG FRII FLG

0 1

*GEOMETRY NO ITV R-COR

16000101 2 .3637826

NO ITV R-COR

1 .3665038

NO ITV R-COR

2 .3782030

*MAJTERIALS

16000201

*SOURCE DIS

16000301

*INIT TEMP

16000400

CM? NO ITV NO-'

14 A;

CM? NO

15

ITV NO CMP NO ITVNO

.5.

SOURCE

0.0

ITV NO

5

FLG

0

16000

16000401

*L-BNDY

16000501

16000502

16000503

16000504

*R-BNDY

16000601

16000602

16000603

16000604

16000605

*SOURCE

16000701

*L-H -ST

16000801

16000802

16000803

16000804

*R-H-ST

TEMP

514.0

501.3

MESH

1

6

HY-VOL

600010000

600020000

600040000

600050000

HY-VOL

603040000

603030000

603020000

603010000

602010000

TYPE .0

CHF-HTR

0

0

0

0

TEMP MESH

522.3 2

INC

0

10000

0

0

INC

0

0

0

0

0

IS-ýIPLR

0

HY-DIA

.0884737

.0884737

.1058911

.2145338

TEMP MESH

503.2 3

B-CDT

1

1

1

1

B-CDT

1

1

1

1

A-CODE

1

A-CODE

TEMP MESH

501.8 4

CY-LENGTH

7.9525000

7.9108334

7.4762500

1.4054167

CY-LENGTH

7.9525000

7.9108334

7.9108334

7.4762500

1.4054167

R-DR-HT

0

CH-LENGTH

7.9525000

7.9108334

7.4762500

1.4054167

TEMP MESH

501.7 5

HT-STR-NO

4

5

HT-STR-NO

1

2

3

4

5

IIT-STR-NO

5

HT-STR-NO

1

3

4

5

L-DR-HT

0

H-EQ-DIA

.2535283

.2535283

.2728816

.3379099

CHF-HTR HY-DIA CH-HR-EQ-DIA Y-IA CH-LENGTH HT-STR-NO
16000901

16000902

16000903

16000904

0

0

0

0

.0201639

.0126981

.0128227

.3369291

.0732836

.0518749

.0523927

.790Z365

7.9525000

7.9108334

7.4762500

1.4054167

1

3

4

5

*HEAT SLAB... STEAM GENERATOR STEAM DOME HEAT LOSS TO ENVIRONMENT *

* ~(INCLUDES UPPER SECTION OF DOWNCOMER)*

" LEFT BOUNDARY = COMPONENTS 612,611,602

" RIGHT BOUNDARY = AMBIENT VOLUME (800)

*GL DATA

16100000

*MESH

16100100

3

NP

6

TYPE S-FLG L-COR

2 1 .6719167

LOG FLG FRI FLG

0 1

*GEOMETRY NO ITV R-COR

16100101 2 0.750

NO ITV R-COR

3 1.000

*MATERIALS

16100201

CMP NO ITV NO

1. 2

CMP NO

17

ITV NO

5

*SOURCE DIS SOU

.16100301

*INIT TEMP

16100400

RCE

FLG

0

ITV NO

5.

* TEMP MESH

16100401 516.5 3

*L-BNDY

16100501

16100502

16100503

*R-BNDY

16100601

16100602

16100603

*SOUJRCE

16100701

*L-H-ST -

16100801

16100802

16100803

HY-VOL

612010000

611010000

602010000

HY-VOL

800010000

800010000

800010000

TEMP MESH

376.6 4

INC

0

0

0

INC

0

0

0

TEMP MESH

239.5 5

B-CDT A-CODE

B-CDT A-CODE

4100 1

4100 1

4100 1

L-DR-HT

0

TEMP MESH

96.4 6

CY-LENGTH

1.1334992

0.1497007

4.8530686

CY-LENGTH

1. 133499Z

0.1497007

4. 8530686

HT-STR-NO

1

2

3

HT-STR-NO

1

2

3

TYPE IS-MPLR

0 .0

R-DR-HT HT-STR-NO

0 3

CHF-HTR

0

0

0

HY-DIA

.6533449

.5664365

.3369291

H-EQ-DIA

.6533449

2.6896228

.5873578

CH-TLENGTH

1.5404167

0.7487500

5.5516667

HT-STR-NO

1

2

3

*R-H-ST CHF-HTR HY-DIA H-EQ-DIA CH-LENGTH HT-STR-NO

16100901 0 0.0 0.0 0.0 3

*HEAT SLAB... BROKEN LOOP ST. GENERATOR HEAT TRANSFER FROM*

* THE RISER TO THE DOWNCOMlER (TOP)

*LEFT BOUNDARY = COMPONENTS 600, 601
*RIGHT BOUNDARY = COMPONENTS 602

*GL DATA

16001000

*MESH

16001100

*GEOMETRY

16001101

*MATERIALS

16001201

*SOURCE DIS

16001301

*INIT TEMP

16001400

Nil

2

NP

3

TYPE S-FIjG 1-COR

2 1 .4341667

LOG FLG FRM FLG

0 1

NO ITV R-COR

2 .4479167

CMP NO ITV NO

1 2

SOURCE

0.0

ITV NO

2

FLG

0

* TEMP MESH

16001401 519.1 1

TEMP MESH

501.3 2

INC

0

0~

TEMP MESH

488.0 3

B-CDT A-CODE CY-LENGTH

1 1 3.5802339

1 1 0.4375000

*L-BNDY

16001501

16001502

*R-BNDY

16001601

16001602

*SOURjCE

16001701

*L-H-ST

16001801

16001802

*R-H-ST

16001901

16001902

flY-VOL

*.600050000

.;601010000

BlY-VOL

* 602010000

602010000

TYPE

0

CHF-HTR

0

0

CHF-IITR

0

0

HT-STR-NO

I2.

2

-INC B CDT0 1

0 1

A-CODE

1

I

CY-LENGtH

3.5802339

0.4375000

IS-MPLR

0

HY-DIA

.7932265

.8683333

IIY-DIA

.3369291

.3369291

L-DR-HT

0

H-EQ-DIA

.8251205

.8683333

NH EQ-DIA

.7902365

.7902365

R-DR-HT HT-'STR-NO

0 2

CH-LENGTH

3.7504167

0.4375000

CH-LENGTH

3.7504167

0.4375500

HT-STR-NO

1

2

HT-STR-NO

1

2 *

* HEAT SLAB... INTACT LOOP STEAM GENERATOR DOWNCOMER FILLERS *

"* ETBUDR CMOET 62 0

* LEGHT BOUNDARY = COMPONENTS 602, 603

*GL DATA

16031000

*MESH

16031100

*GEOMIETRY

16031101

*MATERIALS

16031201

NH

5

NP

3

TYPE

2

S-FIG L-COR

1 .3645833

LOC FLG

0

FRM FLG

1

NO ITV R-COR

2 .39583333

CMP NO ITV NO

2
*SOUJRCE D1S

16031301

SOURCE

0.0

ITV NO

2

*INIT TEMI

16031400

16031401

*L-BNDY

16031501

16031502

16031503

16031504

16031505

*R-BNDY

16031601

16031602

16031603

16031604

16031605

*SOURCE

16031701

.-,*IrH-ST

16031801

16031802

16031803

16031804

16031805

*R-H-ST

16031901

16031902

16031903

16031904

16031905

) FLG

0

TEMP MESH

524.5 1

HY-VOL*

602010000

603010000

603020000

603030000

603040000

HY-VOL

602010000

603010000

603020000

603030000

603040000

TEMP MESH

528.7 2

ING

0

0

0

0

0

TEMP MESH

517.9 3

B-CUT

B-CDT

I

A-CODE

1

CY-LENGTE{

1. 1902917

6.3963472

6. 7681575

6. 7681575

5.3422315

INC

0

0

0

0

0

A-CO

TYPE IS-MPLR.

0 0

L-DR-HT

0

CHF-HTR

0

0

0

0

0

CHF-HTR

0

0

0

0

0

..-HY-DIA.

.3369291

.0128227

.0126981

.0126981

.0126981

HY-DIA

.3369291

.0128227

.0126981

.0126981

.0126981

H:-EQ-DIA.'

.7902365

.0523927

.0518749

.05187.49.

.0518749

H-EQ-DIA

.7902365

.0472456

.0467818

.0467818

.0467818

DE CY-LENGTH

1 1.1902917

1 6.3963472

1 6.7681575

1 6.7681575

1 5.3422315

R-DR-HT

0

.CH7LENGTH

1. 3912500

7.4762500

7.9108334

7.9108334

MOANf66

CH-LENGTH

1.3912500

7.4762500

7.9108334

7.9108334

6. 2441667

HT-STR-NO

1

2

3

4

5

HT-STR-NO

1

2

3

4

5

HT-STR-NO

.5

$T1fzri.M74

1.

2

3

.4

5

HT-STR-NO

1

2

3

4

5

*HEAT SLAB... INTACT LOOP STEAM GENERATOR DOWNCOMER*

* . HEAT TRANSFER TO THE ENVIRONMENT*

*LEFT BOUNDARY = COMPONENTS 603 *RIGHT BOUNDARY = AMBIENT VOLUME (800)

*GL DATA

16030000

.*MS

16030100

NH

4

NP

6

TYPE

2

S-FLG L-COR

1 .3985000

LOG FLG FRII FLG

0 1

*GEOM1ETRY NO ITV R-COR

16030101 2 .4479167

NO ITV R-COR

3 .69791671

CMP NO ITV NO

17 5

*MATERIALS

16030201

*SOURCE DIS

1 2

SOURCE ITV NO
16030301

*INIT TERP

16030400

* TEMP

16030401 514.1

16030402 95.3

0.0

FLG

0

MESH

1

6

5

TEMP MESH

514.0 2

TEMP MESH

513.9 3

*L-BNDY

16030501

16030502

16030503

16030504

*R-BNDY

16030601

16030602

16030603

*SOURCE

16030701

*4-H-ST

16030801

16030802

16030803

16030804

*R-H-ST

16030901

BY-VOL

603010000

603020000

603030000

603040000

flY-VOL

800010000

800010000

800010000

INC

0

0

0

0

INC

0

0

0

B-CDT

410

4100

4100

A-CODE

A-CODE

TEMP MESH

369.0 4

CY-LENGTH

7.4762500

7.9108334

7.9108334

7.9525000

CY-LENGTH

7.4762500

7.9108334

7.9525000

TEMP MESH

232.0 5

HT-STR-NO

1

2

3

4

HT-STR-NO

1

3

4

TYPE IS-HPLR

0 0

CHF-HTR

0

0

0

0

HY-DIA

.0126812

.0126981.:

.0201639

L-DR-HT

0

H-EQ-DIA

.0472456

.0467818

.:..0467&18.

.0667482-

R-DR-HT HT-STR-NO

0 4

CH-LENGTH

7* *4762500

.7.9108334

.7-9108334

7.9525000

lIT-STR-NO

1

2

3

4

CHF-HTR HY-DIA

0 0.0

H-EQ-DIA CH-LENGTH HT-SIR-NO

0.0 0.0 4

*HEAT SLAB... STEAM GENERATOR TUBE BUNDLE (BROKEN LOOP)*

* ~(RISING PRIMARY COOLANT ... FIRST HALF OF U-TUBES)

LETBUDR* TA EEAO RMR OLN CMOET30

*RIEFT BOUNDARY = STEAM GENERATOR PRCONARY COOLANT (COMPONENT 320)

*GL DATA

13200000

NH

5

NP

5

TYPE

2

S-FLG L-COR

1 0.0310417

*MESH LOG FLG FEM FLG

13200100 0 1

*GEOMETRY

13200101

*MATERIALS

13200201

*SOURCE DIS

13200301

*INIT TEMP

13200400

NO ITV R-COR

4 0.0364583

CMP NO

5

SOURCE

0.0

ITV NO

4

ITV NO

4

*INCONEL 600

FLG

-1

*TEMP DISTRIBUTION

13200401 579.0 569.2

13200402 575.0 566.0

559.6 550.3 541.2

552.3 548.8 540.5
13200403

13200404

13200405

*L-BNDY

13200501

13200502

13200503

13200504

*R-BNDY

13200601

13200602

13200603

13200604

*SOURCE

13200701

*L-H-ST

13200801

*R-ll-ST

13200901

13200902

570.9 562.8

567.5 560.1

564.1 557.4

HY-VOL

320010000

320010000

320020000

320040000

HY-VOL

716010000

700010000

700020000

700040000

554.9

552. 9

550.9

INC

0

0

10000

0

INC

0

0

10000

0

547.2

545.9

544.5

539.7

539.0

538.3

B-CDT A-CODE

1

11

11

1 1-H

ACD 0-D 

CY-LENGTH

2. 1666667

13 .4166667

15. 0000000

15.0856194

CY-LENGIH

2.1666667

13.4166667

15. 0000000

15.0856194

HT-STR-NO

1

2

4

5

HT-STR-NO

1

2

4

5

TYPE IS-MPLR

0 0

CHF-HTR HY-DIA

0 .0620833

R-DR-HT HT-STR-NO

0 5

H-EQ-DIA CH-LENGTH

.0620833 0.0

HT-STR-NO

5

HT-STR-NO

4

5

CHF-HTR

.0

0

HY-DIA ..0659845

H-EQ-DIA

.2900678

.3067184

CH-LENGTH

0.0

0.0

*HEAT SLAB... 'STEAM GENERATOR TUBE BUNDLE (BROKEN LOOP)* * ~(DECENDING PRIMARY COOLANT... .SECOND HALF OF U-TUBES)*

* ETBUDR TA EEAO RMR OLN CMOET30

RILEFT BOUNDARY= STEAM GENERATOR SEROMARY COOLANT (COMPONENT 320)

*GL DATA

13201000

*KESH

13201100

* GEOMETRY

13201101

*MATERIALS

13201201

*SOURCE DIS

13201301

*INIT TEMP

13201400

NH

5

NP

5

TYPE S-FLG L-COR

2 1 0.0310417

LOG FLG

0

FRM FLG

I

NO ITV R-COR

4 0.0364583

CMP NO

5

ITV NO

4 *INCONEL 600

SOURCE ITV NO

0.0 4

FLG

-1

*TEMP DISTRIBUTION

13201401 554.5 549.6

13201402 552.4 547.9

13201403 550.2 546.2

13201404 548.4 544.7

13201405 546.6 543.2

*L-BNDY HY-VOL

13201501 320050000

544.9

543.6

542.2Z

541.1

540.0

540.3

539.4

538.4

537.6

536.8

535.8

535.3

534.7

534.2

533.7

INC B-CD'T A-CODE CY-LENGTA

0 1 1 15.0856194

HT-STR-NO

1
13201502 320060000 10000 1 1 15.0000000 3

13201503 320080000 0 1 1 13.4166667 4

13201504 320080000 0 1 1 2.1666667 5

*R-BNDY HY-VOL INC B-CDT A-CODE CY-LENGTH HT-STR-NO

13201601 700040000 0 1 1 15.0856194 1

13201602 700030000 -10000 1 1 15.0000000 3

13201603 700010000 0 1 1 13.4166667 4

13201604 716010000 0 1 1 2. 1666667 5

*SOURCE TYPE IS-NPLR L-DR-HT R-DR-HT HT-STR-NO

13201701 0 0 0 0 5

*L-H-ST CHF-HTR HY-DIA H-EQ-DIA CH-LENGTH HT-STR-NO

13201801 0 .0620833 .0620833 0.0 5

*R-H-ST CHF-HTR HY-DIA H-EQ-DIA CH-LENGTH f{T-STR-NO

13201901 0 .0753070 .3067184 0.0 1

13201902 0 .0659845 .2900678 0.0 5

*HEAT SLAB... STEAM GENERATOR STEAM DOME HEAT LOSS TO ENVIRONMENT *

* ~(INCLUDES UPPER SECTION OF RISER AND SEPARATOR)*

*LEFT BOUNDARY = C *RIGHT. BOUNDARY = A

*GL DATA NH

17023000 2

*MESH LOG FLG

17023100 0

*GEOMETRY NO ITV

17023101 2

*MATERIALS CMI' NO

17023201 1

*SOURCE DIS SOURCE

17023301 0.0

*INIT TEMP FLG

17023400 0

* TEMP MESH

170234&1 516.5 2 -

*L-BNDY HY-VOL INC B-CDT A-CODE CY-LENGTH HT-STR-NO

17023501 701010000 0 1 1 1.3615856 1

17023502 703010000 0 1 1 0.7925179 2

*R-BNDY HY-VOL INC B-CDT A-CODE CY-LENGTH HT-STR-NO

17023601 809010000 0 4300 1 1.3615856 1

17023602 809010000 0 4300 1 0.7925179 2

*SOUIRCE TYPE IS-MPLR L-DR-HT R-DR-HT HT-STR-NO

17023701 0 0 0 0 2

*L-H-ST CHF-HTR HY-DIA H-EQ-DIA CH-LENGTH HT-STR-N0
17023801

17023802

*R-H-ST

17023901

0

0 .6944443.2429779

HY-DIA

0.0

.6944443

.3342205

0.0

0.0

1

2

CHF-HTR

0

H-EQ-DJA CH-LENG'fH HT-STR-NO

0.0 0.0 2

*HEAT SLAB... BROKEN LOOP ST. GEMRAT0R SECONDARY RISER HEAT LOSS *

* ~TO THE ENVIRONMENT*

" LEFT BOUNDARY =COMPONENT 700 & 716

" RIGHT BOUNDARY AMBIENT VOLUME (809)

*GL DATA

17000000

*MESH

17000100

NH

6

LOC FLG

0

NP

5

TYPE S-FLG L-COR

2 .1 .1278333

FRI FLG

1

*GEOM1ETRY NO ITV R-COR NO ITV R-COR

17000101 2 .1458333 2 .3135000

NO ITV R-COR

*MATERIALS

17000201

CMP NO ITV NO

1 2

CMIP NO

32

ITV NO

- 4

*SOURCE DIS - SOURCE

17000301 0.0

* ITV-NO

4

*INIT TEMP

17000400

FLG

0

* TEMP MESH

17000401 519.1 1

TEMP MESH

501.3 2

TEMP MESH

488.9 3

*L-BNDY

17000501

17000502

17000503

17000504

*R-BNDY

17000601

17000602

17000603

17000604

*SOURCE.

17000701

*L-H-ST

17000801

17000802

17000803

17000804

HY-VOL

700010000

700020000

700050000

716010000

HY-VOL

809010000

809010000

809010000

809010000

INC

0

10000

0

0

B-CDT

B-CDT

4400

4400

4400

4400

A-CODE

1

1

1

1

A-CODE

1

1

1

1

TEMP MESH

320.6 4

CY-LENGTH

6. 7083333

7.5000000

6.8229167

10833333

CY-LENGTH

6.7083333

7. 5000000

6.8229167

1.0833333

TEMP MESH

94.1 5

HT-STR-NO

1

4

5

6

HT-STR-NO

1

4

5

6

INC

0

0

0

0

TYPE IS-MPLR

0 0

CHF-HTR

0

0

0

0

HY-DIA

.0659845

.0753070

.1934227

.0659845

L-DR-HT

0

H-EQ-DIA

.1654559

.1759521

.2385353

.1654559

R-DR-IIT HT-STR-NO

0 6

GA-LENGTH

0.0

0.0

0.0

0.0

HT-STR-NO

3

4

5

6

*R-H-ST CHF-HTR HY-DIA

17000901 0 0.0 w

H-EQ-DJA CH-LENGTH HT-STR-NO

0.0 0.0 6

*HEAT SLAB... BROKEN LOOP ST. GENERATOR RISER TO DOWNCOMER*
* LOSS ~HEAT TO THE ENVIRONMENT*

*LEFT BOUNDARY =COMPONENT 711

*RIGHT BOUNDARY = AMBIENT VOLUME (809)

*GL DATA

17110000

*MESH

17110100

*GEOMETRY

17110101

*MATERIALS

17110201

NH

1

LOG FLG

0

NP

5

TYPE S-FLG L-COR

2 1 .2102917

FRM FLG

I

NO ITV R-COR NO ITV R-COR

2 .2317917 2 .3984584

CMP NO ITV NO

1 2

CMP NO

32

ITV NO

4

*SOURCE D'

17110301

*INIT TEN]

17110400

17110401

SOURCE

0.0

ITV NO

4

FLG

0

TEMP MESH

514.5 1

TEMP MESH

514.7 -Z.

TEMP MlESH

513.9 3

TEMP. MESH

300.0 4

TEMP MESH

.95.3 5

*L-BNDY flY-VOL

17110501 711010000

*R-BNDY

17110601

*SOURCE

17110701

*L-H-ST

17110801

*R-H-ST

17110901

.INC* fl-CDT A-CODE CY-LENGTH HT-STR-NO

0 1 1 4.6776013 1

.INC B-CDT A-CODE CY-LENGTH HT-SIR-NO

O 4400 1 4.6776013 1

HY-VOL

809010000

TYPE

0

IS-MPLR

0

L-DR-HT

0

R-DR-HT

0

Hi-STR-NO

1

CHF-HTR HY-DIA

O .3989363

CHF-HTR HY-DIA

0 0.0

H-EQ-:DIA CU-LENGTH HT-STR-NO

.3989363 0.0 1

H-EQ-DIA CH-LENGTH Hi-STR-NO

0.0 0.0 1

*HEAT SLAB... BROKEN LOOP ST. GENERATOR DOWNCOMER*

* HBEAT LOSS TO THE ENVIRONMENT*

*LEFT' BOUNDARY = COMPONENTS 713, 714, & 715

*RIGHT BOUNDARY = AMBIENT VOLUME (809)

*GL DATA

17140000

*MIESH

17140100

*GEOMETRY

17140101

*MATERIALS

17140201

NH

7

LOG FLG

0

NP

5

TYPE

2

S-FLG L-COR

1 .0575

ERM FLG

1

NO ITV -R-COR NO-IiV R-COR

2 .0691667 2 .2358334

CMI' NO ITV NO CMI' NO ITV NO'

1 2 32 4
*SOURCE DIS

17140301

SOURCE

0.0

ITV NO

4

*INIT TEMP

17140400

17140401

FLG

0

TEMP MESH

114.1 1

TEMP MESH

514.0 2

TEMP MESH

513.9 3

*L-BNDY

17140501

17140502

17140503

17140504

17140505

*R-BNDY

17140601

17140602

17140603

17140604

17140605

*SOURCE

17140701

*L-H-ST

17140801

17140802

17140803

HY-VOL

713010000

714010000

714020000

714050000

715010000

HY-VOL

809010000,

809010000

809010000

809010000

809010000

INC

0

0

10000

0

0

INC

0

0

0

0

0

B-CDT

B-CDT

4500

4500

4500

4500

4500

A-CODE

1

1

1

1

1

A-CODE

1

1

1

1

1

TEMP MESH

300.0 4

CY-LENGTH

3. 1426389

4. 0891869

7.5000000

7.4537703

7.8734167

CY-LENGTH

3. 1426389

4. 0891869

7.5000000

7.4537703

7.8734167

TEMP MESH

95.3 5

HT-STR-NO

1

2

5

6

7

-HT-STR-NO

1

2

5

6

7

TYPE -IS-MPLR

0 .0

CHF-HTR

0

0

0

. 'HY-DIA

.1316182

.1150000

-.1303373

L-DR-HT

0

H-EQ-DIA

.1316182

.1150000

.1303373

R-DR-HT HT-STR-NO

0 -7

CH-LENGTH

0.0

0.0

0.0

HT-STR-NO

1

6

7

*R-H-ST CHF-HTR HY-DIA

17140901 0 0.0

H-EQ-DIA CH-LENGTH HT-STR-NO

0.0 0.0 7

*HEAT SLAB... IL SG INLET-OUTLET PLENUM - TOP RECTANGULAR SECTION *

*LEFT BOUNDARY = COMPONENTS 210 & 230 *RIGHT BOUNDARY = AMBIENT VOLUME (808)

*GL DATA

12100000

*MESH

12100100

*GEOMIETRY

12100101

*MATERIALS

12100201

*SOURCE DIS

12100301

*INIT TEMP

12100400

NH

2

LOC FIJO

0

NP

10

TYPE

2

S-FLG L-COR

1 .329989

FRI FLG

1

NO ITV R-COR NO ITV R-COR

7 .958333 2 1.125

CMP NO ITV NO CMP NO

1 7 26

ITV NO

9

SOURCE

0.0

ITV NO

9

FLG

-1

*TEMP DISTRIBUTION
12100401

12100402

*L-BNDY

12100501

*R-BNDY

12100601

12100602

*SOURCE

12100701

*L-H-ST

12100801

606.0 600.0

68.0

540.0 534.0

68.0

HY-VOL

210010000

230010000

BlY-VOL

808010000

808010000

TYPE

0

597.0 594.0 591.0 588.0 585.0 582.0 325.0

531.0 528.0 525.0 522.0 519.0 516.0 292.0

INC

0

0

B-CDT A-CODE

INC B-CDT A-CODE

0 4100

0 4100

CY-LENGTH

0. 078125

0. 078125

CY-LENGTH

0.078125

0.078125

R-DR-HT

0

HI-SIR-NO

2

HI-SIR-NO

1

2

HI-STR-NO

2

HI-SIR-NO

2

IS-M'LPR

0

L-DR-HT

0

H-EQ-DIA

.5192263

CHF-HTR HY-DIA

0 .3258603

CH-LENGTH

0.156250

*R-H-ST CHF-HTR HY-DIA

12100901 0 0.0o

H-EQ-DIA CH-LENGTH HT-STR-NO

0.0 0.156250 2

*HEAT SLAB... IL SG INLET-OUTLET PLENUM -MIDDLE TRAPIZOIDAL SECTION*

~*LEFT-BOUNDARY = COMPONENTS 210 & 230

*RIGHT BOUNDARY =AMBIENT VOLUME (808)

*GL DATA

12101000

*MESH

NH

2

LOC FLG

0

NP

11

TYPE S-FLG L-COR

2 1 .243733

FRN FLG

1

*GEOMETRY NO ITV R-COR NO ITV

12101101 1 .333333 7

*MATERIALS

12101201

*SOURCE DIS

12101301

*INIT TEMP

12101400

R-COR

.958333

ITV NO

10

NO ITV R-COR

2 1.125

CMP NO ITV NO

1 8

CMP NO

26

SOURCE

0.0

ITV NO

10

FLG

-1

*TEMP DISTRIBUTION

12101401 606.0 603.0

+ 325.0 68.0

12101402 540.0 537.0

+ 292.0 68.0

600.0 597.0

534.0 531.0

594.0 591.0 588.0 585.0 58Z.0

528.0 525.0 522.0 519.0 516.0

*L-BNDY

12101501

12101502

*R-BNDY

12101601

12101602

BY-VOL

210010000

230010000

flY-VOL

808010000

8080110000

INC

0

0

B-CDT A-CODE CY-LENGTH

1 0.072917

1 0.072917

HT-STR-NO

1

2

HI-SIR-NO

1

2

INC B-CDT

0 4100.

0 4100

A-CODE CY-LENGTH

0. 072917

0.072917
*SOURCE TYPE IS-MLPR L-DR-HT R-DR-HT HT-STR-NO

12101701 0 0 0 0 2

*L-H-ST CHF-HTR .HY-DIA H-EQ-DIA OH-LENGTH HT-STR-NO

12101801 0 .2513333 .4800904 0.145834 2

*R-H-ST CHF-HTR HY-DIA H-EQ-DIA CH-LENGTH HT-STR-NO

12101901 0 0.0 0.0 0.145834 2

*HEAT SLAB... IL SG INLET-OUTLET PLENUM - BOTTOM TRAPIZOIDAL SECTION*

*LEFT BOUNDARY COMPONENTS 210 & 230

*RIGHT BOUNDARY =AMBIENT VOLUME (808)

*GL DATA NH NP TYPE S-FLG L-COR

12102000 2 4 2 1 .243733-

*MESH LOC Ff20 FRM PLO

12102100 0 1

*GEOMETRY NO ITV R-COR NO ITV R-COR

12102101 1 .333333 2 0.5

,ýMATERIALS CMP NO ITV NO CMP NO ITV NO

12102201 1 1 263

*SOURCE DIS SOURCE ITV NO

12102301 0.0 3

*INIT TEMP FLG

12102400 -1

*TEMP DISTRIBUTION

12102401 606.0 582.0 325.0 80.0

12102402 540.0 516.0 292.0 80.0

*L-BNDY HY-VOL INC B-CDT A-CODE CY-LENGTH HT-STR-NO

12102501 210010000 0 1 1 0.166667 1

12102502 230010000 0 1 1 0.166667 2

*R-BNDY HY-VOL INC B-CDT A-CODE CY-LENGTH HT-STR-NO

12102601 808010000 0 4100 1 0.166667 1

12102602 808010000 0 4100 1 0.166667 2

*SOURCE TYPE IS-MLPR L-DR-HT R-DR-HT HT-STR-NO

12102701 0 0 0 0 2

*L-H-ST CHF-HTR HY-DIA H-EQ-DIA OH-LENGTH HT-STR-NO

12102801 0 .2513333 .4800904 0.333334 2

*R-H-ST CHE-HIR HY-DIA H-EQ-DIA OH-LENGTH HT-STR-NO

12102901 0 0.0 0.0 0.333334 2

*HEAT SLAB... IL SG PLENUM BETWEEN UP & DN STREAM RECTANGULAR SECTION*

*LEFT BOUNDARY = COMPONENT 210

*RIGHT BOUNDARY = COMPONENT 230
*GL DATA NH

12103000 1

*M1ESH LOC FIG

12103100 0

*GEOMERTY NO ITV

12103101 3

*MATERIALS CHP NO

12103201 1

*SOUR .CE DIS SOURCE

12103301 0.0

*INIT TEMP FLG

12103400 -1

*TEMP DISTRIBUTION

12103401 606.0 584.0

*L-BNDY HY-VOL

12103501 210010000

*R-BNDY HY-VOL

12103601 230010000

*SOURCE TYPE

12103701 0

*L-H-ST CHF-HTR

12103801 0

*R-H-ST CHF-HTR

12103901 0

NP

4

FRM FLG

1

R-COR

.095417

ITV NO

3

ITV NO

3

TYPE

1

S-FIG

1

L-COR

0.0

562.0 540.0

INC

0

INC

0

IS-MIPR

0

HY-DIA

.3258603

HY-DIA

.3258603

B-CDT A-CODE

1 0

B-CDT A-CODE

.1 . 0

L-DR-HT

0

SURF-AREA

0.102761

SURF-AREA

.0.10Z761

R-DR-HT

0

CH-LENGTH

0. 156250

CH-LENGTH

0.156250

HT-STR -NO

HT-STR-NO

HT-STR-NO

1

HT-STR-NO

1

H-EQ-DIA

0.875000

H-EQ-DIA

0.875000

*HEAT SLAB... IL SG PLENUM BETWEEN UP & DN STREAM TRAPIZOIDAL SECTION*

"* ETBUDR OPNN 1

" RIEFT BOUNDARY = COMPONENT 210

*GI DATA NH NP

12104000 1 4

*MESH - LOG FIG FRM FIG

12104100 0 1

TYPE S-FIG 1-COR

1 1 0.0

*GEOM1ERTY

12104101

*MATERIALS

12104201

*SOURCE DIS

12104301

*INIT TEMP

12104400

NO ITV

3

CNP NO

1

SOURCE

0.0

FLG

-1

R-COR

.162938

ITV NO

3

ITV NO

3
*TEMP DISTRIBUTION

12104401 606.0 584.0 562.0 540.0

*L-BNDY HY-VOL

12104501 210010000

*R-BNDY HY-VOL

12104601 230010000

INC

0

B-CDT A-CODE SURF-AREA

1 0 0.229152

HT-STR-NO

1

INC B-CDT A-CODE SURF-AREA HT-STR-NO

0 1 0 0.229152 1

*SOURCE

12104701

TYPE IS-MLPR

0 0

L-DR-IIT

0

H-EQ-DIA

.5274709

R-DR-HT HT-STR-NO

0 1

CH-LENGTH HT-STR-NO

0.479167 1

*L-H-ST CHF-HTR HY-DIA

12104801 0 .2513333

*R-H-ST

12104901

CHF-HTR HY-DIA

0 .2513333

H-EQ-DIA CH-LENGTH HT-STR-NO

.5274709 0.479167 1

*HEAT SLABS... IL SO TUBE SHEET FLANGES - UP(1) & DOWNSTREAM()

*LEFT BOUNDARY = COMPONENTS 215 & 225 *RIGHT BOUNDARY =AMBIENT VOLUME (808)

*GL DATA

12150000

NH .- --NP TYPE S-FLG L-COR

2 .14 2 1 .212031

*MESH LOC FLG FMT FLG

12150100- 0 1

*GEON1ERTY

12150101

12150102

*MATERIALS

12150201

12150202

*SOURCE DIS

1 2150301

*INIT TEMI'

12150400

NO ITV R-COR

1 .216114

1 .528545

NO ITV

1

5

CMI' NO

13

R-COR

.216406

.958333

ITV NO

2

NO ITV

3

2

CMI' NO

25

R-COR

.447917

1.12500

ITV NO

11

CMI' NO

5

26

SOURCE

0.0

ITV NO

1

13

ITV NO

13

FLG

-1

*TEMIP DISTRIBUTION

12150401 606.0 605.5

+ . 594 .0 592.0

12150402 540.0 539.5

+ 529.2 527.4

605.0

590.0

539.0

526 .6

INC

0

0

604.5

329.0

538.6

296.6

604.0

80.0

538.2

80.0

601.0 600.0 598.0 596.0

536.4 534.6 532.8 531.0

*L-BNDY

12150501

12150502

*R-BNDY

12150601

12150602

*SOURCE

HY-VOL

215010000

225010000

HY-VOL

808010000

808010000

B-CDT A-CODE CY-LENGTH

1 1 0.380208

1 1 0.380208

HT-STR-NO

1

2

HT-STR-NO

1

2

INC B-CDT

0 4100

0 4100

A-CODE CY-LENGTH

0.380208

0.380208

TYPE IS-MLPR L-DR-H! R-DR-HTRH HT-STR-NO TSRN
12150701 0 0 0 0 2

4L-H-ST CHF-HTR HY-DIA

12150801 0 0.064750

FI-EQ-DIA CH-LENGTH HT-SIR-NO

0.120724 0.760417 2

H-EQ-DIA Gil-LENGTH UT-SIR-NO

0.0 0.760417 2

*R-H-ST

12150901

CHF-HTR

0

HY-D IAP

0.0

B EAT SLABS... IL SG TUBE SHEET CONICAL SECTION - UP(1), DWNSTREAM(2)*

" LEFT BOUNDARY =COMPONENTS 215 & 225

" RIGHT BOUNDARY AMBIENT VOLUME (808)

*GL DATA

12151000

*MESH

12151100

*GEONERTY

12151101

12151102

*MIATERIALS

12151201

12151202

*SOURCE DIS

12151301

*INlT TEMP

12151400

NH

2

LOC FIG

0

NP

9

TYPE S-FLG L-COR

2 1 .212031

PIT FIG

1

NO ITV R-COR

1 .216114

1 .528545

NO ITV

1

2

CMP NO

13

R-COR

.216406

.695211

ITV NO

2

NO ITV

3

R-COR

.447917

CMP NO

5

26

SOURCE

0.0

ITV NO

1

8

ITV NO

8

CMP NO ITV NO

.25. . 6

FLG

-1

*EPDISTRIBUTION

12151401 606.0 605.5

12151402 540.0 539.5

605.0 604.0 600.0 595.0 590.0 329.0

539.0 536.4 534.6 530.8 526.6 296.6

80.0

80.0

*L-BNDY

12151501

12151502

*R-BNDY

12151601

12151602

*SOURCE,

12151701

*L-H-ST

12151801

*R-H-ST

12151901

HY-VOL

215010000

225010000

HY-VOL

808010000

808010000

INC

0

0

B-CDT A-CODE

1-OD

1

1

CY-LENGTH

0.327925

0.327925

CY-LENGTH

0.327925

0. 327925

HI-SIR-NO

1

2

HI-SIR-NO

.1

2

INC B-CDT

0 4100

0 4100

TYPE lS-MIPR

0 0

CHF-HTR HY-DIA

0 0.064750

L -DR-HI

0

H-EQ-DIA

0.120724

H-EQ-DIA

0.0

R-DR-HI HI-SIR-NO

0 2

CH-LENGTH HI-SIR-NO

0.655849 2

CH-LENGTH HI-SIR-NO

0.739583 2

CHE-HIR

0

HY-DIA

0.0

*HEAT SLABS... IL SG TUBE SHEET CENTER SECTION -UP(1) & DOWNSTREAM(2)*

*LEFT BOUN DARY =COMPONE'NTS
* RIGHT BOUNDARY = AMBIENT VOLUME (808)

*GL DATA

12152000

*MESH

12152100

*GEOM1ERTY

12152101

12152102

*MA1TERIALS

12152201

12152202

*SOURCE DIS

12152301

*INIT TEMP

12152400

NH

2

NP

8

TYPE

2

S-FLG L-COR

1 .212031

LOC FLG FMTr FLO

0 1

NO ITV R-COR

1 .216114

2 .614583

NO ITV

1

CMP NO

13

R-COR

.216406

ITV NO

2

NO ITV R-COR

3 .447917

CMP NO

b

26

SOURCE

0.0

ITV NO

1

7

ITV NO

7

CMP NO

25

ITV NO

5

FLG

-1

*TEMP DISTRIBUTION

12152401 606.0 605.5

12152402 540.0 539.5

605.0 604.0 600.0

539.0 536.4 534.6

590.0 329.0

530.8 296.6

80.0

80.0

*L-BNDY

12152501

12152502

*R-BNDY

12152601

12152602

HY-VOL

215010000

225010000

HY-VOL

808010000

808010000

ING

0

0

B-CDT. A-CODE CY7.LENGTfL.-

0. 166867

0.166867

CY-LENGTH

0. 166867

0. 166867

HT-STR-NO

1

2

HT-STR-NO

1

2

I NC B-CDT

0 4100

0 4100

A-CODE

1

1

*SOURCE TYPE IS-MLPR

12152701 0 0

*L-H-ST CHF-HTR HY-DIA

12152801 0 0.064750

*R-ll-ST CHF-HTR HY-DIA

1215Z901 0 0.0

L-DR-HT

0

R-DR-HT IIT-STR-NO

0 2

H-EQ-DIA CH-LENGTH IIT-STR-NO

0.120724 0.333734 2

H-EQ-DIA CH-LENGTH HT-STR-NO

0.0 0.333734 2

*HEAT SLAB... IL SG TUBE SHEET BETWEEN UP & DN STREAM HYD. VOLUMES *

*LEFT-BOUNDARY = COMPONENT 215 *RIGHT BOUNDARY = COMPONENT 225

*GL DATA NH NP TYPE S-FLG L-COR

12153000 1 4 1 1 0.0

*MESH LOC FLG FRM FLG

12153100 0 1

*GEOMERTY

12153101

*MATERIALS

12153201

NO I-TV R-COR

3 .256517

CMP NO

25

ITV NO
*SOURCE DIS

1Z153301

*INIT TEMP

12153400

SOURCE

0.0

ITV NO

3

FLG

-1

*TEMiP DISTRIBUTION

12153401 606.0 584.0

*L-BNDY HY-VOL

12153501 215010000

*R-BNDY HY-vOL

12153601 225010000

562.0 540.0

INC B-CDT A-CODE SURF-AREA HT-STR-NO

0 1 0 0.693967 1

INC

0

B-CDT

1

A-CODE SURF-AREA HT-STR-NO

0 0.693967 1

*SOURCE

12153701

*L-H-ST

12153801

*R-H-ST

12153901

TYPE IS-M'LPR

0 0

CHF-HTR HY-DIA

O 0.064750

CHF-HTR BY-DIA

0 0.064750

L-DR-HT

0

R-DR-HT }IT-STR-NO

0 - 1

H-EQI-DIA CH-LENGTII HT-STR-NO

0.139652 1.75 1

H-EQ-DIA

0.139652

CH-LENGTH

1.75

HT-STR-NO

1

*HEAT SLAB... BL SG INLET-OUTLET PLENUM - TOP RECTANGULAR-SECTION- *

* LEFT BOUNDARY =COMPONENTS 310 & 330

* RIGHT BOUNDARY = AMBIENT VOLUME (808)

*GL DATA

13100000

NH

2

NP

10

TYPE

2

S-FLG L-COR

1 .329960

*MESH LOG FLG FM[T FLG

13100100 0 1

*GEOMERTY NO ITV R-COR

13100101 7 .958333

NO ITV R-COR

2 1.125

*MATERIALS

13100201

*SOURCE DIS

13100301

*INIT TEMP

13100400

CMP NO ITV NO

1 7

ClIP NO

26

ITV NO

9

SOURCE

0.0

ITV NO

9

FLG

-1

*TEMP DISTRIBUTION

13100401 606.0 600.0

+ 68.0

13100402 540.0 534.0

+ 68.0

597.0 594.0

531.0 528.0

INC B-(

0

0

591.0 588.0 585.0 582.0 325.0

525.0 522.0 519.0 516.0 292.0

*L-BNDY

13100501

13100502

HY-VOL

310010000

330010000

DT A-CODE

11

11

CY-'ftNGTH

0.078125

0.078125

HT-STR-NO

1

2

*R-BNDY HY-VOL *RBD YVLINC B-CDT A-CODE CY-LENGTH HT-STR-NO
13100601 808010000

13100602 808010000

0

0

4100

4100

1

1

0.078125

0. 078125

1

2

*SOURCE

13100701

*L-H-ST

13100801

TYPE IS-MLPR

0 0

CHF-HTR HY-DIA

0 .3258603

L-DR-HT

0

R-DR-HT HT-SIR-NO

0 2

H-EQ-IJIA CH-LENGTH HT-SIR-NO

.5192263 0.156250 2

H-EQ-DIA CH-LENGTH HT-STR-NO

0.0 0.156250 2

*R-H1-ST CHF-HTR HY-DIA

13100901 0 0.0

*HEAT SLAB... BL SG INLET-OUTLET PLENUM - MIDDLE TRAPIZOIDAL SECTION*

*LEFT BOUNDARY = COMPONENTS 310 & 330 *RIGHT BOUNDARY = AM.BIENT VOLUME (808)

*GL DATA

13101000

NH

2

NP

11

TYPE

2

S-FLG L-COR

1 .247205

*MESH LOC FLG

13101100 0

FMT FLG

1

*GEOMERTY NO ITV R-COR NO ITV R-COR

13101101 1 A.~33333 -7 .958333

NO ITV R-COR

2 1.125

*MAIJTERIALS

13101201

*SOURCE DIS

13101301

*INIT TEMP

13101400

CHP NO

I

SOURCE

0.0

ITV NO

8

ITV NO

10

ClIP NO

26

ITV NO

10

FLG

-1

*TEMP DISTRIBUTION

13101401 606.0 603.0

+ 325.0 68.0

13101402 540.0 537.0

+ 292.0 68.0

600.0 597.0

534.0 531.0

594.0 591.0 588.0

528.0 525.0 522.0

585.0 582.0

519.0 516.0

*L-BNDY

13101501

13101502

*R-BNDY'

13101601

13101602

HY-VOL

310010000

330010000

Ply-VOL

808010000

808010000

INC

0

0

B-CDT A-CODE CY-LENGTH

11 0.072917

112 0.072917

HI-SIR-NO

1

2

HT-STR-NO

1

2

INC B-CDT

0 4100

0 4100

A-CODE CY-LENGTH

0. 072917

0.072917

*SOURCE TYPE IS-MLPR

13101701 0 0

*L-H-ST CHF-HTR IIY-DIA

13101801 0 .22438322

*R-H-ST CHF-HTR HY-DIA

13101901 0 0.0

L-DR-HT

0

H-EQ-DIA

.397453?Z

H-EQ-DIA

0.0

R-DR-HT HI-SIR-NO

0 2

CU-LENGTH

0.145834

CH-LENGTH

0.145834

HT-STR-NO

2

HT-STR-NO

2 *

** *********   ** *** **   ** *** *** **   **  **   **  * *s~* * *****   ** * *****
*HEAT SLAB... BL SG INLET-OUTLET PLENUM - BOTTOM TRAPIZOIDAL SECTION*

*LEFT BOUNDARY = COMPONENTS 310 & 330 *RIGHT BOUNDARY = AMBIENT VOLUME (808)

*GL DATA

13102000

*MESH

13102100

NH

2

NP

4

TYPE S-FLG L-COR

2 1 .247205

LOC FLO FMT FLG

0 1

*GEOMERTY NO ITV R-COR

13102101 1 .333333

*MATERIALS CMI' NO ITV NO

13102201 1 1

NO ITV

2

CMI' NO

26

R-COR

0.5

ITV NO

3

*SOURCE DIS

13102301

*INIT TEMP

13102400

SOURCE ITV NO

0.0 3

FLG

-1

*TEMIP DISTRIBUTION

13102401 606.0 582.0 325.0 .80.0

*13102-402 -540.0 516.0 -292.G0- 80.0

*L-BNDY

13102501

13102502

*R-BNDY

13102601

13102602

*SOURCE

13102701

NY-VOL

310010000

330010000

HY-VOL

808010000

808010000

TYPE

0

INC

0

0

B-CDT A-CODE

A-CODE

CY-LENGTH

0.250000

0. 250000

CY-LENGTH

0.250000

0.250000

HT-STR-NO

1

2

HT-STR-NO

1

2

INC B-CDT

0 4100

0 4100

IS-MLPR

0

L-DR-HT

0

R-DR-HT HT-STR-NO

0 2

*L-H-ST CHF-HTR HY-DIA

13102801 0 .2243822

*R-H-ST CHF-IITR HY-DIA

13102901 0 0.0

H-EQ-DIA CH-LENGTH HT-STR-NO

.3974532 0.500000 2

H-EQ-DIA CH-LENGTH HT-STR-NO

0.0 0.500000 2

*HEAT SLAB... BL SG PLENUM BETWEEN UP & DN STREAM RECTANGULAR SECTION*

*LEFT BOUNDARY = COMPONENT 310 *RIGHT BOUNDARY = COMPONENT 330

*GL DATA

13103000

13103100

*GE0O1ERT.Y

13103101

Nil

1

NP TYPE S-FLG L-COR

4 1. 1 0.0

FRI FLG

1

LOC FLG

0

NO ITV R-COR

3 .095333
*MATERIALS

13103201

*SOURCE DIS

13103301

*INIT TEMP

13103400

CMP NO

1

SOURCE

0.0

ITV NO

3

ITV NO

3

FLG

-1

*TEMP DISTRIBUTION

13103401 606.0 584.0

*L-BNDY IIY-VOL

13103501 310010000

562.0 540.0

INC

0

B-CDT A-CODE SURF-AREA

1 0 0.102753

HT-STR-NO

1

*R-BNDY

13103601

*SOURCE

13103701

*L-H-ST

13103801

HY-VOL

330010000

TYPE

0

INC B-CDT A-CODE SURF-AREA HT-STR-NO

0 1 0 0.102753 1

IS-MLPR

0

L-DR-HT

0

H-EQ-DIA

.5192263

R-DR-HT

0

CH -LENGTH

0.156250

CHF-HTR HY-DIA

0 .3258603

-HT-STR-NO

1

HT-STR-NO

1

.HT-STR-NO

1

*R-H-ST CHF-HTR HY-DIA

13103901 0 .3258603

H-EQ-DIA CH-LENGTII

.5192263- 0.156250

*HEAT SLAB... BL SG PLENUM BETWEEN UP & DN STREAM TRAPIZOIDAL SECTION*

*LEFT BOUNDARY = COMPONENT 310

*RIGHT BOUNDARY =COMPONENT 330

*GL DATA

13104000

*M'ESH

13104100

NH

I

NP

4

TYPE

I

S-FLG L-COR

1 0.0

LOG FLG FRI FLG

0 1

*GEOMERTY NO ITV R-COR

13104101 3 .222145

*MATERIALS

13104201

*SOURCE DIS

13104301

*INIT TEMP

13104400

CMP NO ITV NO

1 3

SOURCE

0.0

ITV NO

3

FLG

-1

*TEMP DISTRIBUTION

13104401 606.0 584.0- 562.0 540.0

*L-BNDY

13104501

*R-BNDY

13104601

HY-VOL

310010000

HY-VOL

330010000

INC B--CDT

0 1

A-CODE SURF-AREA

0' 0.2.28673

A-CODE SURF-AREA

0 0.228673

HT-STR-NO

1

HT-STR-NO

1

INmC

0

B-CDT

1
*SOURCE

13104701

*L-H-ST

13104801

*--ST

13104901

TYPE IS-MLPR

0 0

CHF-IITR BY-DIA

0 .2243822

CHF-HTR HY-DIA

0 .2243822

L-DR-iIT

0

R-DR-HT HT-STR-NO

0 1

H-EQ-DIA CH-LENGTH HT-STR-NO

.515Z883 0.479167 1

H-EQ-DIA CM-LENGTH HT-STR-NO

.5152883 0.479167 1

*HEAT SLABS... BL SG TUBE SHEET FLANGES - UP(1) & OWiNSTREAM(2)*

*LEFT BOUNDARY COMPONENTS 315 & 325 *RIGHT BOUNDARY =AMBIENT VOLUME (808)

*GL DATA

13150000

NH

2

*ME~SH LOC FLG

13150100 0

*GEOMERTY

13150101

13150102

13150103

*MIATERIALS

13150201

13150202

*SOURCE DIS

13150301

*INIT TEMP

13150400

NO ITV

2

CMP NO

5

26

NP

15

FRM FLG

R-COR

.1331511

.2916667

1.1250000

ITV NO

1

14

TYPE

2

S-FLG L-COR

1 .1277344

NO ITV R-COR

1 .1334427

2 -.4634361

NO ITV R-COR

1 .1958013

6 .9583333

*CHP NO

13

ITV NO

2

CMP NO

25

ITV NO

12

SOURCE ITV NO

0.0 14

FLG

-1

*TEMP DISTRIBUTION

13150401 606.0 605.5

+ 594.0 593.0

13150402 540.0 539.5

+ 529.2 528.3

605.0

592. 0

539.0

527.4

604.5

590.0

538.6

526.2

604.0

329. 0

538.2

296.6

601.0

80.0

536.4

80.0

600.0 598.0 596.0

534.6 532.8 531.0

*L-BNDY

13150501

13150502

*R-BNDY

13150601

13150602

*SOURCE

13150701

*L-H -ST

13150801

*R-H-ST

13150901

HY-VOL

315010000

325010000

HY-VOL

808010000

808010000

INC

0

0

B-CDT A-CODE GY-TLENGTH

0.203125

0.203125

CY-LENGTH

0. 203125

0.203125

INC B -CDT

O 4100

0 4100

A-CODE

HT-STR-NO

1

2

IIT-STR-NO

1

2

HT-STR-NO

2

HT-STR-NO

2

AT-STR-NO

2

TYPE IS-MLPR L-DR-HT

0

R-DR-HT

0

CHF-HTR HY-DIA

0 .0620833

H-EQ-DIA. 'CH-LENGTH

.1167128 0-.406250

H-EQ-fl , C H-LENGTH

0.0 0.406250

CHF-HTR

0

HY-DIA

0.0
*HEAT SLABS... BL SG TUBE SHEET CONICAL SECTION - UP(1), DOWNSTREAM(2)*

*LEFT BOUNDARY = COMPONENTS 315 & 325 *RIGHT BOUNDARY = AMBIENT VOLUME (808)

*GL DATA NH NP TYPE S-FLG L-COR

13151000 2 9 2 1 .1277344

*MESH

13151100

*GEOMERTY

13151101

13151102

*MATERIALS

13151201

13151202

*SOURCE DIS

13151301

*INIT TEMP

13151400

LOC FLG

0

FRM FLG

1

NO ITV R-COR

'1 .1331511

1 .2916667

NO ITV

1

2

R-COR

.1334427

.4634361

NO ITV R-COR

1 .1958013

2 .6301027

CMP NO

5

26

ITV NO

1

8

CMP NO ITV NO CMP NO ITV NO

13 2 25 6

SOURCE ITV NO

0.0 8

FLG

-1

*TEIIP DISTRIBUTIO0N.

13151401 606.0* 605.5

13151402 540.0 539.5

605.0

539.0

604.0 600.0 595.0

536.4 534.6 530.8

590.0 329.0

526.6 296.6

80.0

80.0

*L-BNDY

13151501

13151502

*R-BNDY

13151601

13151602

*SOURCE

13151701

*L-H -ST

13151801

*R-H-ST

13151901

HY-VOL

315010000

325010000

HY-VOL

808010000

808010000

INC

0

0

B-CDT A-CODE CY-LENGTH

.2966746

.2966746

CY-LENGTH

.2966746

.2966746

HT-STR-NO

1

2

HT-STR-NO

1

2

INC B-CDT

0 4100

0 4100

A-CODE

TYPE IS-MLPR

0 0

CHF-HTR HY-DIA

0 .0620833

CHF-HTR HY-DIA

0 0.0

L -DR-HT

0

R-DR-HT HT-STR-NO

0 2

H-EQ-DIA CH-LENGTH HT-STR-NO

.1167128 0.6770833 2

H-EQ-DIA CH-LENGTH HT-STR-NO

0.0 0.6770833 2

*-HEAT SLABS... BL SG TUBE SHEET CYLINDRICAL SECTION - UP(1) & DOWN(2)*

* LEFT BOUNDARY = COMPONENTS 315 & 325

" RIGHT BOUNDARY = AMBIENT..VOLUME (808)

*GL DATA

13152000

NH

2

NP

7

TYPE S-FLG L-COR

2 1 .1277344

*MESH LOC FLG FRM FLG

13152100 0 1

*GEOMERTY NO ITV R-COR NO ITV R-COR NO ITV R-COR
13152101

13152102

*MATERIALS

13152201

13152202

*SOURCE DIS

13152301

*INIT TEMP

13152400

1

1

.1331511

.2916667

1

2

.1334427

.4583333

1 .1958013

CMP NO

5

26

SOURCE

0.0

ITV NO

1

6

ITV NO

6

CHP NO

13

ITV NO

2

CMP NO

25

ITV NO

4

FLG

-1

*ThMP DISTRIBUTION

13152401 606.0 605.0

13152402 540.0 539.0

604.0 600.0 590.0 329.0

536.4 534.6 530.8 296.6

80.0

80.0

*L-BNDY

13152501

13152502

*R-BNDY

13152601

13152602

*SOURCE - 131527&1-

HY-VOL

315010000

325010000

flY-VOL

808010000

808010000

INC

0

0

B-CDT A-CODE

A-CODE

CY-LENGTH

0.2920754

0.2920754

CY-LENGTH

0.2920754

0.2920754

HT-STR-NO

2

HT-STR-NO

1

2

INC B-CDT

0 4100

0 4100

TYPE IS-NLPR

-0 0

L-DR-HT

0

R-DR-HT HT-STR-NO

*L-H-ST CHF-HTR HY-DIA

13152801 0 .0620833

H-EQ-DIA CH-LENGTH HT-STR-NO

.1167128 0.5841508 2

*R-H-ST

13152901 0 0.0 0.0 0.5841508 2

*HEAT SLABS... BI, SG TUBE SHEET HUB SECTION - UP(1 & DOWNSTREAM1(2) *

* LEFT BOUNDARY

* RIGHT BOUNDARY

COMPONENTS 315 & 325

AMBIENT VOLUME (808)

*GL DATA

13153000

*MES11

13153100

*GEOMERTY

13153101

13153102

*KATERIALS

13153201

13153202

*SOURCE DIS

13153301

*INIT TEMP

13153400

NH

2

NP

6

TYPE S-FLG L-COR

2 .1 .1277344

LOG FLG

0

FRM FLG

1

NO ITV R-COR

1 .1331511

2 .3624679

NO ITV R-COR

1 .1334427

NO ITV R-COR

1 .1958013

CMP NO

5

26

SOURCE

0.0

ITV NO

1

5

ITV NO

5

CMP No

- 13

ITV NO

2

CUP NO

25

ITV NO

3

FLG

-1
*TENP DISTRIBUTION

13153401 606.0 604.0

13153402 540.0 536.4

600.0 590.0 329.0

534.6 530.8 296.6

80.0

80.0

*L-BNDY

13153501

13153502

*R-BNDY

13153601

13153602

* SOURCE

13153701

*L-H-ST

13153801

*R-H-ST

13153901

HY-VOL

315010000

325010000

HY-VOL

808010000

808010000

INC

0

0

B-CDT A-CODE CY-LENGTH

0.0835417

0 .0835417

CY-LENGTH

0.0835417

0.0835417

INC B-CDT

0 4100

0 4100

A-CODE

HT-STR-NO

2

HT-STR-NO

1

2

HT-STR-NO

2

TYPE IS-MLPR

10 0

CHF-HTR BY-DIA

0 .0620833

CIIF-JITR HY-DIA

0 0.0

L-DR-HT

0

R-DR-HT

0

ll-EQ-DIA CH-LENGTH HT-STR-NO

.1167128 0.1670833 2

H-EQ-DIA CH-LENGTH

0.0 0.1670833

-HT-STR-NO

2

*HEAT SLAB... BL SG TUBE SHEET BETW4EEN UP & DN STREAM HYD. VOLUMES*

"* ETBUDR OPNN 1

" RIEHT BOUNDARY = COMPONENT 315

*GL DATA

13154000

*MESH

13154100

NH

1

NP

3

TYPE S-FLG L-COR

1 1 0.0

LOG FLG

0

FRM FLG

1

*GEOMERTY NO ITV R-COR

13154101 2 .165750

*MATERIALS

13154201

*SOURCE DIS

13154301

*INIT TEMP

13154400

CMP NO

25

SOURCE

0.0

ITV NO

2

ITV NO

2

FLG

-1

*TEMIP DISTRIBUTION

13154401 606.0 573.0

*L-BNDY HY-VOL

13154501 315010000

*R-BNDY HY-VOL

13154601 3250.10000

540.0

INC B-CDT A-CODE SURF AREA HT-STR-NO

0 1 0 0.41354201

INC B-CDT -A-CODE SURF AREA

0 1 .0 -0.4135420

HT-STR-NO

1

HT-STR-NO

1

*SOURCE

13154701

*L-H-ST

13154801

TYPE IS-MLPR

0 0

CHF-HTR HY-DIA

0 .6020833

L-DR-HT

0

R-DR-HT

0

H-EQ-DIA CH-LENGTH HT-STR-NO

.1326376 1.751830 1
*R-H-ST CHF-HTR HY-DIA

13154901 0 0.064750 11-EQ-HIA

0.064750

CH-LENGTH

1.751830

HT-STR-NO

1

*HEAT SLAB... INTACT & BROKEN LOOP, 3 IN. SCH-160 PIPING*

* ~NOTE - CONTAINS ONLY VOLUME LENGTHS WHICH*

* ~ARE HEATED BY HEATER TAPE.

" LEFT BOUNDARY = COMPONENTS 201,261,262,263,301,363

" RIGHT BOUNDARY = AMBIENT VOLUMES (811 & 813)

*GL DATA

12002000

*MESH

12002100

*GEOMETRY

12002101

12002102

*MATERIALS

12002201

12002202

*SOURCE DIS

12002301

*INIT TEMP

12002400

NH

'8

NP

8

TYPE S-FLG L-COR

2 1 .10933333

LOG FLG

0

FRM FLG

1

NO ITV R-COR

2 .14583333

2 ..32301667

CMP NO ITV NO

1 2

16 7

NO ITV

1

CMP NO

13

R-COR NO ITV *R-COR

.1459333 2 .156350

ITV NO

3

CMP NO

.9

ITV NO

5

SOURCE- .ITV.NO SOURCE

0.0 3- 1.0

SITV NO

5

.SOURCE-.- ITV...NO.

0.0 ' - 7

FLG

0

MESH

1

6

12002401

12002402

*L-BNDY

12002501

12002502

12002503

1200Z504

12002505

12002506

12002507

12002508

*R-BNDY

12002601

12002602

12002603

12002604

12002605

12002606

12002607

12002608

*SOURCE

12002701

12002u"Z70 2

12002-703

12002704

TEMP

548.9

606.3

TEMP

560.4

357.7

MESH

2

7

TEMP

570.4

154.3

HY-VOL

201010000

201020000

261010000

26102O000

262010000

263010000

301010000

363020000

HY-VOL

811010000

811010000

813010000

813010000

813010000

813010000

811010000

813010000

TYPE

110

110

112

112

INC

0

0

0

0

0

0

0

0

B-CDT

1

1

1

1

1

1

1

1

MESH

3

8

A-CODE

TEMP MESH

590.2 4

CY-LENGTH

0.18189

0.54567

1.03188

0. 78704

0.72757

0.54567

0.72757

0.36378

INC

0

0

0

0

0

0

0

IS-MPLR

.013207

.039077

.246930

.186657

B-CDT A-CODE

4100 1

4100 1

4100 1

4100 1

4100 1

4100 1

4100 1

4100 1

L-DR-HT

0

0

0

0

CY-LENGTH

0.18189

0,54567

1.03188

0.78704

0.72757

0. 54567

0. 72757

0.361378

R-DR-HT

0

0

0

0

TEMP MESH

604.8 5

HT-STR-NO

1

2

3

4

5

6

7

8

HT-STR-NO

1

2

3

4

5

6

7

8

HT-STR-NtO

1

2

3

4
12002705

12002706

12002707

12002708

*L.-H-ST

12002801

112

112

110

112

.174759

.129414

.052769

.087280

0

0

0

0

0

0

0

0

5

6

7

8

CHF-HTR HY-DIA

0 0.0

H-EQ-D IA

0.0

CH-LENGTH

0. 218666

HT-STR-NO

8

*R-H-ST CHF-HTR HY-DIA

12002901 0 0.0

H-EQ-flIA CH-LENGTH HT-STR-NO

0.0 0.218666 8

*HEAT SLAB... INTACT LOOP, 3 IN. SCH-160 PIPING*

* ~NOTE' - HEAT SLAB CONTAINS ONLY VOLUME LENGTHS WHICH *

* ~ARE NOT HEATED*

*LEFT BOUNDARY = INTACT LOOP PRIMARY COOLANT (201,261,262,263) *RIGHT BOUNDARY = AMBIENT VOLUMES (801 & 803)

*GL DATA

12003000

*M1ESH

12003100

NH

6

NP

5

TYPE S-FLG L-COR

2 1 0.10933333

LOC FLG

0

FRM FLG

1

* ACTUAL WALL

*GEOMETRY NO ITV

12003101 2

THK. MULT BY_~2.0 .TO ACCOUNT. OR CLAMP+HUB MASS

R-COR

0.182333

NO ITV R-COR

2 0.349000

0.43233 FOR 3 IN. OF INSUL

*MATERIALS

12003201

*SOURCE DIS

12003301

*INIT TEMP

12003400

CMP NO

1

ITV NO

2

CMP NO

16

ITV NO

4

SOURCE ITV NO

0.0 4

FLG

0

12003401

*L-BNDY

12003501

12003502

12003503

12003504

12003505

12003506

*R-BNDY

12003601

12003602

12003603

12003604

12003605

12003606

*SOURCE

12003701

TEMP MESH

550.5 1

HY-VOL

-201010000

201020000

261010000

26102O000

262010000

263010000

HY-VOL

801010000

801010000

803010000

803010000

803010000

803010000

TEMP MESH

544.9 2

TEMP MESH

540.8 3

INC

0

0

0

0

0

0

INC

0

0

0

0

0

0

B -CDT

1

1

1

1

1

1

A-CODE

1

1

1

TEMP MESH

328.2 1 4

CY-LENGTH

2.46061

0. 75516

1.04479

1. 28963

1.34910

1.60783

CY-LENGTH

2. 46061

0.75516

1.04479

1. 28963

1.34910

1.60783

TEMP MESH

147.7 5

HT-STR-NO

1

2

3

4

5

6

HT-STR-NO

1

2

3

4

5

6

B-CDT A-CODE

4100 1

4100. 1

4100 1

4100 1

4100 1i

41001

TYPE

0

IS-MLPR

0

b-DR-HT

0

R-DR-HT HT-STR-NIO

0 6
*L-H-ST

12003801

*R-H-ST

12003901

CHF-HTR HY-DIA

0 0.0

CHF-HTR HY-DIA

0 0.0

H-EQ-DIA

0.0

CU-LENGTH

0.218666

HT-STR-NO

6

H-EQ-DIA CH-LENGTH Hi-STR-NO

0.0 0.218666 6

*HEAT SLAB... INTA~CT LOOP , 2 1/2 IN. SCH-160 PIPING*

* NOTE -HEAT SLAB CONTAINS ONLY VOLUME LENGTHS WHICH *

* ~ARE HEATED WITH HEATER TAPE.*

*LEFT BOUNDARY INTACT LOOP PRIMARY COOLANT (201,202,203,240) *RIGHT BOUNDARY =AMBIENT VOLUMES (811 & 814)

*GL DATA

12004000

NH

15

NP

8

TYPE S-FLG L-COR

2 1 0.088542

*MESH LOC FLG FRM FLG

12004100 0 1

*GEOMETRY

12004101

12004102

*MATERIALS

12004201

12004202

*SOURCE DIS

12004301

*INIi TEMP

12004400

NO ITV R-COR

2 0.119792

2 0.296975

C0P. NO.

1

16

SOURCE

0.0

ITV NIo

2

7

ITV NO

3

NO IiV

1

CMP..NO

13

SOURCE

1.0

R-COR

0.119892

ITV NO

3

ITV NO

5

NO ITV R-COR

2 0.130309

CMP NO

9

SOURCE

0.0

ITV NO

5

ITV NO

7

FLG

0

* TEMP MESH

12004401 563.0 4

TEMP MESH

583.4 5

*L-BNDY

12004501

12004502

12004503

12004504

12004505

12004506

12004507

12004508

12004509

12004510

12004511

12004512

12004513

12004514

12004515

*R-BNDY

12004601

12004602

12004603

12004604

HY-VOL

201020000

202010000

203010000

203020000

203030000

240010000

240020000

240030000

240030000

240040000

240050000

240060000

240070000

Z4008~0000

240090000

HY-VOL

811010000

811010000

811010000

811010000

ING

0

0

0

0

0

0

0

0

0

0

0

-0

0

0

INC

0

0

0

0

TEMP MESH TEMP MESH

582.8 6 342.0 7

B-CDT A-CODE CY-LENGTH

1 1 0.88573

1 1 1.77146

1 1 1.99290

1 1 0.66430

1 1 0.88573

1 1 0.88573

1 1 1.55003

11 0.66430

11 1.77146

11 2.21433

11 3.08856

11 1.34009

11 1.34009

11-- 3.08856

11 2.65719

B-CDT A-CODE CY-LENGTH

4100 1 0.88573

4100 1 1.77146

4100 1 1.99290

4100 1 0.66430

TEMP MESH

149.9 8

Hi-SiR-NO

1

2

3

4

5

6

7

8

9

10

11

12

13

14

15

HT-STR-NO

1

2

3

4
12004605

12004606

12004607

12004608

12004609

12004610

12004611

12004612

12004613

12004614

12004615

*SOURCE

12004701

12004702

12004703

12004704

12004705

12004706

12004707

12004708

12004709

12004710

12004711

12004712

12004713

12004714

12004715

*L-H-ST

12004801

*R-H-ST

12004901

811010000

811010000

811010000

811010000

814010000

814010000

814010000

814010000

814010000

814010000

814010000

TYPE

110

110

110

110

110

110

110

110

113

113

113

113

113

113

113

CHF-HTR

0

0

0

0

0

0

0

0

0

0

0

0

IS-MPLR

.052769

.105537

.118744

.039077

.052769

.052769

.091845

.039077

.114289

.142829

.199265

.086459

.086459

.199265

.171434

HY-DIA

0.0

4100

4100

4100

4100

4100

4100

4100

4100

4100

4100

4100

1

1

1

1

1

1

1

1

1

1

1

0. 88573

0.88573

1.55003

0. 66430

1.77146

2. 21433

3. 08856

1. 34009

1. 34009

3. 08856

Z. 65719

L-DR-HT

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

H-EQ-DIA

0.0

R-DR-HT

0

0

0

0

0

0

0

0

0

0

0

0

0

0

CH-LENGTH

0. 177084

5

6

7

8

9

10

11

12

13

14

15

HT-STR-NO

1

2

3

4

5

6

7

8

9

10

11

12

13

14

15

HT-STR-NO

15

CHF-HTR HY-DIA

0 0.0

H-EQ-DIA CH-LENGTH HT-STR-NO

0.0 0.177084 15

*HEAT SLAB... INTACT LOOP , 2 1/2 IN. SCH-160 PIPING * ~NOTE - HEAT SLAB CONTAINS ONLY VOLUME LENGTHS W4HICH *

* ~ARE NOT HEATED.*

*LEFT BOUNDARY =INTACT LOOP PRIMARY COOLANT (201,202,203,240) *RIGHT BOUNDARY =AMBIENT VOLUMES (801 & 804)

*GL DATA

12005000

NH

14

NP

5

TYPE

2

S-FLG L-COR

1 0.088542

*MESH - LOG FLG .FRII FLO

12005100 01

*ACTUAL WALL

*GEOMETRY NO ITV

12005101 2

THK. MIJLT.

R-COR

0. 151042

BY 2. 0 TO

NO ITrV

2

ACCOUNT FOR CLAMP + HUB MASS

R-COR

0.-317709

*MATERIALS

12005201

*SOURCE DIS

12005301

CNP NO ITV NO CMP NO ITV NO

12 16 4

SOURCE

0.0

ITV NO

4

*INIT TEMP FLG
12005400

12005401

*L-BNDY

12005501

12005502

12005503

12005504

12005505

12005506

12005507

12005508

12005509

12005510

12005511

12005512

12005513

12005514

*R-BNDY

12005601

12005602

:12005603

12005604

12005605

12005606

12005607

12005608

12005609

12005610

12005611

12005612

12005613

12005614

*SOURCE

12005701

12005801

*R-H-ST

12005901

0

TEMP MESH

550.1 1

HY-VOL

201020000

202010000

203010000

203020000

203030000

240010000

240020000

240030000

240040000

240050000

240060000

240070000

240080000

240090000

HY-VOL

801010000

801010000

801010000

801010000

801010000

801010000

801010000

804010000

804010000

804010000

804010000

804010000

804010000

804010000

TEMP MESH

545.2 2

INC

0

0

0

0

0

0

0

0

0

0

0

0

0

0

TEMP MESH

541.5 3

B-CDT

1

1

1

1

1

1

1

1

1

1

1

1

1

1

A-CODE

1

1

1

1

1

1

1

1

1

1

1

1

1

.1

A-CODE

1

1

1

1

1

1

1

1

1

1

1

1

1

1

TEMP MESH

323.6 4

CY-LENGTH

0. 28510

0.97187

0. 66131

1.66862

1.30272

0. 63605

2. 11622

1.01174

0.68150

0.41907

0.18183

0.18183

0.41907

1.55114

TEMP MESH

146.1 5

HT-STR-NO

1

2

3

4

5

6

7

8

9

10

11

12

13

14

HT-STR-NO

1

2

3

4

5.

6

7

8

.9

10

11

12

13

14

INC

0

0

0

0

0

0

0

0

0

0

0

0

0

0

B-CDT

4100

4100

4100

4100

41100

4100

4100

4100

4100

4100

4100

4100

4100

4100

CY-LENGTH

0. 28510

0.97187

.0.66131

1- 66862 -.1.30272

0.63605

2.11622

1.01174

0.68150

0.41907

0.18183

0. 18183

0.41907

1. 55114

TYPE IS-MPLR

0 0

CHF-HTR

0

CHF-HTR

0

HY-DIA

0.0

HY-DIA

0.0

L-DR-HT

0

H-EQ-DIA

0.0

H-EQ-DIA

0.0

R-DR-HT HT-STR-NO

0 14

CH-LENGTH HT-STR-NO

0.177084 14

CH-LENGTH

0.1717084

HT-STR-NO

14

*HEAT &SAB... BROKEN LOOP - 1 1/2 IN. SCH 160 PIPING*

* ~NOTE - HEAT SLAB CONTAINS ONLY VOLUME LENGTHS WHICH *

* ~ARE HEATED BY HEATER BANDS*

*

*

*

LEFT BOUNDARY =BROKEN LOOP PRIMARY COOLANT (340 -VOLUMES 4,5,7)

RIGHT BOUNDARY AMBIENT VOLUME (812).

*GL DATA

13001000

*MESH

13001100

Nh

3

LOC FLG

0

NP TYPE 'S-FLG

11 2 1

L-ýCOR

.0557500

FRM FLG

1
*GEOMETRY

13001101

13001102

*MATERIALS

13001201

13001202

*SOURCE DIS

13001301

NO ITV R-COR

2 .07916667

3 .09222033

NO ITV R-COR

1 .0792000

1 .094824997

NO ITV R-COR

1 .081804167

2 .261491663

ClIP NO

1

9

SOURCE

0.0

ITV NO

2

7

ITV NO

5

ClIP NO

13

1

SOURCE

1.0

ITV NO

3

8

ITV NO

6

ClIP NO

1

16

SOURCE

0.0

ITV NO

4

10

ITV NO

10

*INIT TEMP

13001400

13001401

13001402

*L-BNDY

13001501

13001502

13001504

*R-BNTJY

13001601

13001602

13001604:

*SOURCE

13001701

13001702

13001704

4L-H-ST

13001801

*R-H-ST

13001901

FLG

TEMP MESH

555.0 1

652.8 7

HY-VOL

340040000

340050000

340090000

flY-VOL

812010000

812010000

81-2010000

TYPE

TEMP MESH

573.4 2

648.0 9

INC

0

0

0

INC

0

0

0

IS-MPLR

.399475

.392056

.036122

TEMP

588.8

363.3

MlESH

3

10

TEMP

605.0

145.0

MESH

5

11

B-CDT A-CODE CY-LENGTH

11 2.29167

11 2.25000

11 0.208333

TEMP MESH 640.0 6

liT-SiR-NO

1

2

3

HT-STR-NO

1

2

HT-STR-NO

2

3

B-CDT

4100

4100

.4100

A-CODE CY-LENGTH

2. 29167

2.25000

.0.20833

R-DR-HT

0

0

0

L-DR-IIT

0

0

0

H-EQ-DIA

0.0

CHF-HTR

0

HY-DIA

0.0

CH-LENGTH HT-STR-NO

0.111500 3

CHF-HTR 'HY-DIA

0 0.0

H-EQ-DIA CH-LENGTH Hi-SiR-NO

0.0 0.111500 3

*HEAT SLAB... BROKEN LOOP - 1 1/2 IN. SCH-160 PIPING*

* ~NOTE - HEAT SLAB CONTAINS ONLY VOLUME LENGTHS WHICH *

* ~ARE HEATED WITH HEATER TAPE.*

*LEFT BOUNDARY = BROKEN LOOP PRIMARY COOLANT (301,340,361,362,363) *RIGHT BOUNDARY = AMBIENT VOLUMES (811,812,813)

*GL -DATA

13002000

*MESH

13002100

*GEOMETRY

13002101

13002102

*MATERIALS

13002201

13002202

NH

17

NP

8

TYPE

2

S-FLG L-COR 1 .05575000

LOG FLG

0

FRtI FLO

1

NO ITV R-COR

2 .07916667

2 .0896840

NO ITV

2

R-COR

.079420000..

.Z56350

ClIP NO

1

16

ITV. NO

2

7

PlIP NO ITV NO ClIP NO

13 3 9

ITV NO

5
*SOURCE DIS SOURCE ITV NO SOURCE ITV NO SOURCE ITV NO

13002301 0.0 3 1.0 5 0.0 7

*INIT TEMP FLG

13002400 0

*TEMP MESH TEHP MIESH TEMP MIESH1 TEMP MIESH TEMP MESH

13002401 548.7 1 545.0 3 542.7 4 536.9 5 531.6 6

13002402 299.4 7 139.1 8

*L-BNDY HY-VOL INC B-CDT A-CODE CY-LENGTH HT-STR-NO

13002501 301010000 0 1 1 0.33506 1

13002502 301020000 0 1 1 0.67013 2

13002503 301030000 0 1 1 1.34025 3

13002504 301040000 0 1 1 1.34025 4

13002505 301050000 0 1 1 0.67013 5

13002506 301060000 0 1 1 1.00519 6

13002507 340010000 0 1 1 0.67013 7

13002508 340020000 0 1 1 0.67013 8

13002509 340030000 0 1 1 0.67013 9

13002510 340040000 0 1 1 1.34026 10

13002511 340050000 0 1 1 0.33506 11

13002512 340060000 0 1 1 0.67013 12

13002513 340070000 0 1 1- 0.67013 13

13002514 340080000 0 1 1 4.35581 14

13002515 361010000 _-.0- ý-, 1 0.33506 15

13002516 362010000 0 1 1 0.67013 16

13002517 363010000 0 1 1 0.33506 17

*R-BNDY HY-VOL INC B-CDT A-CODE CY-LENGTH HT-STR-NO

13002601 811010000 0 4100 1 0.33506 1

13002602 811010000 0 4100 1 0.67013 2

13002603 811010000 0 4100 1 1.34025 3

13002604 811010000 0 4100 1 1.34025 4

13002605 811010000 0 4100 1 0.67013 5

13002606 811010000 0 4100 1 1.00519 6

13002607 811010000 0 4100 1 0.67013 7

13002608 811010000 0 4100 1 0.67013 8

13002609 811010000 0 4100 1 0.67013 9

13002610 811010000 0 4100 1 1.34026 10

13002611 812010000 0 4100 1 0.33506 11

13002612 812010000 0 4100 1 0.67013 12

13002613 812010000 0 4100 1 0.67013 13

13002614 812010000 0 4100 1 4.35581 14

13002615 813010000 0 4100 1 0.33506 15

13002616 813010000 0 4100 1 0.67013 16

13002617 813010000 0 4100 1 0.33506 17

*SOURCE TYPE IS-MIPLR L-DR-P.: R-DR-HT HT-STR-NO

13002701 110 .013207 0 0 1

13002702 110 .026384 0 0 .2

13002703 110 .052769 0 0 3

13002704 110 .052738 0 0 4

13002705 110 .026354 0. 0 5

13002706 ~ 1O .039077 0 0 6

13002707 110 .026354 0. 0 7

13002708 110 .026354 .0 0 8

13002709 110 .026354 0 0 9

13002710 110 .052769 0 0 10

13002711 111 .009585 0 0 11
13002712

13002713

13002714

13002715

13002716

13002717

*L-H-ST

13002801

*R-H-ST

13002901

111

CHF-HTR

0

.019147

.019147

.124468

.043740

.087480

.043740

HY-DIA

0.0

0

0

0

0

0

0

0

0

0

0

0

0

12

13

14

15

16

17

H-EQ-DIA CH-LENGTH HT-STR-NO

0.0 0.111500 17

CHF-HTR HY-DIA

0 0.0

H-EQ-DIA

0.0

CH-IJENGTH

0. 111500

HT-STR-NO

17

*HEAT SLAB... BROKEN LOOP - 1 1/2 IN. SCH-160 PIPING*

* ~NOTE - HEAT SLAB CONTAINS ONLY VOLUME LENGTHS WHICH *

* ~ARE NOT HEATED.*

*LEFT BOUNDARY = BROKEN LOOP PRIMARY COOLANT (301,340,361,362,363) *RIGHT BOUNDARY = AMBIENT VOLUMES (801,802,803)

*GL DATA

13003000

NH

18

NP

5

TYPE S-FLG L-COR

2 1 0.0557500

*MESH LOC FLG FRII FLU

13003100 0 1

*ACTUAL WALL THK. MULT BY 2.0 TO

*GEOMETRY NO ITV R-COR NO ITV

13003101 2 0.1002584 2

ACCT FOR CLAMP+HUB MASS

R-COR

0. 2669251

ITV NO

4

*MATERIALS

13003201

*SOURCE DIS

13003301

*INIT TEMP

13003400

CMP NO ITV NO CMP NO

1 2 16

SOURCE ITV NO

0.0 .4

FLG

0

* TEMP MESH

13003401 549.7 1

TEMP MESH

544.8 2

TEMP MESH

541.5 3

*L-BNDY

13003501

13003502

13003503

13003504

13003505

13003506

13003507

13003508

13003509

13003510

13003511

13003512

13003513

13003514

13003515

13003516

HY-VOL

301010000

301020000

301030000

301040000

301050000

301060000

340010000

340020000

340030000

340040000

340050000

340060000

340070000

340080000

340090000

36101000n

INC

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

B-CDT

1

1

1

1

1

1

1

1

1

1

1

1

1

1

1

1

A-CODE

1

1

1

1

1

1

1

1

1

1

1

I

1

1

1

1

TEMP MESH

306.7 4

CY-LENGTH

0. 49827

1. 54000

0.86987

1. 38427

1. 68796

0.97012

0 .93535

1. 66920

0.97362

1. 31120

1.71140

0.34565

0.3456 5

0.99377

2.08834

1.63494.

TEMP MESH

140.5 5

HT-STR-NO

1

2

3

4

5

6

7

10

13

15

16
13003517 362010000 0 1 1 0.97737 17

13003518 363010000 0 1 1 1.99911 18

*R-BNDY HY-VOL ING B-CDT A-CODE CY-LENGTIT HT-STR-NO

13003601 801010000 0 4100 1 0.498Z7 1

13003602 801010000 0 4100 1 1.54000 2

.13003603 801010000 0 4100 1 0.86987 3

13003604 801010000 0 4100 1 1.38427 4

13003605 801010000 0 4100 1 1.68796 5

13003606 801010000 0 4100 1 0.97012 6

13003607 801010000 0 4100 1 0.93535 7

13003608 801010000 0 4100 1 1.66920 8

13003609 801010000 0 4100 1 0.97362 9

13003610 801010000 0 4100 1 1.31120 10

13003611 802010000 0 4100 1 1.71140 11

13003612 802010000 0 4100 1 0.34565 12

13003613 802010000 0 4100 1 0.34565 13

13003614 802010000 0 4100 1 0.99377 14

13003615 802010000 0 4100 1 2.08834 15

13003616 803010000 0 4100 1 1.63494 16

13003617 803010000 0 4100 1 0.97737 17

13003618 803010000 0 4100 1 1.99911 18

*SOUJRCE TYPE IS-I'LPR L-DR-HT R-DR-HT liT-SIR-NO

13003701 0 0 0 0 18

*L-H-ST CHF-HTR HY-DIA H-EQ-DIA CH-LENGTH HT-STR-N0.

13003801 0 0.0 0.0 0.111500 18

*R-H-ST CHF-HTR HY-DIA H-EQ-DIA CIT-LENGTH HI-SIR-NO

13003901 0 0.0 0.0 0.111500 18

*HEAT SLAB... BROKEN LOOP, VESSEL NOZZLES (3 IN. SCH-160)*

* NOTE -HEAT SLAB CONTAINS ONLY VOLUME LENGTHS WHICH *

* ~ARE NOT HEATED*

*LEFT BOUNDARY BROKEN LOOP PRIMARY COOLANT VESSEL NOZZLES (301,363) *RIGHT BOUNDARY AMBIENT VOLUMES (801,803)

*GL DATA NH NP TYPE S-FLG L-COR

13004000 2 5 2 1 0.10933333

*M1ESH LOC FLG FRH FLG

13004100 0 1

*GEOMETRY NO ITV R-COR NO ITV R-COR

13004101 2 0.145833 2 0.312500

*MATERIALS CMP NO ITV NO CMP NO ITV NO

13004201 1 2 16 4

*SOURCE DIS SOURCE ITV NO

13004301 0.0 4

*INIT TEMP FLO

13004400 -1

*TEM!P DISTRIBUTION

13004401 610.1 606.8 604.3 352.4 152.5
13004402 546.9 544.154.318148 541.9 318.8 144.8

*L-BNDY

13004501

13004502

*R-BNDY

13004601

13004602

*SOURCE

13004701

*L-H-ST

13004801

BY-VOL

301010000

363020000

NY-VOL

801010000

803010000

INC

0

0

B-CDT A-CODE CY-LENGTH

1 1 0.61160

1 1 0.91239

HT-STR-NO

1

2

HT-STR-NO

1

2

INC B-CDT

0 4100

0 4100

A-CODE CY-ILEN GTH

0. 61160

0. 91239

TYPE IS-MLPR

.0 0

CHF-HTR HY-DIA

0 0.0

L-DR-HT

0

R-DR -HT NT-SIR-NO

0 2

H-EQ-DIA CH-LENGTH HI-SIR-NO

0.0 0.218666 2

*R-H-ST CHF-HTR HY-DIA H-EQ-DIA CH-LENGTH HT-STR-NO

13004901 0 0.0 0.0 0.218666 2

*HEAT SLAB... INTACT LOOP PUMP* * NOTE - HEAT SLAB MODELS HEAT LOSS DUE TO PUMP SEAL COOLING *

*LEFT BOUNDARY =COMPONENT. 250

**RGTBOUNDARY = SPECIFIED 1N'TABLE 251"

*PUMP HEAT LOSS IS TABULATED AS A LINEAR FUNCTION OF PUMP ANGULAR SPEED

*GL DATA

12500000

NH

1

NP

4

TYPE

2

S-FLG L-COR

1 0.08865

*MESHI LOG FLU

12500100 0

FRN FLU

1

*GEOM1ETRY NO ITV R-COR

12500101 3 0.1500

*MATERIALS

12500201

*SOURCE DIS

12500301

*INIT TEMP

12500400

CMP NO

1

SOURCE

0.0

ITV NO

3

ITV NO

3

FLU

0

* TEMP MESH

12500401 540.7. 1

*L-BNDY NY-VOL

12500501 250010000

TEMP MESH

436.6 2

TEMP MESH

345.9 3

TEMP MESH

265.0 4

INC

0

B-CDT A-ýC0DE- CY-LENGTH HT-SIR-NO

1 1 '2.26167 1

*R-BNDY

12500601

*SOURCE

12500701

*L-H-ST

HY-VOL

0

INC B-CDT A-CODE CY-LENGIH HT-STR-NO

0 (22)51 .1 2.26167 1

TYPE

0

IS-MPLR

0

L-DR-NT

0

R-DR-HT HT-SIR-NO

0 1

CHF-HTR HY-DIA CHFHT -EQ-DIA N-DA CH-LENGTH NT-SIR-NO
12500801

*R-H-ST

125009U1

0 0.0 0.0 2.2Z6167 1

CHF-HTR HY-DIA

0 0.0

H-EQ-DIA

0.0

CH-LENGTH HT-STR-NO

2.26167 1

*HEAT SLAB... BROKEN LOOP PUMP*

* NOTE - HEAT SLAB MODELS HEAT LOSS DUE TO PUMP SEAL COOLING *

* LEFT BOUNDARY = COMPONENT 350

*RIGHT BOUNDARY = SPECIFIED IN TABLE 351

*PUMP HEAT LOSS 1• TABULATED AS A LINEAR FUNCTION OF PUMP ANGULAR SPEED

*GL DATA

13500000

*MESH

13500100

* GEOMETRY

13500101

* MATERIALS

13500201

*SOURCE DIS

13500301

*INIT TEMP

13500400

NH

1

LOG FLG

0

NP

4

TYPE S-FLG L-COR

2 1 0.07014

FRM FLG

1

NO ITV R-COR

3 0.12325

CMP NO ITV NO

1 3

SOURCE ITV NO

0.0 3

FLG

0

* TEMP MESH

13500401 531.1 1

*L-BNDY HY-VOL

13500501 350010000

TEMP MESH

434.0 2

TEMP MESH

350.8 3

TEMP MESH

277.4 4

CY-LENGTH

1. 9635

INC

0

B-CDT

1

A-CODE

I

HT-STR-NO

1

*R-BNDY

13500601

*SOURCE

13500701

HY-VOL

0

INC B-CDT A-CODE CY-LENGTH HT-STR-NO

0 2351 1 1.9635 1

TYPE IS-MPLR

0 0

L-DR-HT

0

R-DR-HT HT-STR-NO

0 1

*L-H-ST CHF-HTR HY-DIA

'13500801 0 0.0

*R-H-ST CHF-HTR HY-DIA

13500901 0 0.0

H-EQ-DIA CH-LENGTH HT-STR-NO

0.0 1.9635 1

H-EQ-DIA

0.0

CH-LENGTH

1. 9635

HT-STR-NO

1

*HEAT SLAB... PRESSURIZER HEAT TRANSFER TO PRESSURIZER WALLS

* ~WITHOUT LINER - ALUMINUM SHEATH HEATED BY HEATER TAPE *

*LEFT BOUNDARY =COMPONENT 999

*RIGHT BOUNDARY = AMBIENT VOLUME (816)

*GL DATA

19990000

NH1

8

NP TYPE

114 2

S-FLG L-COR

1 .151291 7
*MESH

19990100

* GEOMETRY

19990101

19990102

*MATERIALS

19990201

19990202

*SOURCE DIS

19990301

*INIT TEMP

19990400

LOC FLO ERM FLG

0 1

NO ITV

3

1

CMP NO

1

13

SOURCE

0.0

R-COR

.187500

.272267

ITV NO

3

9

ITV NO

9

NO ITV R-COR

4 .270833

2 .282683

NO ITV R-COR

1 .272167

2 .449350

CMP NO

19

9

SOURCE

1.0

ITV NO

7

11

ITV NO

11

ClIP NO

20

30

SOURCE

0.0

ITV NO

8

13

ITV NO

13

FLG

0

* TEMP MESH

19990401 602.0 2

*L-BNDY

19990501

19990502

19990503

19990504

*R-BNDY

19990601

19990602

19990603

19990604

*SOURCE

19990701

19990702

19990703

19990704

*L-H-ST

19990801

19990802

19990803

19990804

*R-H-ST

19990901

19990902

19990903

19990904

HY-VOL

999010000

999020000

999070000

999080000

HY-VOL

816010000

816010000

816010000

816010000

TYPE

117

117

117

117

CHF-HTR

0

0

0

0

CHF-HTR

0

0

0

0

TEMP MESH

602.0 12

INC

0

10000

0

0

INC

0

0

0

0

IS-MPILR

.125065

.128192

.129234

.104742

HY-DIA

.2858333

.3025833

.3025833

.1005325

iIY-DIA

0.0

0.0

0.0

0.0

B-CDT

1

410

4100

4100

4100

A-CODE

1-OD

1

1

CY-LENGTH

2.500000

2. 562500

2.583333

2. 093750

CY-LENGTH

2. 500000

2.562500

2.583333

2. 093750

L-DR-HT

0

0

0

0

H-EQ-DIA

.2914500

.3025833

.3025833

.2251253

H-EQ-DIA

0.0

0.0

0.0

0.0

TEMP MESH

140.0 14

R-DR-HT

0

0

0

0

CA-LENGTH

2.500000

2.562500

2. 583333

2.093750

CA-LENGTH

2. 500000

2.562500

2. 583333

2. 093750

HT-STR-NO

1

6

7

8

HT-STR-NO

6

7

8

HT-STR-NO

6

7

8

HT-STR-NO

1

6

7

8

HT-STR-NO

1

6

7

8

*HEAT SLAB... PRESSURIZER HEATER RODS------ DATA FROM RAMA CORP., *

* ~HEATER ROD MANUFACTURER*

*LEFT BOUNDARY = ADIABATIC *RIGHT BOUNDARY = COMPONENT 999

*GL DATA NH

I

NP

9

TYPE S-FLG L-COR
*MESH

19992100

*GEOMETRY

19992101

19992102

*MATERIALS

19992201

19992202

*SOURCE DIS

19992301

*INIT TEMP

19992400

LOG FLG

0

FEM FLG

1

NO ITV R-COR

2 2.1539E-2

2 3.1042E-2

NO ITV

1

CHP NO

22

R-COR

2.1833E-2

ITV NO

3

NO ITV R-COR

2 2.695SE-2

CHP NO

21

23

SOURCE

0.0

ITV NO

2

7

ITV NO

2

CHP NO

21

ITV NO

5

ITV NO

7

SOURCE ITV NO SOURCE

1.0 3 0.0

FL2G

0

* TEMP MESH

19992401 631.0 8

*L-BNDY

19992501

*R-BNDY

1999260.1

*SOURCE

19992701

*1,-H-ST

19992801

HY-VOL

0

flY-VOL

999080000

INC

0

B-CDT A-CODE CY-LENGTH

0 0 0.0

HI-STR-NO

1

INC B-CDT A -CODE CY-LENGTH Hi-SIR-NO

0 1 1 . 12.0 1

TYPE IS-MPLR

10999 1.0

CHF-HTR HY-DIA

0 0.0

L-DR-fIT

0

R-DR-HT HT-STR-NO

0 1

H-EQ-DIA CH-LENGTH HI-SIR-NO

0.0 2.093750 1

H-EQ-DIA CH-LENGTH HI-SiR-NO

.1901660 2.093750 1

*R-H-ST CHF-HTR HY-DIA

19992901 0 .1005325

*HEAT SLAB... PRESSURIZER HEAT TRANSFER OUT END CAPS AND INSTRUMENT *

* ~PORTS - THERMAL CONDUCTIVITY CALCULATED TO MATCH TEST *

*LEFT BOUNDARY = COMPONENT 999

*RIGHT BOUNDARY = AMBIENT VOLUME (806)

*GL DATA

19993000

*M1ESH

19993100

*GEOME-TR.Y

19993101

*MATERIALS

19993201

*SOURCE DIS

19993301

T

*INIT TEMP

19993400

NH

8

NP

3

TYPE

2

S-FLG L-COR

1 .1512917

LOG FLG FRI FLG

0 1

-NO ITV. R-1COR

2 .449350,

CMP NO

31

SOURCE

0.0

ITV NO

2

ITV NO

2

FLG

0
19993401

*L-BNDY

19993501

19993502

19993503

19993504

*R-BNDY

19993601

19993602

19993603

19993604

*SOURCE

19993701

*L-H-ST

19993801

19993802

19993803

19993804

*R-H-ST

19993901.

19993902

19993903

19993904

TEMP NESH

602.0 1

flY-VOL

999010000

999020000

999070000

999080000

HY-V0[L

806010000

806010000

806010060

806010000

TEMP MESH

370.0 2

INC

0

10000

0

0

INC

0

0

0

0

TEMP MESH

140.0 3

B-CDT

410

4100

4100

4100

A-CODE

1

1

1

1

A-CODE

1

1

1

1

CY-LENGTH

2. 500000

2. 562500

2. 583333

2.093750

CY-LENGTH

2. 500000

2. 562500

2. 583333

2.093750

HT-STR-NO

1

6

7

8

HT-STR-NO

1

.6

7

8

TYPE IS-KPLR

0 0

CHF-HTR

0

0

0

0

CHF-.HTR

0

0

0

0

HY-DIA

.2858333

.3025833

.3025833

.1005325

L-DR-HT

0

H-EQ-VIA

.2914500

.3025833

.3025833

.2251253

H-EQ-DIA

0'0

0.0

0.0

0.0

R-DR-HT HT-STR-NO

0 8

CU-LENGTH HT-STR-NO

2.500000 1

2.562500 6

2.583333 7

2.093750 8

HY-DIA

-070

0.0

0.0

0.0

CU-LENGTH

2.500000

2562500

2. 583333

2.093750

HT-STR-NO

1

6

7

8

B EAT SLAB... PRESSURIZER SURGE LINE HEAT LOSS*

*LEFT BOUNDARY = COMPONENT 997

*RIGHT BOUNDARY = AMBIENT VOLUME (807)

*GL DATA

19970000

*MESH

19970100

*GEOMETRY

19970101

*MATERIALS

19970201

NH

2

NP

5

TYPE S-FLG L-COR

2 1 .0154167

LOC FLG

0

ERN FLG

1

NO ITV R-COR NO ITV R-COR

2 .035000 2 .054460

CMP NO ITV NO

1 2

CMP NO

24

ITV NO

4

*SOURCE DIS SOUJRCE ITV NO

*INIT TEMP

19970400

FLG

0

* TEMP MESH

19970401 602.0 2

*L-BNDY HY-VOL

19970501 997020000

TEMP MESH

602.0 5

INC

0

B-CDT A-CODE CY-LENGTH

1 1 5.6458333

HT-STR-NO

1
19970502 997030000 0 1 I1 4.0625000

*R-BNDY

19970601

19970602

*SOURCE

19970701

HY-VOL

807010000

807010000

INC B -CDT

0 4100

0 4100

A--C0DE CY-LENGTH

5. 6458333

4. 0625000

R-DR-HT

0

2

ILT-STR-NO

1

2

HT-STR-NO

2

TYPE IS-MPLR

0 0

4L-H-ST CHF-HTR HY-DIA

19970801 0 0.0

L-DR-HT

0

H-EQ-DIA

0.0

H-EQ-DIA

0.0

CH-LENGTH HT-STR-NO

0.0 2

*R-H-ST

19970901

*CHF-IITR

0

HY-DIA

0.0

CH-LENGTH

0.0

HT-STR-NO

2

********* HEAT STRUCTURE THERMAL PROPERTY DATA ***~****

* TYPE

*316L STAINLESS STEEL

20100100 TBL/FCTN

*AVERApJGE TWO.PHASE DATA

20100200 'TBL/F.CTN

*BORON NITRIDE

20100300 TBL/FCTN

*CONSTANTAN

20100400 TBL/FCTLN

*INCONEL 600

20100500 TBL/FCTN

CN FLG CA FLG

1 1

1 I

1

1

1

1

1

1

*GRAFOIL (GRAFOIL IS A TRADE NAME OF A UNION

20100600 TBL/FCTN I

CARBIDE PRODUCT)

*COPPER CA 102 (OXYEN FREEN COPPER)

20100700 TBL/FCTN 1

*CAL-TEMP INSULATION (MODIFIED VALUES

20100800 TBL/FCTN 1

1

*ALUMJNIA *(ALUMINUN OXIDE)

20100900 TBL/FCTN

*INCONEL 718

-2OltOlOOO__._.TI1LLCTN._

1

1

FOR VI,SSEL HEAT LOSS)

*HONEYCOMIB - HEXAGONAL MATRIX CORE

20101100 TBL/FCTN 11

*HONEYCOMlB - SQUARE MATRIX CORE

20101200 TBL/FCTN 1I

*CONTACT RESISTANCE PROPERTIES (CONDUCTIVITY

20101300 TBL/FCTN 1I

OF AIR; STORAGE = 0.0)
*STEAM GI

20101400

* WATER

20101500

*CAL-TEMf

20101600

*CAL-TEMl

20101700

*THERMAIA,

20101800

*CAL-TEKP

20101900

*ALUMflNUý

20102000

*M]AGNESIUj

20102100

*NICHROME

20102200

*INCOLOY

20102300

*CAL-TEMjP

20102400

*0.35%

20102500

*CAL-TEMP

20102600

~NERAT0R FILLER PIECE CONSTRUCTION

TBL/FCTN 1 1

TBL/FCTN 1 1

INSULATION (MODIFIED VALUES FOR PIPING HEAT LOSS)

TBL/FCTN 1 1

INSULATION (MODIFIED VALUES FOR STEAM GENERATOR HEAT Li

TBL/FCTN 1 I

LINER - JOHN'S MANVILILE MIN-K 2000, 30-35 PCF

TBL/FCTN 1 1

INSULATION (MODIFIED VALUES FOR PRESSURIZER HEAT LOSS)

TBL/FCTN 1 1

I(USED IN PRESSURIZER GUARD HEATERS)

TBL/FCTN 1 1

MN OXIDE (USED IN PRESSURIZER HEATER RODS)

TBL/FCTN 1 1

V (USED IN PRESSURIZER HEATER RODS)

TBL,/FCTN 1 1

800 (USED IN PRESSUIZER HEATER RODS)

TBL/FCTN 1 1

INSULATION (FOR PRESSURIZER SURGE LINE HEAT LOSS)

TBL/FCTN 1 1

CARBON STEEL USED FOR SG TUBE SHEETS

TBL/FCTN 1 1

INSULATION (FOR INLET PLENUM HEAT LOSS)

TBL/FCTN I 1

DSS)

*UOZ USED

20102700

*ZIRCALOY

20102800

IN NUCLEAR CORE

TBL/FCTN 1

USED IN NUCLEAR CORE

TBL/FCTN 1

1

1

*GAP USED IN NUCLEAR CORE

20102900 TBL/FCTN 1 1

*TEMP-MIAT INSULATION (MODIFIED VALUES FOR PRESSURIZER HEAT LOSS)

20103000 TBL/FCTN 11

*PRESSURIZER END CAP AND INSTRUMtNT HEAT LOSS*:- CAECULATE- -VALIIES20103100 TBL/FCTN 1 1

*CAL-TEMP INSULATION (MODIFIED VALUES FOR BL STEAM GENERATOR HEAT LOSS)

20103200 TBL/FCTN 1 1

...................................................................................

*THERMAL CONDUCTIVITY BTU/(S FT F)
* TEMP

*316L STAINLESS STEEL

20100101 32.0

20100102 100.00

20100103 4000.00

*AVERGE TWO PHASE DATA

COND - TEMP COND TEMP COND

.00215

.00215

.00397

800.00 .00306 1600.00 .00397

20100201

20100202

32.00 .000006

212.00 .000006 572.00 .000008 4000.00 .000008

* BORON NITRIDE (NEW

20100301 32.00

20100302 200.00

20100303 1500.00

20100304 3000.00

*CONSTANTAN

20100401 0.00

*INCONEL 600

20100501 32.00

20100502 100.00

20100503 700.00

20100504 4000.00

CURVE FROM

.00255

.00241

.00133

.000074

C.FINEMAN. .IN 1/30/79 BY DMK)

500.00

2000.00

3500.00

.00216

.000909

.000074

1000.00

2500.00

4000.00

.00174

.000491

.000074

.00389 3000.00 .00389 4000.00 .00389

.00236

.00236

.00322

.00378

300.00 .00267 500.00 .00294

900.00 .00350 1100.00 .00378

*GpfAFOIL

20100601

20100602

20100603

20100604

32.00

250.00

1000.00

2000.00

..000799

.000799

.000509

.000463

500.00

1250.00

3000.00

.000683

.000484

.000486

750.00

1500.00

4000.00

.000579

.000468

.000486

*COPPER CA 102

20100701 32.00 .0622 212.00 .0606

20100702 932.00 .0575 4000.00 .0575

572.00 .0589

*CAL-TEMP

20100801

20100802

20100803

INSUL (INCREASED BY FACTOR OF 35.0 FOR VESSEL HEAT

0.00 3.2410E-4 100.00 3.2410E-4 200.00

300.00 3.8500E-4 400.00 4.0540E-4 500.00

600.00 4.8610E-4 700.00 5.3290E-4 800.00

LOSS)

3.4420E-4

4.4530E-4

5. 8720E-4

*ALUMINA (ALUMIINUM OXIDE)

20100901 0.00 .00034722 3300.00 .00034722

*INCONEL 718

20101001

20101002

20101003

0.00

600.00

1200.00

.0021667

.0025556

.0033333

200.00

800.00

1400.00

.0022778

.0028056

.0035556

400.00

1000.00

1600.00

.0023333

.0030556

.0038333

*HONEYCOM'B - HEXAGONAL MATRIX COP]

20101101 0.00 Z.61110E-5

*HONEYCOMB

20101201

700.00 Z-611I0E-5

700.00 2.27780E-5 -SQUARE MATRIX COR

0.00 2.27780E-5

*CONTJACT

20101301

20101302

20101303

20101304

RESISTANCE (HEATERS TO

0.00 3.5750E-6

260.00 5.4000E-6

530.00 6.9970E-6

800.00 8.3940E-6

PIPING)

80.00

350 .00

620.00

890.00

(CONDUCTIVITIES OF AIR)

4.2110E-6 170.00 4.8190E-6

5.9500E-6 440.00 6.4810E-6

7.4780E-6 710.00 7.9500E-6

8.84Z0E-6 980.00 9.2750E-6

*STEAM GENERATOR FILLER PIECES (CONDUCTIVITIES FROM TEST GRB-14-82)
20101401 80.00 3.0280E-4 260.00 3.3610E-4 4-40.00 3.6950E-4

20101402 620.00 4.0280E-4 800.00 4.3610E-4

* WATER

20101501 32. 88.61I0E-6 104.0 100.8330E-6 176.0 107.2220E-6

20101502 248.0 110.OOOOE-6 356.0 108.3370E-6 464.0 101.9440E-6

20101503 500.0 98.0550E-6 572.0 86.6660E-6 700.0 86.6660E-6

*CAL-TEMP INSUL (INCREASED BY FACTOR OF 7.0 FOR PIPING HEAT LOSS)

20101601 0.00 6.4810E-5 100.00 6.4810E-5 200.00 6.8830E-5

20101602 300.00 7.7000E-5 400.00 8.1080E-5 500.00 8.9050E-5

20101603 600.00 9.7220E-5 700.00 10.6580E-5 800.00 11.7440E-5

*CAL-TEM) INSUL (INCREASED BY FACTOR OF 2.6125 FOR ILSG HEAT LOSS)

20101701 0.00 2.4189E-5 100.00 2.4189E-5 200.00 2.5697E-5

20101702 300.00 2.8740E-5 400.00 3.0255E-5 500.00 3.3233E-5

20101703 600.00 3.6596E-5 700.00 3.9784E-5 800.00 4.3987E-5

*THEWIAL LINER - JOHN'S MANVILLE MIN-1( 2000. 30-35 PCF

20101801 300.00 1.1110E-5 600.00 1.2730E-5 1000.00 1.4810E-5

*CAL-TE['P INSUL (INCREASED BY FACTOR OF 1.0 FOR PRESSURIZER HEAT LOSS)

20101901 0.00 9.2600E-6 100.00 9.2600E-6 200.00 9.8330E-6

20101902 300.00 1.1000E-5 400.00 1.1580E-5 500.00 .1.2720E-5

20101903 600.00 1L*3890E-5 -700.00 1.5230E-5 800.00 1.6780E-5

20101904 1000.00 1.9880E-5

*ALUMINUM (USED IN PRESSURIZER GUARD HEATERS)

20102001 32.00 3.2434E-2 212.00 3.3076E-2 392.00 3.4521E-2

20102002 572.00 3.6609E-2 752.00 3.9980E-2 1000.00 4.2608E-2

;k*

*M1AGNESIUMI OXIDE (USED IN PRESSURIZER HEATER RODS)

20102101 100.00 4.6296E-4 1000.00 3.3796E-4

*NICHROHE V (USED IN PRESSURIZER HEATER RODS)

20102201 32.00 1.9749E-3 212.00 Z.Z158E-3 392.00 2.5048E-3

20102202 572.00 2.7456E-3 752.00 2.8902E-3 1112.00 3.6127E-3

*INCOLOY 800 (USED IN PRESSURIZER HEATER RODS)

20102301 70.00 1.8519E-3 1000.00 3.2176E-3 1500.00 4.0278E-3

*CAL-TENP INSUL (INCREASED BY FACTOR OF 1.0 PZR SURGE LINE HEAT LOSS)

20102401 0.00 9.2600E-6 100.00 9.2600E-6 200.00 9.8330E-6

20102402 300.00 1.1000E-5 400.00 1.1580E-5 500.00 1.272E-5

20102403 600.00 1.3890E-5 700.00 1.5230E-5 800.00 1.6780E-5

*0.35Z CARBON STEEL USED FOR SG TUBE SHEETS

20102501 32.00 .00944 68.00 .00917 212.00 .00889

20102502 392.00 .00817 572.00 .00750 752.00 .00694

20102503 1112.00 .00564 1472.00 .00478

*CAL-TENP INSUJ (INCREASED BY ACTS 0F10 IMLETPLENUJWHEAT-LOSS-)

20102601 0.00 9.2600E-6 100.00 9.2600E-6 200.00 9.8330E-6

20102602 300.00 1.1000E-5 400.00 1.1580E-5 500.00 1.2720E-5

20102603 600.00 1.3890E-5 700.00 1.5230E-5 800.00 1.6780E-5

20102604 1000.00 1.9880E-5

*U02 USED IN NUCLEAR CORE

20102701 32.00 .00152 200.00 .00120 400.00 .00100

20102702 600.00 .00090 800.00 .00074 1000.00 .00066

20102703 1200.00 .00059 1500.00 .00052 2000.00 .00044-
20102704 2500.00 .00039 3000 3000.00 .037 .00037 4000.00000 .08 .00038

*ZIRCAL0Y

20102801

20102802

20102803

20102804

*GAP USED

20102901

20102902

USED IN NUCLEAR CORE

32.00 .00197

1478.80 .00366

1579.80 .00381

1639.70 .00391

1099.50

1498.60

1599.60

1759.80

.00320

.00369

.00384

.00411

1199.80

1529.20O

1619.70

1999.20o

.00330

.00373

.00387

.00458

IN NUCLEAR

32.00

1502.30

CORE

2.2500E-5

5.7800E-5

602.30 3.8520E-5

2006.30 6.7420E-5

998.33 4.6500E-5

5408.33 1.2040E-5

*TEMP-M1AT INS (INCREASED BY A FACTOR OF 1.0 FOR PRESSURIZER HEAT LOSS)

20103001 0.00 4.9770E-6 100.00 5.7870E-6 200.00 6.5970E-6

20103002 300.00 7.6390E-6 400.00 8.7960E-6 500.00 1.0420E-5

20103003 600.00 1.2040E-5 700.00 1.4120E-5 800.00 1.6320E-5

20103004 1000.00 1.6960E-5

*PRESSURIZER END CAP AND INSTRUMENT HEAT LOSS - CALCULATED VALUES

20103101 0.00 1.8334E-6 1000.00 1.8334E-6

*CAL-TEMP

20103201

20103202

20103203

20103204

]!NSUL (INCREASED BY FACTOR OF 2.2040 FOR BLSG HEAT

0.00 2.0340E-5 100.00 2.0340E-5 200.00

300.00 2.4238E-5 400.00 2.5521E-5 500.00

600.00 3.0606E-5 700.00 3.3564E-5 800.00

1000.00 4.3794E-5

LOSS)

2. 1671E-5

2.8028E-5

3. 6975E-5

.. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

*VOLUMIETRIC HEAT CAPACITY DATA *TEMP CAP

*316L STAINLESS STEEL

20100151 32.00 61.30

20100152 800.00 67.10

(BTU/CUFT-F)

TEMP CAP TEMP CAP

400.00 61.30 600.00 64.60

1000.00 69.35 4000.00 69.35

*AVERAGE

20100251

20100252

TWO PHASE

32.00

4000.00

*BORON NITRIDE

20100351 32.0

20100352 1200.00

20100353 2400.00

*CONSTANTAN

20100451 32.00

20100452 932.00

20100453 2552.00

1.00

64.00

37.50

54.60

61.40

56.00

67.00

84.00

212.00

400.00

1600.00

3400.00

212.00

1472.00

3000.00

1.00 572.00 64.00

37.50

58.30

62.50

56.00

73.00

90.00

800.00

2000.00

4000.00

572.00

2192.00

4000.00

48.30

60.00

62.50

61.00

7.00

90.00

*INCONEL 600 ...- 20100551

*GRAFOIL

20100651

20100652

20100653

20100654

*COPPER CA 102

20100751

-3Z 00 5...2.5 4000.00-

32.0 11.90 80.40

260.40 17.15 350.40

530.40 22.40 620.40

800.40 26.32 4000.00

52.225

11.90

19.60

23.80

26.32

51. 336

170.40

440.40

710.40

14.70

21.35

25.20

32.00 51.336 4000.00
*CAL-TEM1P INSUL1ATI ON

20100851 0.00

*ALUMIINA (ALUMINUM

20100951 0.00

*INCONEL 718

2.898

OXIDE)

55.20

1000.00

3300.00

2.898

55.20

20101051 0.00 48.5797 200.00

20101052 600.00 61.5912 800.00

20101053 1200.00 .74.4227 1400.00

*HONEYCOMB - HEXAGONAL MATRIX CORE

20101151 0.00 2.28969 200.00

20101152 600.00 2.89224 800.00

20101153 1200.00- 3.49379 1400.00

*HONEYCOMB - SQUARE MATRIX CORE

20101251 0.00 2.15978 200.00

20101252 600.00 2.71815 800.00

20101253 1200.00 3.29651 1400.00

*CONTACT RESISTANCE (HEATERS TO PIPING)

20101351 0.00 0.00 3300.00

53. 7597

65. 1840

76.9890

2.53081

3. 06095

3 .61530

2. 38713

2. 88729

3.41018

400.00

1000.00

1600.00

400.00

1000.00

1600.00

400.00

1000.00

1600.00

56 .458

69. 290

82. 121

2. 6512

3.2537

3. 8563

2. 5008

3.0691

3.6375

0.00

*STEAMI GENERATOR FILLER PIECE

20101451 0.00 13.00

*WATER (SATURATED)

20101551 32.00 63.033

20101552 248.00 59.895

20101553 500.00 57.989

*CAL-TEMP INSULATION

20101651 0.00 2.898

*CAL-TEMP INSULATION

20101751 0.00 2.898

*THERMAL LINER - JOHN'S MANVILL]

20101851 400.00 7.475

20101852 1200.00 8.775

* CAL-TEMP INSULATI ON

20101951 0.00 2.898

*ALUMINUM (USED IN PRESSURIZER

20102051 32.00 36.177

*MAGNESIUM OXIDE (USED IN PRESl

20102151 10.00 43.07

(CALCULATION FROM TEST

1000.00 13.00

GRB-14-82)

104.00

356.00

.572.00

1000.00

61.966

58.553

-60.-999

176.00

464.00

700.00

60. 950

57.845

62.576

E

1000.00

MIN-If 2000,

800.00

1600.00

2.898

2.898

30-35 PCF

8.125

8.775

1000.00 2.898

GUARD HEATERS)

10000.00 36.177

URIZER HEATER RODS)

10000.00 43.07

.*NICHROME V (USED IN

20102251 10.00

*INCOLOY 800 (USED 1

20102351 10.00

*CAL-ThE1P INSULATION

20102451 0.00

*0.35Z. CARBON STEEL

P RESSU RIZE R H EATER -ROD S) -

55.07 10000.00 55.07

i PRESSURIZER HEATER RODS)

61.00 10000.09 61.00

2.898 1000.00 2.898
20102551

*CAIL-TEMP

20102651

*U02 USED

20102751

20102752

20102753

20102754

*ZIRCAL0Y

20102851

20102852

20102853

20102854

68.00 51.40 3000.00 51.40

INSULATI ON

0.00

IN NUCLEAR

32.00

600.00

1200.00

2500.00

2.898 1000.00 2.898

CORE

43. 255

49.072

51. 939

55.994

200.00

800.00

1500.00

3000.00

1099.50

1498.60

1599.60

1759.80

45. 394

50. 308

52. 721

60.096

33. 550

53.180

73.640

34.790

400.00

1000.00

2000.00

4000.00

1199.80

1529.20

1619.70

1999.20

47.459

51. 238

53.920

79.014

35. 190

59.330

77.790

34.790

USED IN NUCLEAR CORE

32.0 27.820

1478.80 35.190

1579.80 62.190

1639.70 79.780

*GAP USED IN NUCLEAR CORE

20102951 32.00 8.051E-5 5408.30 8.0514E-5

*TEMP-MAT INSULATION

20103051 0.00 2.125 1000.00 2.125

*PRESSURIZER END CAP AND.INSTRUMENT HEAT LOSS

20103151 0.00 0.000 1000.00 0.000

*CAL-TEMIP INSULATION

20103251 0.00 2.898 1000.00 2.898

* ~TABLES*

* ******************CORE POWER***********

20150

20215000

20215001

20215002

20215003

20215004

20215005

20215006

20215010

20215011

20215012

TABLE

POWER

TRIP

409

TIME COEF

1.0

POWER COEF

1.000

TIME

0.0

1.1957

5.9783

7. 1739

10 .7608

11.9565

21.5217

31.0870

51.4130

81. 3048

.100.4348

979.'2388

POWER

1.000

.98216

.29432

.22553

.11781

.10006

.05289

.04263

.03880

.03500

.03313

'.02080'

(ANS STANDARD DECAY CURVE)

* ********~** PRESSURIZER HEATER ROD POWER ******

20299900 POW4ER

TIME

TRIP TIME COEF *POWER COEý

439 1.0 1O.4200E-3 * MW

POWER
20299901 0.0

20299902 10000.0

0.000

0.000

* ~PUMP SPEED TABLES (NORMALIZED SPEED)*

20225000

20225001

20225002

20225003

20225004

20225005

20225006

20225007

20225008

20225009

20225010

20225011

20225012

20225013

20225014

20350

20235001

20235001

20235002

20235003

20235004

20235005

20235006

20235007

20235008

202350109

20235010

20235011

20235012

TABLE

REAC-T

TIME

-1.0

0.0

1:1956

8.3695

9. 5652

19.1304

29.8913

38. 2608

59. 7826

62. 1739

64. 5652

66.9565

68.1521

4000.0

REAC-T

-1.0

0.0

1.1956

8.3695

10.7608

20. 3260

40.6521

59. 7826

60.9782

64.5652

65.7608

69.3478

4000.0

TRIP

412 * INTACT LOOP PUNP

NORM PUMP SPEED

1.0

1.0

0.97220

0. 55521

0. 50440

0.32739

0.23488

0. 22025

0.21159

0.19573

0.18887

0. 04289

0.0

0.0

413 *BROKEN LOOP PUMP

1.0

1.0

0.98527

0.63678

0. 55975

0.42278

0.40220

0. 40315

0.32766

0. 25842

0. 16130

0.0

0.0

*

*

*

SYSTEM HEAT LOSS TABLES

*

*

*

*HEAT LOSS DUE TO INTACT LOOP PUMP PASSIVE COOLING, 20.0 J(W AT FULL FLOW

* 1.0 BTU = 1055.056 JOULES (INTERNATIONAL TABLE)

** TABLE

*20225100 HtRNRATE

TRIP TIME COEF RATE C(JEF

412 ' '1.0 8.8931 * BTU/S)FTZ

*20225101

*20225102

*20225103

*20225104

*20225105

*20225106

*20225107

TIME

-1.0

0.0

10.4

20.8

32.0

42.4

62.4

NORM H.T.RATE

1.000

1.000

0.505

0.325

0.227

0.181

0.150
*20225108 64.0 0.000

*20225109 4000.0 0.000

*HEAT LOSS DUE TO INTACT LOOP PUMP ACTIVE COOLING, 4.3 KW ALWAYS

* TABLE

20225100 HTRNRATE

TRIP TIME COEF RATE COEF

412 1.0 1.9120 * BTU/S-FT2

NORM H.T.RATE

1.000

1.000

20250

20225101

TIME

0.0

20000.0

*BEAT LOSS DUE TO tROKEN LOOP PUMP PASSIVE COOLING, 14.7 KW AT FULL FLOW

* FROM TEST S0-2B-38, H. S. CRAPO, HSC-2-84, 3 FEB 1984

* 1.0 BTU = 1055.056 JOULES (INTERNATIONAL TABLE)

** TABLE

*20235100 HTRNRATE

TRIP TIME COEF RATE COEF

413 1.0 9.1631 *ý BTU/S-FT2

*20350

*20235101

*20235102

*20235103

*20235105

*20235105

*20235107

*20235107

*20235108

TIRE

-1.0

0.0

9.6

13.6.

20.8

30.4

60.0

64.8

4000.0

NORM H.T.RATE

1.000

1.000

0.590

0.498

0.407

0.385

0.385

0.000

0.000

*HEAT LOSS DUE TO BROKEN LOOP PUMP ACTIVE COOLING,

* FROM TEST SO-2B-38, H. S. CRAPO, HSC-2-84, 3

4.3 KW` ALWAYS

FEB 1984

* TABLE

20235100 HTRNRATE

TRIP

413

TIME COEF RATE COEF

1.0 2.6804 * BTU/S-FT2

20350

20235101

TIME

0.0

20000.0

NORM H.T.RATE

1.000

1.000

*SPECIFIED HEAT TRANSFER COEFFICIENTS ON PIPING INSULATION SURFACE

* (VALUES CALCULATED FOR FREE CONVECTON IN AIR + RADIATION)

* TABLE

20210000 HTC-TEMP

20100

20210001

20210003

20210003

20210004

20210005

TEMP

100.0

150.0

200.0

300.0

500.0

750.0

H. T. COEF.

0.00136

0.00206

0.00247

0.00302

0.00374

0.00438

(BTU/S-FT2-F)

*SPECIFIED HEAT TRANSFER COEFFICIENTS ON ILSG INSULATION SURFACE

* (VALUES CALCULATED FOR FREE CONVECTON IN AIR + RADIATION)

* TABLE
20220000 HTC-TEMP 0 1.0 0.0 3.5426

20200

20220001

20220002

20220003

20220004

20220005

TEMP

100.0

150.0

200. 0

300.0

500.0

750 .0

H.T.COEF

0.00136

0.00206

0.00247

0.00302

0.00374

0. 00438

(BTU/S-FT2-F)

ON BLSG STEAM DOME INSULATION

CONVECTON IN AIR + RADIATION)

* SPECIFIED HEAT TRANSFER COEFFICIENTS

* SURFACE (VALUES CALCULATED FOR FREE

20230000

20230001

20230002

20230003

20230004

20230005

20230006

TABLE

HTC-TEMP

TEMP

100.0

150.0

200.0

300.0

500.0

750.0

0 1.0 0.0 3.35

H. T. COEF

0. 00136

0.00206

0.00247

0.00302

0.00374

0.00438

(BTU/S-FT2-F)

" SPECIFIED HEAT TRANSFER COEFFICIENTS ON I3LSG RISER INSULATION

" SURFACE (VALUES CALCULATED FOR FREE CONVECTON -IN-AIR + RADIATION)

* TABLE

20240000 HTC-TEMP 0 1.0 0.0 3.35

*TEMP H.T.COEF.. (BTU/S-.YT2-F)

20240001 100.0 0.00136

20240002 150.0 0.00206

20240003 200.0 0.00247

20240004 300.0 0.00302

20240005 500.0 0.00374

20240006 750.0 0.00438

" SPECIFIED HEAT TRANSFER COEFFICIENTS ON BLSG DOWNCOMER INSULATION * SURFACE (VALUES CALCULATED FOR FREE CONVECTON IN AIR + RADIATION)

* TABLE

20250000 HTC-TEMP 0 1.0 0.0 3.35

20250001

20250002

20250003

20250004

20250005

..20250006

TEMP

100.0

150.0

200.0

300.0

500.0

750.0

H. T . CIOEF

0.00136

0.00206

0.00247

0.00302

0.00374

0. 00438

(BTU/S-FTZ-F)

* . POWER TABLES FOR PI PING HEATERS .*

* ***** POWER TABLE FOR GUARD HEATER POWER BUS 110 ***

* ***** (POWER TO INTACT AND BROKEN LOOP HOT LEGS) **

TABLE TRIP TIME COEF POWER COEF

20211000 P0OWER .430 1.0 8.4380E-3 MW
*TIME POW4ER

20211001 0.0 1.00

20211002 10000.0 1.00

* ***** POWER TABLE FOR GUARD HEATER POWER BUS 111 **

* ******** (POWER TO BROKEN LOOP PUMP SUCTION) ****

*TABLE TRIP TIME COEF POWER COEF

20211100 POWER 431 1.0 4.0130E-3 M W

* TME POWER

20211101 0.0 1.00

20211102 10000.0 1.00

* ***** POWER TABLE FOR GUARD HEATER POWER BUS 112 **

* ***** (POWER TO INTACT AND BROKEN LOOP COLD LEGS) **

*TABLE TRIP TIME COEF POWER COEF

20211200 POWER 432 1.0 3.1220E-3 *M~W

-TIME POWER

20211201. - ý.0.0 1.00

20211202 10000.0 1.00

* ***** POWER TABLE FOR GUARD HEATER POW4ER BUS 113 **

* ******** (POWER TO INTACT LOOP PUMP SUCTION) ~ '**

*TABLE TRIP TIME COEF POWER COEF

20211300 POWER 433 1.0 8.2610E-3 M W

*TIME POWER

20211301 0.0 1.00

20211302 10000.0 1.00

* ***** POWER TABLE FOR GUARD HEATER POWER BUS 116 **

* (POWER TO EXTERNAL HEATERS ON VESSEL AND DOWNCOMER)*

*TABLE TRIP TIME CORE POWER COEF

20211600 POWER* 436 .1.0 19.8320E-3 *MW

*TIME POWER'

20211601 0.0 1.00

20211602 10000.0 1.00

* *** POW4ER TAb~dh FOR GUARD HEATER POWER B US 117 **

* ***** (POWER TO EXTERNAL HEATERS ON PRESSURIZER) **

*TABLE TRIP TIME COEF POWER COEF

20211700 POWER 43^7 1.0 1.5930E-3 *MW
*TIME POWER

20211701 -1.0 1.00

20211702 0.0 0.00

20211703 10000.0 0.00

* ~CONTROL VARIABLES*

I* VESSEL INTERFACE LEVEL (-13 -578) *

** 2 CORE INTERFACE LEVEL (105 -501) *

** 3 DOWNCOMER INTERFACE LEVEL (+29 -578) *

** 4 UPPER PLENUM INTERFACE LEVEL (+153 -13) *

** 5 UPPER HEAD INTERFACE LEVEL (4421 +160) *

** 6 PRESSURIZER INTERFACE LEVEL *

** 7 INTACT LOOP U1-TUIBE UP SIDE INTERFACE LEVEL *

** 8 INTACT LOOP U-TUBE DOW4N SIDE INTERFACE LEVEL *

** 9 INTACT LOOP PUMP SUCTION DOWN SIDE INTERFACE LEVEL *

**10 INTACT LOOP PUMP SUCTION UP SIDE INTERFACE LEVEL *

**11 BROKEN LOOP U-TUBE UP SIDE INTERFACE LEVEL *

**12 BROKEN LOOP U-TUBE DOWN SIDE INTERFACE LEVEL *

**13 BROKEN LOOP PUMP SUCTION DOWN SIDE INTERFACE LEVEL *

**14 BROKEN LOOP PUMP SUCTION UP SIDE INTERFACE LEVEL *

**15 INTACT LOOP STEAM-GENERATOR RISER INTERFACE LEVEL *

**16 INTACT.-LOOP STEAM-.GENERATOR DOWNCOMER INTERFACE LEVEL *

**17- BROKEN LOOP STEAM GENERATOR RISER INTERFACE LEVEL *

-8~.BROKEN LOOP STEAM -GENERATOR .IOWNCOMER INTERFACE LEVEL *

*19' 'INTACT LOOP STEAM GENERATOR SECONDARY RISER MASS *

**20 INTACT LOOP STEAM GENERATOR SECONDARY DOWNCOMER MASS *

**21 INTACT LOOP STEAM GENERATOR SECONDARY TOTAL MASS *

**22 BROKEN LOOP STEAM GENERATOR SECONDARY RISER MASS *

**23 BROKEN LOOP STEAM GENERATOR SECONDARY DOWNCOMER MASS *

**24 BROKEN LOOP STEAM GENERATOR SECONDARY TOTAL MASS *

Z* 5 TOTAL STEAM GENERATOR SECONDARY MASS *

**26 ENERGY REMOVED FROM PRIMARY TO SECONDARY BY INTACT LOOP SG *

**27 ENERGY REMOVED FROM PRIMARY TO SECONDARY BY BROKEN LOOP SG *

**28 ENERGY REMOVED FROM CORE HEATER RODS TO PRIMARY COOLANT *

**29 MAXIMUM CORE HEATER ROD TEMPERATURE *

**150-151 CONTROL SYSTEM FOR CORE HEATER ROD POWER *

**200-221 CONTROL SYSTEM TO REDISTRIBUTE POWER ON VESSEL HEATERS *

**250-251 CONTROL SYSTEM TO OBTAIN DESIRED INTACT LOOP MASS FLOW RATE 350-351 CONTROL SYSTEM TO OBTAIN DESIRED BROKEN LOOP MASS FLOW RATE** 

**400 FLUID MASS IN DOWNCOMER *

**401 FLUID MASS IN LOWER PLENUM *

**402 FLUID MASS IN CORE *

**403 FLUID MASS IN UPPER PLENUM *

**404 FLUID MASS IN UPPER HEAD *

**405, FLUID MASS IN BYPASS LINE, SUPPORT COLUMNS, GUIDE TUBES *

**406 FLUID MASS IN PRESSURIZER *

**407 FLUID MASS IN INTACT LOOP HOT LEG *

**408 FLUID MASS IN INTACT LOOP U-TUBES *

**409 FLUID MASS IN INTACT LOOP COLD LEG *

**410 FLUID MASS IN BROKEN LOOP HOT LEG *

**411 FLUID MASS IN BROKEN LOOP U-TUBES *

**412 FLUID MASS IN BROKEN LOOP COLD LEG *

**413 TOTAL PRIMARY COOLANT SYSTEM FLUID MASS *

**501 VESSEL DELTA P -13 TO -578 CM *

**502 VESSEL CORE DELTA P -105 TO -501 CM *

**503 VESSEL DOWNCOMER DELTA P 29 TO -578 CM *

**504 VESSEL UPPER PLENUM, DELTA P 135 TO -13 CM *

**505 VESSEL UPPER HEAD DELTA P 421 TO 160 CM *
**506 PRESSURIZER DELTA P 632 TO 30 CM *

**507 INTACT LOOP STEAM GENERATOR U-TUBE UPSIDE DELTA P 926 TO -57E *

**508 INTACT LOOP STEAM GENERATOR U-TUBE DNSIDE DELTA P 926 TO -5ThX* **509 INTACT LOOP PUMP SUCTION DOWNSIDE DELTA P -57X TO 114 *

**510 INTACT LOOP PUMP SUCTION UPSIDE DELTA P 114 TO 116 *

**511 BROKEN LOOP STEAM GENERATOR U-TUBE UPSIDE DELTA P 925 TO -57E *

**512 BROKEN LOOP STEAM GENERATOR U-TUBE DNSIDE DELTA P 925 TO -57X *

**513 BROKEN LOOP PUMP SUCTION DOWNSIDE DELTA P -5TX TO B65 *

**514 BROKEN LOOP PUMP SUCTION UPSIDE DELTA P B65 TO B73 *

**515 INTACT LOOP STEAM GENERATOR RISER DELTA P 1117 TO 89 CM *

**516 INTACT LOOP STEAM GENERATOR DOWNCOMER DELTA P 1117 TO 51 CM *

**517 BROKEN LOOP STEAM GENERATOR RISER DELTA P 1186 TO -7 CM *

**518 BROKEN LOOP, STEAM GENERATOR D0OWNCOMER DELTA P 1186 TO 18 CM *

**519 BROKEN LOOP STEAM GENERATOR DOWNCOMER DELTA P BETWEEN HORIZS *

**531 VESSEL COLLAPSED LEVEL -13 TO -578(RiEF) CM *

**532 VESSEL CORE COLLAPSED LEVEL -105 TO -501(REF) CM *

**533 VESSEL DOWNCOMER COLLAPSED LEVEL 29 TO -578(REF) CM *

**534 VESSEL UPPER PLENUM COLLAPSED LEVEL 135 TO -13(REF) CM *

**535 VESSEL UPPER READ COLLAPSED LEVEL 421 TO 160(REF) CM *

**536 PRESSURIZER COLLAPSED LEVEL 632 TO 30(REF) CM *

**537 ILSG U-TUBE UPSIDE COLLAPSED LEVEL 926 TO -57E(REF) CM *

**538 ILSG U-TUBE DOWNSIDE COLLAPSED LEVEL 926 TO -57X(REF) CM *

**539 INTACT LOOP PUMP SUCTION DOWNSIDE COLLAPSED LEVEL REF 116 CM *

* *540 INTACT LOOP PUMP SUCTION UPSIDE COLLAPSED LEVEL REF 116 CM *

**541 BLSG U-TUBE UPSIDE COLLAPSED LEVEL 925 TO -57E(REF) CM *

**542 BLSG U-TUBE DOW4NSIDE COLLAPSED LEVEL*925 TO -57X(REF)' CM *

**543 BROKEN LOOP PUMP* SUCTION DOWNSIDE COLLAPSED LEVEL-REF B65 -CMN.**.-

**544 BROKEN LOOP PUMP SUCTION UPSIDE COLLAPSED LEVEL REF B65 CM *

**545 INTACT LOOP STEAM GENERATOR RISER COLLAPSED LEVEL REF 89 CM *

**546 INTACT LOOP STEAM GENERATOR DOWNCOMER COLLAPSED LEVEL REF 51CM**

**547 BROKEN LOOP STEAM GENERATOR-RISER COLLAPSED LEVEL REF. -7CM *

**548 BROKEN LOOP STEAM GENERATOR DOWNCOMER COLLAPSED LEVEL REF 18CM**

**549 BROKEN LOOP STEAM GENERATOR DNCHR HOR COLLAPSED LEVEL REF 18CM**

**561 VESSEL COLLAPSED LEVEL -13 TO -578 REF COLD LEG *

**562 VESSEL CORE COLLAPSED LEVEL -105 TO -501 REF COLD LEG *

**563 VESSEL DOWNCOMER COLLAPSED LEVEL 29 TO -578 REF COLD LEG *

**564 VESSEL UPPER PLENUM COLLAPSED LEVEL 135 TO -13 REF COLD LEG *

**565 VESSEL UPPER HEAD COLLAPSED LEVEL 421 TO 160 REF COLD LEG *

**566 PRESSURIZER COLLAPSED LEVEL 632 TO 30 REF ZERO CM *

**567 ILSG U-TUBE UPSIDE COLLAPSED LEVEL 926 TO -57E REF TUBE SHEET *

**568 ILSG U-TUBE DOWNSIDE COLLAPSED LEVEL 926 TO -57X REF TUB SilT **569 INTACT LOOP PUMP SUCTION DOWNSIDE COLLAPSED LEVEL REF COLD LEG** **570 INTACT LOOP PUMP SUCTION UPSIDE COLLAPSED LEVEL REF COLD LEG *

**571 BLSG U-TUBE UPSIDE COLLAPSED LEVEL 925 TO -57E REF TUBE SHEET *

**572 BLSG U-TUBE DOWNSIDE COLLAPSED LEVEL 925 TO -5TX REF TUB Sf1 *

**573 BROKEN LOOP PUMP SUCTION DOWNSIDE COLLAPSED LEVEL REF COLD LEG** **574 BROKEN LOOP PUMP SUCTION UPSIDE COLLAPSED LEVEL REF COLD LEG *

**575 -INTACT LOOP STEAM GENERATOR RISER COLLAPSED LEVEL REF TUB SHT *

**576 INTACT LOOP STEAM GENERATOR DOWNCOMER COLLPSD LVL REF TUB SilT

**577 BROKEN LOOP STEAM GENERATOR RISER COLLAPSED LEVEL REF TUB SHT *

**578 BROKEN LOOP STEAM GENERATOR DOWNCOMER COLLPSD LVL REF TUB SHT *

**579 BROKEN.LOOP STEAM GENERATOR DNCMR HOR COLLPSD LVL REF TUB SHT *

**606-610 CONTROL SYSTEM TO OBTAIN DESIRED MASS IN INTACT LOOP SG *

**620 INTACT LOOP STEAM GENERATOR RECIRCULATION RATIO *

**625 INTACT LOOP STEAM GENERATOR CIRCULATION RATIO *

**630-637 CONTROL SYSTEM TO HOLD IL STEAM DOME PRESSURE WITiHIN BAND *

**706-710 CONTROL SYSTEM TO OBTAINl ESIRED MASS IN BROKEN LOOP SG *

**720 BROKEN LOOP STEAM GENERATOR RECIRCULATION RATIO *

**725 BROKEN LOOP STEAM GENERATOR CIRCULATION RATIO *

**730-737 CONTROL SYSTEM TO HOLD BI, STEAM DOME PRESSURE WITHIN BAND *

** 800 TOTAL HEAT LOSS MONITORING SYSTEM *
**980-985 CONTROL SYSTEM TO OBTAIN DESIRED PRESSURIZER LIQUID LEVEL *

**990-999 CONTROL SYSTEM FOR PRESSURIZER INTERNAL HEATER RODS *

** **

* CONTROL VARIABLES FOR COMPARISON TO EQUIVALENT SEMISCALE DATA

* *****************LIQUID LEVELS **********

20500100

20000

20500101

20500102

20500103

20500104

20500105

20500106

20500107

20500108

205001109

20500110

20500111ý

20500120

20000

20500200

20000

20500201

20500202

20500203

2050Z020

20500205

20500206

20500207

20500320

20000

20500300

20000

20500301

20500302

20500303

20500304

205003105

20500306

20500307

20500308

20500309

205003102

20500311

205003012

20500402

NAME TYPE 'COEF INIT VAL FLG

VSLLVL SUN 30.48 -13.000 1 * VESSEL LEVEL (CM)

* (-13 TO -578)

-19. 0860ý 0.073491

2.760833

1.000833

2.0

2.0

2.0

2.0

2.0

2.0

1.635833

0.721917

0.466667

VOIDE

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

VOIDE

VOIDF

VOIUF

VOIDF

VOIDF

VOIDF

163010000

162010000

161010000

150060000

150050000

150040000

150030000

150020000

150010000

140010000

130010000

120010000

CORELVL

-16.42833

SUM' '30.48 -105.092 1 * CORE LEVEL (CM)

* (.-105. TO -501.)

0.16667

2.00000

2. 00000

2.00000

2. 00000

2.00000

2. 00000

0.81375

'VOIDF

VOIDF

VOIDF

VOIDE

VO1DF

VOIDF

VOIDF

VOIDF

1400)0000

150010000

15002O0000

150030000

150040000

150050000

150060000

161010000

DNCRIVL SUM 30.48 30.480 1 * DOWNCOMER LVL (CM) * (+29 TO -578)

-19.08608 2.0

2.260833

1.:000833

2.0

2.0

2.0

2.0

2.0

1.465667

1.207667

0.962500

0.781917

0.466667

UPLMLVL SUM 30.48

-0.426509 2.550000

2.343176

UHLVL SUM 30.48

VOIDF

VOIDE

VOIDF

VOIDF

VOIDF

VOl DF

VOID F

VOIDF

VOIDF

VOIDF

VOID F

VOIDF

VOIDF

101010000

110010000

110020000

1)0030000

110040000

110050000

110060000

110070000

110080000

110090000

110100000

130010000

120010000

136.144 1 *

VOID 1641000

VOIFF 164010000

423.570 1 *

UP PLENUM LVL (CM)

(+135 TO -13)

UP. HEAD

N#21 TO

LVL (CM)

+160)

+5. 120 2.880833 VOIDF 194010000

3.453333 VOIflE 193010000
20500503

20500504

20000

20500600

20000

20500601

20500602

20500603

20500604

20500605

20500606

20500607

20500608

20500609

20500700

20000

20500701

20500702

20500703

20500704

2050070.5

20500800

20500901

20500802

20500803

20500804

20500805

20000

20500900

205010901

205010902

205010903

205010904

20501090

20501090

20501090

205011000

205012001

205012002

205012003

1.965833 VOIDF 192010000

0.476667 VOIDF 191010000

PZRLVL SUN 30.48 625.793 1 * PZR LEVEL (CH)

0.0 2.50

2. 5625

2. 5625

2. 5625

2. 5625

2. 5625

2. 583333

2.09375

0.541667

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

999010000

999020000

999030000

999040000

999050000

999060000

999070000

999080000

997010000

ILUTU SUM 30.48

-1.75

ILUTD

-1;.75 .

1.7500000

7.9525000

7.9108334

7.9108334

6. 5999883

*SUM 30'.48

1.7500000

6.5999883

7.9108334

7.9108334

7.9525000

925.830 1 *

VOIDF 21500000*

VOIDF 215010000 *

VOIDF 220010000 *

VOIDF 220020000 *

VOIDF 220030000 *

925.830 1 *

*VOIDF 225010000 *

VOIDE 220050000 *

VOIDE 220060000 *

VOIDF 220070000 *

VOIDF 220080000

IL U-TUBE UP

(CM) - FROM

-57 CM BELO1IW

TOP OF TUBE SHEET

TO TOP OF MODEL

U-TUBE

IL -TUBE DOWN

(CM) - FROM

-57 CM.BELOW.-

TOP OF TUBE SHEET

TO TOP OF MODEL

U-TUBE

ILPSD SUM 30.48 151.803 1 * IL P-S DOWNi (CM)

* (DPI-57X*14)

-9.229167 0.6354167

1.1836602

3.6662500

3.4475000

2.8958333

3.4733333

0.7266667

ILPSU SUM 30.48

-9.229167 0.7266667

3.4733333

4. 20833333

BLUTU SUM 30.48

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

230010000

240010000

240020000

240030000

240040000

240050000

240060000

-25.019 1 * IL P-S UP (CM)

* (DPI*14B*16)

VOIDF

VOIDF

VOIDF

240070000

240080000

240090000

-1.7508333 1. 7508333

7.7916667

7.5000000

7.5000000

7.5000000

923.290 1 *

VOIDF 315010000 *

VOIDF 320010000 *

VOIDF 320020000 *

VOIDF 320030000 *

VOIDE 320040000

BL U-TUBE UP

(CM) - FROM

-57 CM BELOW

TOP OF TUBE SHEET

TO TOP OF MODEL

U-TUBE

BL -TUBE DOWN

(CM) - FROM

-ý7 CM BELOW

TOP*0F TUBE SHEET

BTJUTD

-1. 7508333

SUf1 30.48I 9h3.293 . I *

1.7508333 VOIDF 325010000

7.5000000 VOIDF 320050000
20501203

20501204

20501205

20010

20501300

20010

20501301

20501302

20501303

20501304

20501305

20501306

20501307

20010

20501400

20010

20501401

20501402

20501403

20501500

20501501

20501502

20501503

20501504

20501505

20010

20501600

20501601

20501602

20501603

20501604

20501605

20501606

20010

20501700

20501701

20501702

20501703

20501704

20501705

20501706

20501800

7.5000000

7.5000000

7.7916667

VOIDF

VOIDE

VOIDF

320060000 * TO TOP OF MODEL

320070000 * U-TUBE

320080000

BLPSD SUM 30.48 142.944 1 B L P-S DOWN (CM)

*(DPB-57X*65A)

-9.179583 0.8020833

1.3076602

2.3393333

1.6437500

4.9431250

4. 2964583

0.6466667

VOIDF

VOIDF

VOIIIF

VOII)F

VOIDF

VOIDF

VOIDF

330010000

340010000

340020000

340030000

340040000

340050000

340060000

BLPSU SUM 30.48 -27.026 1 * BL P-S UP (CM)

* (DPB*65*73A)

-9.179583 0.6466667

5. 3495833

2.2966667

VOIDF

VOIDF

VOIDF

340070000

340080000

340090000

ILSGRSL

0.0

I1SGDCL

0.0

SUM 30.48 1130.780

7.9525000

7.9108334

7.9108334

7.476Z500

-5.1558333

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

600010(

600020(

600030(

600040(

600050(

1 * 1.12. S.l. LVL (CM)

* (TOP OF TUBE

)00 * SHEET TO TOP OF

)00 * CENT. SEPARATOR)

)00 * (0 TO +1130)

)00 * RISER. SIDE

)GO

SUM 30.48 1130.780 1

7.476Z500

7.9108334

7.9108334

7.9525000

5. 5516667

1. 5404167

VOIDF

VOIOF

VOID F

VOIDF

VOIDF

VOIDF

603010000

603020000

603030000

603040000

602010000

6.12010000

*

*

*

*

*

*

BLSGRSI, SUM 30.48 1120.150 1

0.0 1.0833333

6.7083333

7.5000000

7.5000000

7. 5000000

6.8229167

1.3333333

VOIDF

VOIDF

VOIDE

VOIDF

VOID F

VOJUF

VOIDF

716010000

700010000

700020000

700030000

700040000

700050000

701010000

*

*

*

*

*

*

I.L. S.G. LVL (CM)

(TOP OF TUBE

SHEET TO TOP*OF

CENT. SEPARATOR

(0 TO +1130)

DOWNCONER SIDE

B.L.S.G. LVL (CM)

(TOP OF TUBE

SHEET T0 TOP OF

GRAV. SEPARATOR)

(0.0 TO 1172)

RISER SIDE

B.L.S.G. LVL (CM)

(TOP OF TUBE

SHEET TO BOT OF

GRAV. SEPARATOR)

(0.0 TO 1131)

DOWNCOMER SIDE

BLSGDCL SlIM 30.48

.5416667 4.0000000

7.5000000

7.5000000

7.5000000.

7.2500000

2.8229167

Vc

Vc

VL

1120.140 1 *

IDF 1401000*

IIDF 714010000 *

111W 714020000 *

IIDF 714030000 *

VOIDF 711010000

IbSGMR SUM .028316846 0.0 1 * IL S.G. SECONDARY

* RISER MASS (KG)
20501901

20501902

20501903

20501904

20501905

20501906

20501907

20502000

20* Z0

20502001

20502002

20502003

20502004

20502005

205021006

20020

20502100

20020

20502101

-20502102

20502200

20020

20502201

20502202

20502203

205022104

20502205

20502306

20502320

20502208

20502209

205022105

20020

20502300

20020

20502301

20502302

20502303

20502304

205023005

20502306

20502307

0.0 1.0038417

0. 9402046

0.8926058

1.0017945

2.2709806

0.4508175

0.4Z49623

RHO

RHO

R11O

RHO

RHO

RHO

RHO

600010000

600020000

600030000

600040000

600050000

601010000

611010000

ILSGMD SUN .028316846 0.0 1 * IL S.G. SECONDARY

* DOWNCOMER MASS(KG)

0.0 3. 0085308

0.7816260

0.2211171

0.2316581

0. 2316581

0.3322701

RHO

RHO

RHO

RHO

RHO

RHO

602010000

612010000

603010000

603020000

603030000

603040000

IISGM SRI 1.0 0.0 1 * IL S.G. SECONDARY

* MASS (EG)-

19

20

0.0 1.00

1.00

CNTRTJVAR

CNITRbJVAR

BLSGNR SUM .028316846 0.0 I * BI, S.G. SECONDARY

* RISER MASS (KG)

0.0 0.0344994

0.2213819

0.2476839

0.2461911

0.2649840

0.3268035

0.5794734

0.1534235

0.1002201

0. 0680664

RHO

RHO

RHO

RHO

RHO

RHO

RHO

RHO

RHO

RHO

716010000

7009010000

700020000

700030000

700040000

700050000

701010000

703010000

704010000

705010000

BLSGMD SUM .028316846 0.0 1 * BL S.G. SECONDARY

* DOWNCOHER MASS(KG)

0.0 0.6232431

0. 0718342

0.0366917

0.0424740

0.0779018

0.0779018

0.0779018

0.0774216

0. 0972227

RHO

RHO

RHO

RHO

RHO

RHO

RHO

RHO

RHO

711010000

712010000

713010000

714010000

714020000

714030000

714040000

714050000

715010000

BLSGM SUN 1.0 0.0

0.0 1.00

1.00

CNTRL VAR

CNTRI1VAR

1 * BL S.G. SECONDA~RY

* LIQUID MASS (KG)

22

23

1 * TOTAL SE7CONDARY

* LIQUID MASS (KG)

2-1

24

T0TSGM1 SUM 1.0 0.0

0.0 1.00

1.00

CNTRL VAR

CNTRI1VAR
20502600

20* Z0

20502601

20502603

20502603

20502604

20502605

20502606

20502607

20502608

20020

20502700

20020

20502701

20502702

20502703

20502704

20502705

20502706

20502707

20502708.

20502800

*0020

20502801

20502802.

20502803

205028104

20502805

20502806

20502807

20502808

20502809

205028104

20502811

20502812

20502900

20502901

20502910

20502903

20502904

ILSGQ SUN -1.OE-3 0.0 1 * IL SG 0(KW)

0.0 1.00

1.00

1.00

1.00

1.00

1.00

.1.00

1.00

Q

Q

(1

Q

Q

Q

Q

U

220010000

220020000

220030000

220040000

220050000

220060000

220070000

220080000

BLSGQ

0.0

SUM -1.OE-3 0.0 1 BLSG Q(IN~)

1.00

1.00

1.00

1.00

1.00

1.00

1.00

1.00

Q

Q

Q

U

Q

Q

Q

Q

320010000

320020000

320030000

320040000

320050000

320060000

320070000

320080000

CORPOW SUM .23607E-3 0.0 1 *CORE POWER (K•W)

0.0 1.00

1.00

1 ;0

1.00

1.00

1.00

1.00

1.00

1.00

1.00

1.00

1.00

*HTRNR

IITRNR

:HTPRN

HTRNR

HTRNR

HTRNR

IITRNR

IITRNR

HTRNR

HTRNR

HTRNR

HTRNR

*150000101

150000201

.150000301

' 150000401

150000501

150000601

150000701

150000801

150000901

150001001

150001101

150001201

,.0 1 MNAX ROD TEMP4

150000118

150000Z18

150000318

150000418

150000518

150000618

150000718

150000818

150000918

150001018

150001118

150001218

IIAXROD STDFNCTN 1.0 0

MAX HTTEMP

HTTEM~P

H1TTEMP

IITTEMP

HTTEMP

HUEMP

HITEMP

HITEMP

HTTEMP

HmTmp

HTTEMP

HTTEMP

* ~CONTROL BLOCH( FOR PRIMARY COOLANT SYSTEM .MASS*

20540000 DNCRMAS SUM .028316846 0.0 1 * DOWNCOMER MA.SS

* G(G)

20540001 0.0 205001 0.2113940 .0 RHO 101010000
20540002

20540003

20540004

20540005

20540006

20540007

20540008

20540009

20540010

20540011

20400

20540100

20400

20540101

20540102

20540103

20400

20540200

20540201

20540202

20540203

20540204

20540205

20540206

205404030

20540301

20540302

20540303

20540304-

20540400

20540401

20540402

20540403

20540404

20540500

20540501

20540502

20540503

0.0700293

0. 0260607

0.0520780

0.0520780

0.0520780

0.0520780

0.0520780

0. 0381645

0.0451975

0.07335Z5

RHO

RHO

RHO

RHO

RHO

RHO

RHO

RHO

RHO

RHO

110010000

110020000

110030000

110040000

110050000

110060000

110070000

110080000

110090000

110100000

LPLMMAS SUM .0283 16~

0.0 0.2381304

0.2328024

0. 1229966

346 0.0 1

RHO 120010000

RHO 130010000

RHO 140010000

A46 0.0 1

* MASS (KG)

COREMAS SUM .0283 16~ * CORE MASS (KG)

0.0 0.0607520

0 .0607520

0. 0607520

0.0607520

0. 0607520

.0.0607520

RHO

RHO

RHO

RHO

RHO

RHO

150010000

150020000

150030000

150040000

150050000

150060000

UPL!INAS

0.0

UPHDMAS

SUM .028316846 0.0 I UPPER PLENUM

*MASS (KG)

0. 0579072

0.1260044

0. 1223341

0.1445850

RHO

RHO

RHO

RHO

161010000

162010000

163010000

164010000

SUM .028316846 0.0 1 * UPPER HEAD

* MASS (KG)

0.0 0.0236441

0.1028720

0.1854233

0.1777042

RHO

RHO

RHO

RHO

191010000

192010000

193010000

194010000

BYSCGT SUM .028316846 0.0 1 * BYPASS LINE,

* SUPPORT COLUMNS,

)00 * AND GUIDE TUBE

)00 * MASS (KG)

0.0 0.0025551

0.0032783

0.0142473

0.0087675

0.0111809

0.0052981

0.0298418

RHO

RHO

RHO

RHO

RHO

RHO

RHO

181010(

181020(

182010000

183010000

184010000

185010000

186010000

PZRIASS SUM -.028316846. 0.0 1 * PRESSURIZER

* MASS (KG)

0.0 0.0033454

0. 0042156

0 .0030333

0.1731566

0.1842654

0. 1842654

0. 1842654

0.1842654

0.1842654

RHO

RHO

RHO

RHO

RHO

RHO

RHO

RHO

RHO

997010000

997020000

997030000

999010000

999020000

999030000

999040000

999050000

999060000
20540610

20540611

20400

20540700

20400

20540701

20540702

20540703

20540704

20540705

20540706

20540707

20540708

20400

20540800

20400

20540801

20540802

20540803

20540804

20540805-

20540806

20540807

20540808

20400

20540900

20540901

20540902

20540903

20540904

205409105

20540906

20540907

20540908

20540909

20540910

20540911

205410912

205410913

205410914

205410915

205410916

20410

20541000

20410

20541001

205411002

205411003

205411004

205411005

20541100

0.1857634 RHO 999070000

0.1120170 RHO 999080000

IHOTMAS SUN .028316846 0.0

1 " INTACT LOOP

" HOT LEG

0.0 0.1047757 * MASS (KG)

0.0776879

0. 0675653

0. 0653702

0. 0574572

0.0538994

0. 0478680

0.0345748

RHO

RHO

RHO

RHO

RHO

RHO

RHO

RHO

201010000

20102O0000

202010000

203010000

203020000

203030000

210010000

215010000

ITUBMAS SUN .028316846 0.0

I " INTACT LOOP

" U-TUBE

0.0 0. 1571175 * MASS (RG)

0.1562943

0.1562943

0. 1322144

0.1322144

0.1562943

0.1562943

0.1571175

RHO

RHO

RHO

RHO

RHO

RHO

RHO

RHO

220010000

220020000

220030000

220040000

220050000

220060000

220070000

220080000

ICLDMAS .SUNM .028316846 0.0 1 * INTACT LOOP

LEG .*.COLD 

0.0 0.0345748

0.0478680

0. 0374799

0.0902957

0.0849081

0.0713212

0.0863894

0.0374835

0.0374835

0.0863894

0. 1036466

0.0558400

0.0779869

0.0779869

0.0779869

0.0854513

RHO

RHO

RHO

RHO

RHO

RHO

RHO

RHO

RHO

RHO

RHO

RHO

RHO

RHO

RHO

RHO

225010000

230010000

240010000

240020000

240030000

240040000

240050000

240060000

240070000

240080000

240090000

250010000

261010000

261020000

262010000

263010000

* MAJSS (KG)

BHOTMAS SUN .028316846

0.0 0.0584279 RHO

0.0215803 RHO

0.0215803 RHO

0.0266031 RHO

0.0230250 RHO

0.0192876 RHO

0.0495847. RHO

0.*0115250 

- RHO

BTUBMAS SUM .028316846

0.0 

1

301010000

301020000

301030000

.301040000

301050000

301060000

310010000

3150TO000

" BROKFEN LOOP

" HOT LEG

" MASS (1%)

0.0 1 

** BROKEN LOOP

U-TUBE

0.0 0.0471739 MASS (1(G)

0.0454080

0. 0454080

0.0456672

RHO

RHO

RHO

RHO

320010000

320020000

320030000

320040000

*
20541105

20541106

20541107

20541108

20410

20541200

20410

20541201

20541202

20541203

20541204

20541205

20541206

20541207

205412108

20541209

20541210

20541211

20541214

20541213

20541214

20541215

205412016

20410

20541300

20410

20541301

20541302

20541303

20541304

20541305

205413106

20541310

20541311

20541312

0. 0456672

0.0454080

0. 0454030

0.0471739

RHO

RHO

RHO

RHO

320050000

3" .060000

320070000

320080000

BCLDMAS SUM .028316846 0.0 1 * BROKEN LOOP

* COLD LEG

0.0 * MASS (KG)

PCSMASS

0;. O

0. 0115250

0.04950847

0.*0156764

0.0228420

0.0160501

0.0482662

0.0419519

0.0099184

0. 0099184

0 .0522349

0.0224253

0. 0303500

0.0192357

0. 0160367

0.0227915

0.0479251

SUM

1.00 O

1.00

1.00

1.00

1.00

1.00

1.00

1.00

1.00

1.00

1.00

1.00

1.00

RHO

RHO

RHO

RHO

RHO

Rilo

RHO

Rlio

RHO

RHO

RHO

RHO

RHO

RHO

RHO

RHO

325010000

330010000

340010000

340020000

340030000

340040000

340050000

340060000

340070000

340080000

340090000

350010000

-361010000

362010000

363010000

363020000

1.0 '0.0

CNTRLVAR

CNTRILVAR

CNTRL VAR

CNTRL VAR

CNTRL VAR

CNTRL VAR

CNTRL VAR

CNTRL VAR

CNTRL VAR

CNTRL VAR

CNTRIJVAR

CNTRL VAR

CNTRI.JVAR

1 * TOTAL PRIMARY

*,COOLANT-SYSTEM

400- :MASS-.(-KG)

401

402

403

404

405

406

407

408

409

410

411

412

* ~CNTRLVAR DELTA P (KPA)*

*NAME TYPE SCALE INITI VALJ FL

20550100 VESDP SUN 1.OE-3 100.0

20550101

20550102

2055.0200

20550201

20550202

20550300

20550301

20550302

0.0 1.0 P.

-1.0 P

120010000 0.3303

163010000 -3.3898

NAME TYPE SCALE INIT VAL EL

COREDP SUM 1.OE-3 100.0

G

1 * VESSEL LEVEL DP

* -13 TO -578 CM

RHO 120010000

RHO 163010000

G

1 * CORE LEVEL DP

* -105 TO -501 CM

RHO 140010000

RHO 161010000

0.0 1.0

-1.0

P

P

140010000 -1.9198

161010000 0.9447

NAME TYPE SCALE INIT VAL

DWNCMDP SUM 1.OE-3 100.0

FLG

RHO

RHO

0.0 1.0 P

-1.0 P

120010000 0.3303

101010000 2.8420

DWNCM LEVEL DP

29 TO -578 CM

120010000

101010000
20550400

20550401

20550402

20550500

20550501

20550502

20550600

20500

20550601

20550602.

20550700

20550701

20550702

205510800

-205510301

205510802

20551090

205510901

20551090

205512000

NAME TYPE

VESUPDP SUM

0.0 1.0 P

-1.0 P

NAME TYPE

VESUHDP SUN

0.0 '1.0 P -i.0 P

NAME TYPE

PRZDP SUM

0.0 1.0 P

-1.0 P

SCALE INIT VAL FLG

1.OE-3 100.0 1 * VESSEL~ UPPER

* PLENUM DP

* 135 TO -13 CM

163010000 3.3898 RHO 163010000

164010000 3.6964 RHO 164010000

SCALE INIT VAL FLG

1.OE-3 100.0 1 * VESSEL UPPER

191010000

194010000

SCALE INII

1.OE-3 I

* HEAD DP

* 421 TO 160 CM

0.3256 RHO 191010000

4.0503 RHO 194010000

VAL FLG

.00.0 1 * PRESSURIZER

* 632 TO 30 CM

1.8327 RHO 999080000

4.3145 RHO 999010000

999080000

999010000

NAME TYPE SCALE I

ISGUPDP SUN 1.OE-3

NIT VAL FLG

100.0 1 * JLSG UPSIDE

* 9263T0 757E CM

-0. *5900 -RHO 210010000

.9.8588 RHO -220040000

0.0 1.0 P

NAME TYPE

ISGDNDP sum

-1.0 P

NAME TYPE

IPSDNDP sum

* 210010000

220040000

.SCALE''INIT VAL FLG

1.OE-3 100.0 1 * ILSG DOWNSIDE

* 926 TO -57X CM

230010000 -0.5900 RHO 230010000

220050000 9.8588 RHO 220050000

SCALE INIT VAL FL(

1.OE-3 100.0

0.0 0.5

0.5

-1.0

NAME I

IPSUPDP

0.0. 0.5

0.5

NAME

BSGUPDP

P

P

P

[YPE

sum

P

P

P

240060000

240070000

230010000

0. 5115

0. 5115

0. 5900

3

1 * IL PUNP SUCTION

" DOWNSIDE

" -57X TO 114

RHO 240060000

RHO 240070000

RHO 230010000

I. * IL PUNP SUCTION

" UPSIDE

" 114 TO 116

RHO 240060000

RHO 240070000

RHO 240090000

SCALE INIT VAL FL(

1.OE-3 100.0

240060000

240070000

240090000

0.5115

0. 5115

4. 3006

.YPE SCALE INTVL FLO

SUM 1.OE-3 100.0 1 * BLSG UPSIDE

* 925 TO -57E

310010000 -0.8393 RHO 310010000

320040000 10.'0822 . RHO 320040000

0.0 1.0 P

-1.0 P

NAME

BSGDNDP

l* p SCALE INIT'VAL

SUM 1.OE-3 100.0

FLG

1 *

0.0 1.0 P

-1.0 P

330010000 -0.8393 RHO

320050000 10.0822 RHO

BLSG DOWNSIDE

925 TO -57X

330010000

320050000
*NAME TYPE SCALE INIT VAL FLG

20551300 BPSDNDP SUM 1.OE-3 100.0 1 *

20551301

20551302

20551303

0.0 0.5

0.5

-1.0

P

P

P

340060000

340070000

330010000

0.4829

0.4829

0. 8393

RHO

RHO

RHO

BL PUMP SUCTION

DOWNSIDE

-57X TO B65

340060000

340070000

330010000

*NAME TYPE

20551400 BPSUPDP SUP]

SCALE INIT VAL FL(

1.OE-3 100.0

3

1 * BL PUMP SUCTION

" UPSIDE

" B65 TO B73

RHO 340060000

RHO 340070000

RHO 340090000

20551401

20551402

20551403

0.0 .0.5

0.5

-1.0

P

P

P

*NAME TYPE

20551500 ILSGRDP SUM

20551501 0.0 1.0 P

20551502 -1.0 P

340060000

340070000

340090000

SCALE INI:

1.OE-3

600010000

602010000

SCALE INI]

1.OE-3

603040000

602010000--

SCALE INI]

1.OE-3

0 .4829

0.4829

0. 6504

I VAL FLG

20510

20551600

20551601,

NAME TYPE

ILSGDDP SUM

100.0 1 * ILSG RISER

* 1117 TO 89 CM

3.1356 RHO 600010000

7.8576 RHO 602010000

[ VAL FLG

100.0 1 * ILSG DOWNCOMER

* 1117 TO 51 CM

6.9282 RHO 603040000

7.8576. - RHO 602010000

1 VAL FLG

100.0 1 * BLSG RISER

* 1186 TO -7 CH

2.3040 RHO 716010000

0.5601 RHO 703010000

0.0 1.0 P

-1.0 P

*NAME TYPE

20551700 BLSGRDP SUM

20551701

20551702

0.0 1.0 P

-1.0 P

716010000

703010000

*NAME TYPE

20551800 BLSGDDP SUM

20551801 0.0 1.0 P

20551802 -1.0 P

SCALE INIT VAL

M.E-3 100.0

FLG

1 * BLSG DOWNCOMER

* 1186 TO 18 CM

715010000

703010000 0.5601 RHO 703010000

* NAME

20551900 BLSGDHDP

TYPE

sum

SCALE INILT VAL FLG

1.OE-3 100.0 1 * BLSG DWN HORIZ

* 1036 TO 18 CH

20551901

20551902

0.0 1.0 P

-1.0 P

715010000

713010000

* ~CNTRLVAR COLLAPSED LIQUID LEVEL CMH

20553100

NAME TYPE

VESCL DIV.

SCALE VALO FLG * VESSEL CLSPD

10204.082 100. 1 * LEVEL -13 TO

* -578 REF -578

20553101 RHOF 163010000 CNTRL VAR 501

*NAME TYPE SCALE VALO -FLG

20553200 CORECL DIV 10204.082 100. .1

*CORE CLSPD *LEVEL -105 TO

*-501 REF -501

20553201 RHOF 161010000 CNRVA CNTRLVAR 50502
20553300

20553301

20553400

20553401

20553500

20553501

20553600

.20553601

20553700

20553701

20553800

20553801

20553900

20553901

20554000

20540

205541001

20554100

20554200

NAME

DWNCHCL

RHOF

TYPE

DIV

101010000

NAME TYPE

VESUPCL DIV

RHOF 164010000

NAME TYPE

VESUHCL DIV

RHOF 194010000

NAME

PRZCb

RHOF

TYPE

DIV

999010000

NAME TYPE

ISGUPCL DIV

RHOF 220040000

SCALE

10204. 082

CNTRL VAR

SCALE

10204.082

CNTRL VAR

SCALE

10204.082

CNTRL VAR

SCALE

10204.082

CNTRL VAR

10204.082

CNTRL VAR

SCALE

10204.082

CNTRLVAE

SCALE

10204. 082

CNTRL VAf

SCALE

10204.082

CNTRL VAl

SCALE

10204.082

CNTRLVXi

VALO FLG

100. 1

503

VALO FIG

100. 1

504

VALO FLG

100. 1

505

VALO FLG

100. 1

506

VALO FI.G

100. 1

507

VALO FLG

100. 1

508

VALO FLG

100. 1

z 509

VALO FLG

100. 1

1 510

VATL0 FLG

100. 1

R 511

* DWNCM CLSPD

* LEVEL 29 TO

* -578 REF -578

* VES UP CLSPD

* LEVEL 135 TO

* -13 REF -13

* VES UH CLSPD

* LEVEL 421 TO

* 160 REF 160

* PRZ CLSPD

* LEVEL 632 TO

* 30 REF 30

1.ILSG .1JP..CLSPD

**LEVEL 926 TO- *-57E REF -57

*ILSG DN CLSPD *LEVEL 926 T0 *-57X REF -57

NAME

ISGDNCL

RHOF

TYPE

DIV

220050000

NAME TYPE

IPSDNCL DIV

RHOF 230010000

NAME TYPE

IPSUPCL DIV

RHOF 240090000

NAME TYPE

BSGUPCL DIV

RHOF 320040000

* ILPS DN CLSPD

" LEVEL -57X TO

" 114 REF 114

" ILPS UP CLSPD

" LEVEL 114 TO

" 116 REF 114

" BLSG UP CLSPD

" LEVEL 925 TO

* -57E REF -57

NAME

BSGDNCL

TYPE

DIV

SCALE VALO FLG .*BLSG DN CbSPD

10204.082 100. 1ý *'LEVEL 925 TO

* -57X REF -57

20554201 RHOF 320050000 CNTRL VAR 512
20554300

20554301

20554400

20554401

20554500

20554501

20554600

20554601

-20554700-

20554701

20554800

20554801

20554900

20554901

20556100

20556101

20556200

20556201

20556300

20556301

NAME TYPE

BPSDNCL DIV

RHOF 330010000

NAME TYPE

BPSUPCL DIV

RHOF 340090000

NAME TYPE

ILSGRCL DIV

RHOF 611010000

NAME TYPE

ILSGDCL DIV

RHOF 611010000

NAME TYPE*

BLSGRCL -DIV-- -'

RHOF 703010000

NAME TYPE

BLSGDCL DIV

RHOF 703010000

NAME TYPE

BLSGDHCL DIV

RHOF 703010000

SCALE

10204.082

CNTRLVAI

SCALE

10204. 082

CNTRLVAF

SCALE

10204.082

CNTRLVAP

SCALE

10204.08Z.

CNTRL VAR

SCALE

10204.082-

CNTRL VAR

SCALE

10204. 082

CNTRL VAR

SCALE

10204. 082

CNTRL VAR

VALO FLG

100. 1

513

VALO FLG

100. 1

514

VALO FLG

100. 1

515

VALO FLO

100. 1

516

VALO .FLG

-100.. ----1

517

VALO FLG

100. 1

518

VALO FLG

100. 1

519

" BLPS DN CLSPD

" LEVEL -57X TO

" B65 REF B65

" BLPS UP CLSPD

" LEVEL B65 TO

" B73 REF B65

" ILSG RIS CLSPD

" LEVEL 1117 TO

" 89 REF 89

" ILSG DWN CLSPD

" LEVEL 1117 TO

" 51 REF 51

" BLSG RIS CLSPD-

*.LEVjEL 1186 -TO

* -7 REF -7

*

*

*

BLSG DW4N CLSPD

LEVEL 1186 TO

18 REF 18

* BLSG DNHZ CLSPD

* LEVEL 1036 TO

* 18 REF 18

NAME TYPE

VESCLR SUM

-578.0 1.0

NAME

CORECLR

-501.0

NAME

DWNCMCLR

-578.0

TYPE

SUM

1.0

TYPE

SUM

1.0

SCALE

1.0

CNTRL VAR

SCALE

1.0

CNTRL VAR

SCALE

1.0

CNTRL VAR

VALO

-13.0

531

VALO

-105.0

532

VALO

+29.0

533.

FLG

1

FLG

1

* VESSEL CLSPD

* LEVEL -13 TO

* -578 REF ZERO

* CORE CLSPD

* LEVEL -105 TO

* -501. REF ZERO

* DWNCM CLSPD

* LEVEL 29 TO

* -578 REF ZERO

FLG

1
20556400

20556401

20556500

20556501

20556600

20556601

20556700

20556701

20556800

20556801

20556900

20556901

20557000

20570

205571001

20557100

20557101

20557200

20557201

NAME

VESUPCLR

-13 .0

NAME

VESURCLR

160.0

NAM

PRZCLR

30.0

NAME

ISGUPCLR

-57.0

TYPE

SUM

1.0

TYPE

SUM

1.0

TYPE

SUM

1.0

TYPE

SUM

1.0

.. NAME TYPE

- I SGDNCI7R-ý - SUN

-57.0 1.0

SCALE

1.0

CNTRL VAR

SCALE

1.0

CNTRL VAR

SCALE

1.0

CNTRL VAR

SCALE

1.0

CNTRL VAR

SCALE

1.0

CNTRL VAR

SCALE

1.0

CNTRL VAR

SCALE

1.0

CNTRL VAR

SCALE

.1.0

CNTRL VAR

SCALE

1.0

CNTRL VAR

SCALE

1.0

CNTRL VAR

VALO

+135 .0

534

VALO

+421.0

535

VALO

+63Z. 0

536

VAGO0

+926.0

537

VALO

+926.0

538

VALO.

203.6

539

FLG

FLG

FLG

1

FLG

. 1

FLG

1

VES UP CLSPD

LEVEL 135 TO

-13 REF ZERO

VES UH CLSPD

LEVEL 421 TO

160 REF ZERO

PRZ CLSPD

LEVEL 632 TO

30 REF ZERO

ILSG UP CLSPD

LEVEL 926 TO

-57E REF ZERO

ILSG DN-CLSPD

* LEVEL .926 T0.

-57X REF ZERO

ILPS DN CLSPD

LEVEL -57X TO

114 REF ZERO

ILPS UP CLSPD

LEVEL 114 TO

116 REF ZERO

BLSG UP CLSPD

LEVEL 925 TO

-57E REF ZERO

BLSG DN CLSPD

LEVEL 92 TO

-57X REF ZERO

BLPS DN CLSPD

LEVEL -57X TO

B65 REF ZERO

NAME

IPSDNCLR

-281.3

NAME

IPSUPCLR

-281.3

NAME

BSGUPCLJR

-57.0

NAME

BSGDNCLR

-57.0

NAME

BPSDNCLR

-279.8

TYPE

SUN

1.0

TYPE

SUM

1.0

TYPE

sum

1.0

TYPE

SUM

1.0

TYPE

SUM

1.0

VALO FLO

0.0 1 *

540

VALO

+925.0

541

VALO

+925.0

542

VALO

203.6

54z13

FLG

1

FLG

I

ALG

I

*

*

*

*

*

*

*

*

*
20570

20557400

20570

20557401

20557500

20557501

20557600

20557601

NAME TYPE

BPSUPCLR SUN

-279.8 1.0

NAME TYPE

ILSGRCLR SUN

89.2 1.0

NAMý TYPE

ILSGDCLR SUN

SCALE VALO FLG * BLPS UP CLSPD

1.0 0.0 1 * LEVEL B65 TO

* B73 REF ZERO

CNTRL VAR 544

SCALE VALO FLG

1.0 +1117.0 1

*

*

*

CNTRL VAR 545

SCALE VALO FLG

1.0 +1117.0 1

*

*

*

ILSG RIS CLSPD

LEVEL 1117 TO

89 REF ZERO

ILSG DWN CLSPD

LEVEL 1117 TO

51 REF ZERO

BLSG RIS CLSPD

LEVEL 1186 TO

-7 REF ZERO

50.5 1.0 CNTRLVAR 546

NAME TYPE

BLSGRCLR SUM

-7.0 1.0

NAME TYPE

BIJSGDCLR SUN

16.51 1.0

NAME TYPE

BLSGHCLR SUN

16.51 1.0

SCALE VALO

1.0 +1186.0

FLG

1

*

*

*

CNTRL VAR 547

SCALE VALO

1.0 +1186.0

CNTRL VAR 548

FLG

1

*

*

BLSG DWN CIJSPD

LEVEL-1186 TO

18 -REF ZERO

BLSG DNHZ CLSPD

LEVEL 1036 TO

18 REF ZERO

SCALE VALO FLG *

1.0 0.0 1 *

CNTRL VAR 549

* ~CONTROL BLOCK FOR CORE POWER*

20515000 DCYPOWER FUNCTION 2.0147538 0.0

20515001 TIME 0 150

20150

20515100

1 MNW

1

150 *WATTS 1.5 % ?

ACTPOWER

0.0

SUM

1.000

1.0 0.0

CNTRL VAR

* ~CONTROL BLOCK FOR PRESSURIZER HEATER RODS

20990

20599501

20599900

20599901

VARPOW4ER FUNCTION 1.0

TIME 0

0.0

999

0.0

CNTRL VAR

1 *NMW

PZRPOWER

0.0

SUM

1.0

1.0 1

995 * WATTS

*INTERNAL PZR HEATER CONTROLS (REF GWJ-9-82)*

*20599000 T698 TRIPUNIT 1.0 0.0 1
*20599001

*20990

*20599101

*20599201

*20599400

*20599201

*20599600

*20599601

*20599400

*20599701

698

0ONOF]"HIRS SUM 875.0

1 1.0

T495 TRIPUNIT 1.0

495

T497 TRIPUNIT 1.0

497

T699. TRIPUNIT 1.0

0.0

CNTRL VAR

0.0

0.0

0.0

699,

PROPPWR1

0.0

INTERNED

15. 6E6

1

990

1

993

CNTRLVAR 992

SUN

1.0

SUN

-1.0

250.0 0.0

CNTRL VAR

1.25E-3 0.0

P 999010000

1.0 0.0

CNTRLVAR 996

PROPPWR2 HULT

CNTRJJVAR 994

*20599800 PZRINTHTRS SUN 1.0 0.0 1

*20599801 0. 1.0 CNTRLVAR 995 1.0 CNTRLVAR 997 -1.0 CNTRLVAR 991

* CONTROL BLOCK FOR PRESSURIZER LEVEL

*OBTAIN

20980

20598000

205981001

20598100

20598200

20598201

20930

20598500

SPECIFIED AND MAINTAIN CONSTANT MASS

T429 TRIPUNIT 1.0 0.0

429

PZRERR SUN 0.01 0.0

175.0 -1.0 CNTRLVAR

PZRCORR NULT 1.0 0.0

CNTRL VAR 980 CNTRL VAR

PZRFW NUILT .0066805 0.0

RHO 999070000 CNTRL VAR

IN THE PRESSURIZER

1

6

0

981

0

982

* INPUT DESIRED

" LEVEL IN GM 90.10.6

* CORRECT LEVEL IN

" PZR UNTIL T529

* PRESSURIZER

* FEED FLOW RATE

* ~CONTROL BLOCK FOR PUMPS*

* ********** STEADY STATE *****

*INTACT LOOP PUMP SPEED --- INPUT DESIRED INTACT LOOP

20525000 ILMERR SUM 1.0 0.0 1

20525001 9.10000 -1.0 NFLOWJ 163010000-*

20525100 ILPSPD INTEGRAL 20.0 1873.37 1

20525101 CNTRL VAR 250

FLOW RATE (KG/S)*

90.9. 18

*BROKEN LOOP PUMP SPEED --- INPUT DESIRED BROKEN LOOP FLOW RATE (KG/S)*

20535000 BLNERR SUN 1.0 0.0 1
20535001 3.20000 -1.0 2053001 FLOWJ .2000 -.163020000 0 * 90.9.18

20535100 BLPSPD INTEGRAL 60.0 1492.32

20535101 CNTRL VAR 350

1

*

*

*

*

**********TRANSIENT ******

INTACT LOOP

*20525100 ILPMPSPD FUNCTION 1873.37

*20525101 TIME 0

0.0

250

1 * FROM CNTRLVAR 251

* IN STEADY-STATE *

*

*

BROKEN LOOP

*20535100 BLPMPSPD FUNCTION 1492.32

*20535101 TIME 0

0.0

350

1 * FROM CNTRLVAR 351

* IN STEADY STATE

* ~CONTROL BLOCK FOR STEAM GENERATORS*

*OBTAIN SPECIFIED AND MAINTAIN CONSTANT MASS IN THE STEAM GENERATORS

20560600

20560601

T419 TRIPUNIT 1.0 0.0 1

419 * 90.9.18

20560700 ILMERR -SUM

20560701 73.0 -1.0

20560800 ILNCORR MULT

.20560801 CNTRL VAR

20560900 ILSGLS SUM

20560901 0.0 1.0

*20560902 1.0

I-1.0 .... 0. 0-

CNTRL VAR

1.0 0.0

606 CNTRL VAR

1

21

* INPUT DESIRED ILSG

* LIQUID MASS IN KG *90.9.18*90.9.18

0 * CORRECT MASS IN

607 * ILSG UNTIL T519

0 * MASS FLOW OUT ILSG

p000

~0000*INATLO

1.0 0.0

MFLOWJ 635000

M.FLOWJ 63700

20561000

20561001

20561002

ILSGFW SUM

0.0 1.0

1.0

1.0 0.0

CNTRL VAR

CNTRL VAR

0

608

609

* FEED FLOW RATE

" RECIRC RATIO

* CIRCULATION RATIO

20562000 IRCRCR DIV 1.0

20562001 MFLOWJ 601010000

0.0 1

MFLOWJ 601020000

20562500 ICRCR DIV 1.0 0.0 1

20562501 MFLOWJ 601010000 MFLOWJ 601030000

20570600

20570601

T419 TRIPUNIT 1.0 0.0

419 * 90.9.18

1

20570700 BLMERR

20570701 23.0

SUM

-1.0

1.0 0.0

CNTRL VAR

1

24

" INPUT DESIRED BLSG

* LIQUID MASS IN KG 90.9.18

20700

20570800

20570900

20570901

*20570902

BLMCORR MULT 1.0 0.0

CNTRL VAR 706 CNTRL VAR

0 * CORRECT MASS IN

707 * BLSG UNTIL T519

BLSGLS SUM

0.0 1.0

1.0

1.0 0.0 0

MFLO Wi 735000000

MFLOWJ 737000000

* MASS FLOW OUT BLSG

20571000 BLSGFW SUM 1.0 00 0.0 0 *BRKNLO * BROKEN LOOP
20571001

20571002

0.0 1.0

1.0

CNTRL VAR 708 * FEED FLOW RATE

CNTRL VAR 709

20572000 BRCRCR DIV 1.0 0.0 1

20572001 MFLOWJ 704010000 MFLOWJ 713030000

* RECIRC RATIO

20572500 BCRCR DIV 1.0

20572501 PIFLO14J 704010000

0.0 1 *CIRCULATION RATIO

MFLOWJ 701010000

" CONTROL INTACT LOOP STEAM VALVE TO HOLD STEAM DOME PRESSURE IN

" BAND GIVEN BY TRIPS 462 AND 463 - OPEN AND CLOSE STEAM VALVE AT

" RATES GIVEN IN TRIPS 464 AND 465 - OPEN OR CLOSE DEPENDING ON

" TRIPS 662 AND 663'

20630

20563000

205631001

20563101

PERR SUM

4.55E6 -1.0

-1.0 0.0 1

P 611010000

" DESIRED PRESSURE

" PASCAL~S - MID BAND9O.9.18

DPERR DIFFREND 1.0

CNTRL VAR 630

20563200 POSDPDT TRIPUNIT 1.0

20563201 662

0.0

0.0

0.0

1

1

1 20630

'20563300

'20563301

20563400

NEGDPDT TRIPUNIT 1.0 .663

OPEN MULT

CNTRL VAR

.20563500 CLOSE MUtT

20563501 CNTRL VAR

1.0 0.0

630 CNTRL VAR

1.0 0.0

630 CNTRL VAR

1.E-8 0.0

CNTRIJVAR

CNTRI.JVAR

1

632

1

633

0

634

635

20563600

20563601

20563602

20630

20563700

RATE SUM

0.0 1.0

1.0

POSN INTEGRAL 1.0

CNTRL VAR 636

0.294088 0

" CONTROL BROKEN LOOP STEAM VALVE TO HOLD-STEAM D0Iý

* BAND GIVEN BY TRIPS 472 AND 473 - OPEN AND CLOSE

* RATES GIVEN IN TRIPS 474 AND 475 - OPEN OR CLOSE

" TRIPS 672 AND 673

IE PRESSURE IN

STEAM VALVE AT

DEPENDING ON

" DESIRED PRESSURE

* PASCAI1S - MID BAND9O.9.18

20730

20573000 PERR SUN

4.48E6 -1.0

-1.0 0.0 1

P 705010000

20573100 DPERR DIFFREND 1.0

20573101 CINTRL VAR 730

20573200 POSDPDT TRIPUNIT

20573201 672

1.0

1.0

0.0

0.0

0.0

1

1

20730

20573300

20573400

20573401.

NEGDPDT TRIPUI'

OPEN MULT

CNTRL VAR 732

1.0 0.0

730 CvNTRL VAR
20573500 CLOSE MULT 1.0 0.0 1

20573501 CNTRL VAR 730 CNTRL VAR 733

20573600 RATE SUM 4.E-9 0.0 0

20573601 0.0 1.0 CNTRLVAR 734

20573602 1.0 CNTRL VAR 735

20573700 POSN INTEGRAL 1.0 0.04367422 0

20573701 CNTRL VAR 736

* ~VESSEL, DOWNCOMER, AND UPPER HEAD EXTERNAL HEATERS*

20520000 PWRBASE FUNCTION 1.0 0.0 0

20520001 TIME 0 116

20520100 VSLPWR MULT 1.0 1.0 0

20520101 CNTRL VAR 200

20520200 UHTRIP TRIPUNIT 1.0 0.0 1

20520201 640

20520300 UVTRIP TRIPUNIT 1.0 0.0 1

20520301 641

20520400 MVTRIP TRIPUNIT 1.0 --0-.0 1

20520401 642

20520500 INVUHT SUM 1.0 1.0 1

20520501 1.0 -1.0 CNTRLVAR 202

20520600 INVUVT SUM 1.0 1.0 1

20520601 1.0 -1.0 CNTRJJVAR 203

20520700 INVMVT SUM 1.0 1.0 1

20520701 1.0 -1.0 CNTRL VAR 204

20520800 UHPWR ?IULT 0.13193 1.0 1

20520801 CNTRL VAR 201 CNTRL VAR 205

20520900 UVPWRA IIULT 0.06597 1.0 1

20520901 CNTRL VAR 201

20521000 UVPWRB MIJLT 0.01003 1.0 1

20521001 CNTRIJVAR 201 CNTRIJVAR 202

20521100 IIVP14RT SUN 1.0 1.0 1

20521101 0.0 1.0 CNTRJJVAR 209

*20521102 1.0 CNTRLVAR 210

20521200 UVPWR NIJLT 1.0 1.0 1

20521201 CNTRL VAR .211 CNTRI1VAR 206

20521300 MVPWRA MULT 0.17589 1.0 1

20521301 CNTRL VAR 201

20521400 NVPWRB NULT 0.02673 31.0 1

20521401 CNTRL VAR 201 CNTRLVAR 202

20521500 MVPWRC NULT 0.01667 1.0 1
20521501 CNTRLVAR 201 CNTRL VAR 203

20521600 NSJPWT SlIR 1.0 1.0 1

20521601 0.0 1.0 CNTRLVAR 213

*20521602 1.0 CNTRIAIAR 214

*20521603 1.0 CNTRL VAR 215

20521700 MVPWR MULT 1.0 1.0 1

20521701 CNTRL VAR 216 CNTRL VAR 207

20521800 VSPWRA MUJJT 0.62621 1.0 1

20521801 CNTRLVAR 201

20521900 VSPWRB' MULT 0.09517 1.0 1

20521901 CNTR1bVAR 201 CNTRILVAR 202

20522000 VSPWRC MULT 0.05933 1.0 1

20522001 CNTRL VAR 201 CNTRLVAR 203

20522100 VSPW4RD MULT 0.21929 1.0 1

20522101 CNIRLVAR 201 CNTRljVAR 204

20522200 VSPWR SUP] 1.0 1.0 1

20522201 0.0 1.0 CNIRLVAR 218

*20522202 1.0 CNIRLVAR 219

*20522203 1.0 CNTRLVAR 220

.*20522204 1.0 - CNTRLVAR-. 221

20522300 VTIRP TRIPUNIT 1.0 0.0 1

20522301 643

20522400 INVVI SUM 1.0 1.0 1

20522401 1.0 -1.0 CNTRLVAR 223

20522500 VSPWR NULT 1.0 1.0 1
/JOB

SNHiTS, T6000.

/USER

ATTACH,STHZXT,RE364BX.

PURGE, SN1T1RP/NA.

DEFINE, RSTPLT=SNiT1RP.

PURGE,SNHlPF5/NA.

DEFINE, PL0TFL=SNH1PF5.

ATTACH, RSTIN=SN1S2RP.

FILE,RSTIN,SBF=N0.

FILE, RSTPLT, SBF=NO.

RFL ,CM=370000 ,EC=200.

REDUCE(-

RE364BX, ,*PL=50000.

/EOR

= RELAP5 MODEL FOR THE SEMISCALE NH-i POSTTEST - TRANSIENT RUN

(BRK 0.000012079 , ALL LEVEL 090.10.10) 16:30

*PROBLEM

0000100

0000101

. *UNITS

*0000102

0000103

*TIME OUT

*0000105

0000201

3750000

3750101

3750102

3750201

3750300

3750301

TYPE . OPTION

RESTART TRANSNT

INP-CHK OR RUN

RUN

-INPUT.-----OUT-PUT -(SI

BRITISH S.

14170 *(90.10.8. 09:20)

OR BRITISH)

FROM SNH1S2, SN1S2RP PZR'INTERFACE LEVEL CHECK

MIN MAX

125.0 150.0

T END MIN ST MAX ST

5000. 1.0-7 0.05

ST CL

3

MR NJ

40 2000 2000

WR

BRK-VLV VALVE

362010000 900000000

0.90 0.90

1 0.0 0.0 0.0

TRPVLV

402

0. 000012079 0.0 0.0 100 * (90.9.28)

20505100 INTBRK INTEGRAL 1.0

20505101 MFLOWJ 375000000

0.0 0

*DELETE PUMP S.S. CONTROLLER

*20525000 ILNERR DELETE 0.0 0.0 0.0 0.0 0.0 0.0

*20535000 BLMERR DELETE 0.0 0.0 0.0 0.0 0.0 0.0

* ADD PUMP TRANSIENT CONTROLLER

20525100 ILPMPSPD FUNCTION 1873.37 0.0 1

20525191 TINE 0 250

20535100 BLPMPSPD FUNCTION .1492.32 0.0 1

20535101 TIME 0 350

* DELETE PZR LEVEL CONTROLLER

20598000 T4119 DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20598100 PZRERR DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20598200 PZRCORR DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20598500 PZRFW DELETE 0.0 0.0 0.0 0.0 0.0 0.0

* DELETE PZR COMPONENT

9100000 PZRSPRY DELETE
9850000 PZRIJVLJ DELETE

9910000 TMD-PRZ DELETE

* DELETE S/G LEVEL CONTROLLER

20560600 T419 DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20560700 ILMERR DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20560800 ILMCORR DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20560900 ILSGLS DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20561000 ILSGFW DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20562000 IRCRCR DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20562500 ICRCR DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20570600 T419 DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20570700 BLMERR DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20570800 BLNCORR DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20570900 BLSGLS 'DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20571000 BLSGFW DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20572000 BRCRCR DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20572500 BCRCR DELETE 0.0 0.0 0.0 0.0 0.0 0.0

*20563000 PEER DELETE 0.0 0.0 0.0 0.0 0.0 0.0

*20563100 DPERR DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20563200 POSDPDT DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20563300 NEGDPDT DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20563400 OPEN DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20563500 CLOSE DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20563600 RATE DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20563700 POSN DELETE 0.0 0.0 0.0 0.0 0.0 0.0

*20573000 'PEER DELETE 0.0 0.0 0.0 0.0 0.0 0.0

*20573100 DPERR DELETE 0.0 0.0 0.0 0.0 0.0 0.0.

20573200 POSDPDT DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20573300 NEGDPDT DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20573400 OPEN DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20573500 CLOSE DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20573600 RATE DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20573700 POSN DELETE 0.0 0.0 0.0 0.0 0.0 0.0

20598000

20598001

20598100

20598101

T429 TRIPUNIT 1.0 0.0 1

429

PZRERR SUM 0.01 0.0 1

340.0 -1.0 CNTRLVAR 6

* S-NH-i TRIP SEQUENCE

* OPEN BREAK

0000402 TIME 0 GE NULL 0 0.0 1, -1.

* SCRAM SIGNAL

0000407 P 999010000 LE NULL 0 1900.1

* MAIN STEAM VALVE CLOSE (INTACT & BROKEN)

0000410 TIME 0 GE TIMEOF 407 1.0 L

0000411 TIME 0 GE TINEOF 407 1.0 L

* SI SIGNAL GENERATED

0000421 P 999010000 LE NULL 0 1815.0

0 L -1.

-1.

-1.

L -1.

* MAIN FW STOPPED

0000414 TIME 0

0000415 TIME 0

* AUX FW ACTUATED

0000416 TIME 0

0000417 TIME 0

GE

GE

GE

GE

TIMEOF 421 1.0 L

TIMEOF 421 1.0 L

TIMEOF 421. 1.0 L

TIMEOF 421 1.0 L

-1.

-1.

-1.

-1.

6150000

6150101

6150200

6150201

6150202

ISGAFWJ TMDPJUN

625000000 603010000

1 416

-1.0 0.0 0.0 0.0

0.0 0.0 0.0 0.0

0.012
6150203

6340000

6340101

6340201

6340300

6340301

7280000

7280101

7280200

7280201

7280202

7280206

2000.0 0.0 0.0 0.0

ISGRV VALVE * SIMUILATED ADV

611010000 640000000 0.0002592 0.0 0.0 100

1 0.0 0.0 0.0

TRPVLV

661

BSGAFWJ TMDPJUN

729000000 726000000 0.004

1 417

-1.0 0.0 0.0 0.0

0.0 0.0 0.0 0.0

2000.0 o:o 0.0 0.0

7340000 BSGRV VALVE * SIMULATED B ADV

7340101 705010000 740000000 0.007 0.0 0.0

7340201 1 0.0 0.0 0.0

7340300 TRPVLV

7340301 671

* PUMP COASTUOWN

0000412 TIME 0 GE TIMEOF 421 2.0 L -1.

0000413 TIME 0 GE TIMEOF 421 2.0 L -1.

* MAX PCT

0000426 CNTRJJVAR 29 GE NULL 0 811.0 N -1. *STEAM ADV VALVE OPEN

0000661 426 AND 426 N -I.-

0000671 426 AND 426 N -1.

* ACC INJECTION TIME

0000450 MFLOWJ 430010000 GT NULL 0 0.0 N -;

0000451 MFLOWJ 530010000 GT NULL 0 0.0 N

* LPIS SET POINT TIME

0000499 P 999010000 LT NULL 0 0.0 L -1.

* ADD SC MAIN FW COMPONENT

6100000 ISGFWJ TMDPJUN

6100101 620000000 603010000 0.012

6100200 1 414

6100201 -1.0 1.8078 0.0 0.0 *90.10.08

6100202 0.0 1.8078 0.0 0.0

6100203 24.0 1.8078 0.0 0.0

6100204 26.0 0.0 0.0 0.0

100

1.

-1.

7220000

7220101

7220200

7220201

7220202

7220203.

7220204

BSGFWJ TMDPJUN

724000000 720000000 0.004

1 415

-1.0 0.56119 0.0 0.0

0.0 0.56119 0.0 0.0

24.0 0.56119 0.0 0.0

26.0 0.0 0.0 0.0

*6150000 (T416) & 7280000 (T417) FOR AUX FW

6350000 ISGDJ VALVE

6350101 611010000 650000000 0.007 204.67 204.67 100

6350201 1 0.0 5.6034 0.0

6350300 MTRVLV

61350301 403 410 .3333 .2940 0

7350000 BSGDJ VALVE
7350101

7350201

7350300

7350301

705010000 750000000 0.007 1022.36 1022.36 100

1 0.0 0.56119 0.0

MTrRVLV

403 411 0.2 0.04367 0

**TRIPS -- TRIP CANCELLATION CARD 400

** -- TRIP STOP CARD 600

*MINOR EDIT VARIABLES

VARIABLE TRIP CARDS 401-599 *

LOGICAL TRIP CARDS 601-699 *

0000301

0000302

0000303

0000304

0000305

0000306

0000307

0000308

0000309

0000310

0000311

0000312

0000313

0000314

0000315

0000316

0000317

0000318

0000319

0000320

0000321

0000322

0000323

0000324

0000325

0000326

0000327

0000328

0000329

0000330

0000331

0000332

0000333

0000334

0000335

*0000336

0000337.

*0000338

0000339

0000340

0000341

0000342

0000343

0000344

0000345

0000346

0000347

0000348

0000349

0000350

CNTRJJVAR

CNTRL VAR

CNTRLVA1

CNTRL VAR

CNTRL VAR

CNTRL VAR

CNTRL VAR

CNTRL VAR

CNTRL VAR

CNTRL VAR

CNTRL VAR

CNTRL VAR

CNTRL VAR

CNTR.LVAR

CNTRL VAR

CNTRJLVAR

CNTRL VAR

CNTRL VAR

CNTRJJVAR

CNTRL VAR

CNTRL VAR

CNTRL VAR

CNTRI4VAR

CNTRL VAR

CNTRiLVAR

CNTRJNAR

P

P

P

P

MFLOWJ

ffFLOWJ

MFLOWJ

MFLOWJ

MFLOWJ

MFLOWJ

MFLOWJ

MFLOWJ

MFLOWJ

MFLOWJ

MFLOWJ

MFLOWJ

MFLOWJ

MFLOWJ

DIFLOWJ

PMPVEL

PMPVEL

VEFF

VELG

VELF

6

9

10

13

14

15

16

.17

18

26

27

28

29

150

151

501

502

506

509

510

513

514

531

532

162010000

601010000

701010000

999010000

375000000

635000000

735000000

610000000

722000000

420010000

430010000

520010000

530010000

615000000

728000000

634000000

734000000

262010000

362010000

250

350

301060000

301060000

203030000

* VESSEL LEVEL

* CORE LEVEL

* PZR LEVEL

" ILPMP DOWN LEVEL

* ILPMP UP LEVEL

" BLPPNP DOWN LEVEL

* BLPMP UP LEVEL

* ILSG2UP LEVEL

* ILSG2DN LEVEL

* BLSG2UP LEVEL

* BLSG2DN LEVEL

* ILSG HEAT (K(W)

" BLSG HEAT (1(W)

* .CORE POWER (K(W)

* MAX ROD TEMP

" UCY POWER. ..61WI -

;k ACT POWER'(WATT)

* VESSEL LEVEL DP

* CORE LEVEL DP

* PZR LEVEL DP

* ILPMP DOWN DP

* ILPMP UP DP

* BLPMP DOWN DP

* BLPMP UP DP

* VESSEL COLLAPSED LEVEL

* CORE COLLAPSED LEVEL

* PVUP

* PISG2

* PBSG2

*PPZR

*BREAK FLOWRATE

*MISG2 OUT (MAIN)

*MBSG2[C[C[C[C

*MISG2 IN

*MBSG2 IN

FIHPIS

*MBACC

*MISOAIIX

*MBSGAUX

*MISGADV

*MBSGADV

*MIL

*MBL

*VIPUMP

* VBPUMP

* LIQUID VELOCITY BLHL

* VAPOR VELOCITY BLIL

* LIQ VEL ILHL
0000351 VELG

0000352 RHO

0000353 RHO

0000354 RHO

0000355 RHO

0000356 RHO

0000357 RHO

0000358 RHO

0000359 VOIDF

0000360 VOIDF

0000361 VOIDF

0000362 VOIDF

0000363 VOIDF

0000364 VOIDF

0000365 VOIDE

0000366 VOIDF

0000367 VOIDF

0000368 VOIDE

0000369 VOIDF

0000370 VOIDF

0000371 VOIUF

0000372 VOIDF

0000373 VOIDF

0000374 VOIDF

0000375 VOIDF

0000376- VOIDF

00003.77. VOIDF

0000399 VOIDF

0000378 VOIDF

0000379 VOIDF

0000380 VOIDF

0000381 VOIDF

0000382 VOIDF

0000383 VOIDF

0000384 HTTEI'D

0000385 HTTEM]

0000386 HTTEM]

0000387 TEMPF

0000388 TENPF

0000389 TEMPF

0000390 CNTRI

0000391 CNTR]

0000392 MFLOWJ

0000393 CNTRLV~

*PLOT VARIABLES

LVAR

UVAR

203030000

201010000

263010000

301010000

363020000

150010000

150030000

150060000

220010000

220020000

220030000

220040000

220050000

220060000

220070000

220080000

320010000

320020000

320030000

320040000

320050000

320060000

320070000

320080000

240080000

240090000

.340080000-

340090000

150010000

150020000

150030000

150040000

150050000

150060000

150000112

150000612

150001212

162010000

140010000

620010000

15 *

17 *

*

*

*

*

*

*

*

*

*

YAP VEL

DENSITY

DENSITY

DENSITY

DENSITY

DENSITY

DENS ITY

DENSITY

V01D IL

ILHL

ILHIJ

ILCL

BLHIJ

BLCL

VESSEL

VESSEL

VESSEL

SG

AT 012

AT 183

AT 342

"*OD LS

"*ODI UPSCINU

-*VOID BL PUMP SUCTION UP

* VOID CORE

*CORE HEATER TI

SGlIUP

SG1BUP

* DC

AR

110010000

51 * INT BRI(

Z0000

20300100

20300200

20300300

20300400

20300500

20300600

20300700

20300800

203010900

203011000

20301100

210301300

Z0301400

P

P

P

P

P

P

P

P

MFLOWJ

MFLOWJ

MFLOWJ

MFLOWJ

MFLOWJ

MIFLOWJ

162010000

201010000

263010000

301010000

363010000

601010000

701010000

999010000

3,75000000

635000000

73500Q000

610000000

722000000

615000000

*

*

*

*

*

*

*

*

*

*

*

*

*

*

UPPER PLENUM

LOW4ER PLENUM

SG FDW TEMP

PVHJP (MPA I

PIHL

PICL

PBHL

PBCL

PISG2

PBSG2

PPZR

MBRK [KG/S]

MISG20

MBSGZO

MISG2I

MBSGZI

MISG2PAUXI

EMP (DOWN)

(MID)

(UP)

LIQ TEMP

LlQ TEMP

(PV*UP-13)

(PI*1)

(PI*23A)

(PB*50)

(PB*79)

(PIS+1117)

(PBG+1186)

(P*PRZ+632)

(MDOT*BREAK)

(MDOT*ILSTM)

(MDOT*BLSTM)

(MDOT*ILFDW)

(MD0T*D"LFDW)

(MDOT*IGAXFW)
20301500

20301600

20301700

*20301800

20301900

*20302000

20302100

20302200

20302300

20302400

20302500

20302600

20302700

20302800

20302900

20303000

20303100

20303200

20303300

20303400

20303500

20303600

20303700

20303800

20303900

20304000

†20304100

20304200

20304300

20304400

20304500

20304600

20304700

20304800

20304900

20305000

20305100

20305200

20305300

20305400

20305500

20305600

20305700

20305800

20305900

20306000

20306100

20306200

20306300

20306400

20306500

20306600

20306700

20306800

20306900

20307000

20307100

20307200

20307300

20307400

20307500

MFLOWJ

MFLOWJ

MFLOWJ

M*FLO14J

NFLOWJ

I1FL0WJ

MELOWJ

MFLO~WJ

M1FL0WJ

CNTURL VAR

CNTRL VAR

CNTRL VAR

CNTRL VAR

CNTRLVAR

CNTRJJVAR

CNTRL VAR

CNTRL VAR

CNTRIJVAR

RHO

RHO

RHO

RHO

RHO

RHO

RHO

VELF

VEJG.

VELF

VELG

VOIDF

VOIDF

VOIDF

VOIDE

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

VOLUF

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

VOIDE

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

728000000

634000000

734000000

420010000

430010000

520010000

530010000

262010000

362010000

509

510

513

514

1

4

5

3

6

201010000

263010000

301010000

363020000

150010000

150030000

150060000

301060000-

301060000

203030000

203030000

220010000

220020000

220030000

220040000

220050000

220060000

220070000

220080000

320010000

320020000

320030000

320040000

320050000

320060000

320070000

320080000

240010000

240020000

240030000

240040000

240050000

240060000

240070000-

240080000

240090000

340010000

340020000

340030000

340040000

340050000

340060000

340070000

" MBSGZAUXI

" MISG2ADVO

" MBSG2ADVO

" NIHP

" MIACC

" MIBHP

" MBACC

" MIILHL

" IIBLAL

" DPIPD

" DPIPD

" DPBPD

" DPBPU

" LVl

" LV4

* LV5

" LVDC

" LVPZR

" DILHL WKG/3]

" DILCL

" DBI2HL

" DBLCL

" DVO12

* DV183

" DV342

" VLBLHL WNS)

" VGBLHL

" VLILHL

* VGILHh

" VDISG1

(tNDOT*BGAXFW)

(tNDOT* IL*ADV)

(tNDOT*BL*ADV)

(MDOT*IL*ACUN)

(MDOT*BL*ACUM)

(DPI-57X*14A)

(DPI*14B*16)

(DPB-57X*65A)

(DPB*65*73A)

(LV-13M-578)

(LV+135-13N)

(LV+421A-160)

(LVD+29-578)

(LPRZ*PROCESS)

(RI*1B)

(RI*23A*B)

(RB*5OB)

(RB*99B)

(RV*23+12)

(RV*234-183)

(RV*23+342)

" VDBSG1

" VDIPDIP

" VDBPDIP
20307600

20307700

20307800

20307900

20308000

20308100

20308200

20308300

20308400

20308500

20308600

20308700

20308800

20308900

20309000

20309100

20309200

20309300

20309400

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

VOIDF

CNTRL VAR

PRPVEL

PMPVEL

IITTEMP

HTTEMP

HTTEMP

TEMPF

TEMPF

TEMPF

CNTRJJVAR

CNTRL VAR

340080000

340090000

150010000

150020000

150030000

150040000

150050000

150060000

150

250

350

150000112

150000612

150001212

162010000

140010000

620010000

15

17

*

*

*

*

*

*

*

*

*

DCYPOWER [PC

VIPUMP [R/S]

VBPUMP

TH043H [K)

THPEP1K

T11352H

TFVUP

TFVLP

TFIFDW

(CORE.POWER)

(WI*PUNP)

(14B*PUNi')

(THV*B3+43)

(THV*PEAK)

(THV*D2+352)

(TFV*UP-13M)

(TFV*LP-552)

(TFSC*IGFDW)

'~SG11UP (LIP+971-57E)

'~SGIBUP (LBPLH993-57E)

20309500 MFLOWJ 110010000

20309600 CNTRL VAR 51 *

$$$$$$$$ ****** END

* DC

INT BRK

OF RELAP5 INPUT
4RC FOR--- 335 U.S. NUCLEAR REGULATORY COMMISSION 1. REPORT NUMBER

Q-89) lAosig-~d by NRC. Add Vol.. Sqpp.. Rev.. NRCM 1102. a-d A~dd-r~vm Numb.,,. If sny.I 3201.3202 BIBLIOGRAPHIC DATA SHEET

2TILANSUTTE(See I'nsrrucrions on the reese NUREG/IA-0099

RELAP5 Assessment Using Sendscale SBLOCA. Test S-NH-I 3. DATE REPORT PUBLISHED

MONTH YEAR

~June 1993

4. FIN OR GRANT NUMBER

____ ___ ____ ___ ____ ____ ___ ___ ____ ___ ___ ____ ___ ___ ___ L2245

5. AUTHOR(IS) 6. TYPE OF REPORT

Euy-Joon Lee, Bub-Dong Chung and Hho-Jung Kim

Technical

7. PERIOD COVERED fircluuve Daes)

nam. *ad maoflkg adamsi

Safety Analysis Department

Korea Institute of Nuclear Safety

P.O. Box 16, Daeduk Danji.

Taej.on, Korea

9. SPONSORING ORGANIZATION - NAME AND ADDRESS 111Nqc, trpe gbeilatcop.idNOg'n.Office or R*Ndft. U.Sý. uclea,-Aeu1Jro,-rnVs~n

sod mefflVn add.'euI

Office of Nuclear Regulatory Research

U.S. Nuclear Regulatory Commission

Washington, D'C. 20555

10. SUPPLEMENTARY NOTES

It. ABSTRACT 120Vof wa r.lost)

2-inch cold leg break test S-NH-i1, conducted at the 1/1705 volume scaled facility Semiscale, was analyzed using

RELAP5IMOD2 Cycle 36.04 and MOD3 Version 5m5. Loss of HPIS was assumed, and reactor trip occurred on a

low PZR pressure signal (13.1 UFA), and pumps began an unpowered coastdown on SI signal (12.5 MýTa). The

system was recovered by opening ADV's when the PCTr became higher than 811 K. Accumulator was finally

Iinjected into the system when the primary system pressure was less than 4.0 MPa. The experiment was terminated

when the pressure reached the LPIS actuation set point. RELAP5/M1OD2 analysis demonstrated its capability to

predict, with a sufficient accuracy, the main phenomena occurring in the depressurization transient, both from a

qualitative and quantitative points of view. Nevertheless, several di *fferences were noted regarding the break flow

rate and inventory distribution due to deficiencies in two-phase choked flow model, horizontal stratification

interfacial drag, and a CCFL model. The main reason for the core to remain nearly fully covered with the liquid was

the under-prediction of the break flow by the code. Several sensitivity calculations were tried using the, MOD2 to

improve the results by using the different options of break flow modeling (downward, homogeneous, and area

increase). The break area compensating concept based on "the integrated break flow matching" gave the best results

than downward junction and homogeneous options. And the MOD3 showed improvement in predicting a CCFL in

SG and a heatup in the core.

12. KEY WORDSIDESCR!PTORS (List~n wodr Opilaw that wiltsWilt ftambonf ko locitinp therrwoon.) 13. AVAILABILTY STATEMENT

ICAP Program Unlimited

RELAP5 14. SECURITY CL.ASSIFICATION

Semiscale SBLOCA.. Irhil Pa"e

Unclassified

["71 Repont

Unclassified

15. NUMBER OF PAGES

16. PRICE

NRC FORM 335 (2-89)
Federal Recycling Program

UNITED STATES

NUCLEAR REGULATORY COMMISSION

WASHINGTON, D.C. 20555-0001

OFFICIAL BUSINESS

PENALTY FOR PRIVATE USE, $300

SPECIAL FOURTH-CLASS RATE

POSTAGE AND FEES PAID

USNRC

PERMIT NO. G-67