NUREG/IA-0103

International

Agreement Report

Assessment of

BETHSY Test 9.1.b

Using RELAP5/MOD3

Prepared by

S. Lee, B. D. Chung, H. J. Kim

Korea Institute of Nuclear Safety

P. 0. Box 16

Daeduk-Danji

Daejon, Korea, 305-606

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

the United States Government nor any agency thereof, or any of

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

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

use, or the results of such use, of 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.

Available from

Superintendent of Documents

U.S. Government Printing Office

P.O. Box 37082

Washington, D.C. 20013-7082

and

National Technical Information Service

Springfield, VA 22161
NUREG/IA-0103

International

Agreement Report

Assessment of

BETHSY Test 9.1.b

Using RELAP5/MOD3

Prepared by

S. Lee, B. D. Chung, H. J. Kim

Korea Institute of Nuclear Safety

P. 0. Box 16

Daeduk-Danji

Daejon, Korea, 305-606

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 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 USNRC 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 Commission 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.
ICAP

ASSESSMENT OF BETHSY TEST 9.l.b USING RELAP5/MOD3

Abstract

2" cold leg break test 9.1.b, conducted at the BETHSY facility was

analyzed using the RELAP5/1OD3 Version 5m5 code.

The test 9.1.b was conducted with the main objective being the

investigation of the thermal-hydraulic mechanisms responsible for the

large core uncovery and fuel heat-up, requiring the implementation of

an ultimate procedure.

The present analysis demonstrates the code's capability to

predict, with sufficient accuracy, the main phenomena occurring in the

depressurization transient, both from a qualitative and quantitative

point of view. Nevertheless, several differences regarding the

evolution of phenomena and affecting the timing order have to be

pointed out in the base calculation.

Three calculations were carried out to study the sensitivity to

change of the nodalization in the components of the loop seal

cross-over legs, and of the auxiliary feedwater control logics, and of

the break discharge coefficient.

iii

Executive Sumary

The BETHSY Test 9.1.b has been analyzed using the RELAP5/MOD3

version 5m5 codes to assess the code's ability for a 2 inch cold leg

break LOCA, to improve common understanding of PWR thermal-hydraulic

response during such a transient and to identify areas for desirable

model .improvements based on comparisons between data and predictions.

The maii. goal of the calculation is the assessment of the

simulation capability of the code for the following phenomena occurring

during the small break LOCA experimental test, particularly for the

large core uncovery and fuel heat-up, requiring the implementation of

an ultimate procedure.

The calculated overall trend agreed well with the test data.

However, several differences regarding the evolution of phenomena and

affecting the timing order have to be point out.

In the base calculation with the RELAP5/MOD3, one can observe

three fundamental disagreements between calculated and experimental

transient sequences. The first is the overestimation of the calculated

break flow rate between 1500 and 2500 seconds leading to an excessive

mass discharge from the primary system and therefore from the pressure

vessel. This may cause faster depressurization, earlier opening of

steam generator steam dump system and earlier accumulator injection

compared with the test. The second is the occurrence of loop seal

V
clearing in the cross-over leg. In the experiment, loop seal clearing

occurred in the cross-over leg of the loop 2 (intact), while it

occurred first in that of the loop 2 and next in that of the loop 1

(broken) in the present calculation. The third discrepancy of the

calculation in comparison with the experiment is the auxiliary

feedwater flow rate to each steam generator. In the experiment the

auxiliary feedwater flow was controlled by the steam generator narrow

range liquid level. This discrepancy may cause the large differences

in the steam generator mass inventory.

Three calculations were carried out to study the sensitivity to

change of the nodalization in the components of the loop seal

cross-over legs, and of the auxiliary feedwater control logics, and of

the break flow discharge coefficient. The change of the nodalization

into twice than the base case in the cross-over leg resulted in little

differences in the transient thermal-hydraulic behavior and its timing

order. However the changes of the auxiliary feedwater control logic

with steam generator wide range liquid level shows better prediction of

the auxiliary feedwater supply. And the change of the break discharge

coefficient from 0.85 to 1.0 for the subcooled liquid causes in

excessive mass discharge from the break leads to earlier core heatup

and earlier opening of SG steam dump system.

vi
List of Contents

Abstract ....................................................... iii

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

List of Tables ................................................. viii

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

1. Introduction .................................................. 1

2. Facility and Test Description ................................. 3

2.1 Facility Description ....................................... 3

2.1.1 General Design ......................................... 3

2.1.2 Main Characteristics ................................... 3

2.2 Test Description ........................................... 6

3. Code and Modeling Description ................................. 8

3.1 Code Description ...... , .................................... 8

3.2 Modeling Descriptions ...................................... 8

4. Base Case Calculations ........................................ 12

5. Sensitivity and Nodalization Studies .................. , ....... 18

5.1 Sensitivity ................................................ 18

5.2 Nodalization ............................................... 19

6. Run Statistics ................................................ 21

7. Conclusions ................................................... 22

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

Appendix

vii
List of Tables

Table 1 Specified Operational Setpoints and Conditions for BETHSY

Test 9.1.b .............................................. 24

Table 2 Comparison of Initial Conditions ........................ 25

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

Table 4 Run Statistics Data in Base Case ........................ 29

viii
List of Figures

Fig. 1 General Structure of BETHSY Test Facility ............... 30

Fig. 2 Nodalization of BETHSY for RELAP5/MOD3 Code ............. 31

Fig. 3 Primary Pressure ........................................ 32

Fig. 4 SG Steam Dome Pressure .................................. 33

Fig. 5 Upper Head Diff. Pressure ............................... 34

Fig. 6 Upper Plenum Diff. Pressure ............................. 35

Fig. 7 Core Collapsed Level .................................... 36

Fig. 8 Break Flowrate .......................................... 37

Fig. 9 Integrated Break Mass Flow ....... .............. 38

Fig. 10 SG Steamline Steam Flowrate ............................ 39

Fig. 11 Accumulator Pressure .................................. 40

Fig. 12 Accumulator Mass .................................. * .... 41

Fig. 13 SG 1 U-Tube Inlet-To-Outlet Diff. Pressure ............ .42

Fig. 14 SG 1 Inlet Plenum Diff. Pressure . ................. 43

Fig. 15 SG 1 U-Tube Upflow Side Diff. Pressure .................. 44

Fig. 16 SG 2 U-Tube Inlet-To-Outlet Diff. Pressure ............. 45

Fig. 17 SG 2 Inlet Plenum Diff. Pressure ........................ 46

Fig. 18 SG 2 U-Tube Upflow Side Diff. Pressure .............. 47

Fig. 19 SG 3 U-Tube Inlet-To-Outlet Diff. Pressure ............ 48

Fig. -20 SG 3 Inlet Plenum Diff. Pressure ...................... 49

Fig. 21 SG 3 U-Tube Upflow Side Diff. Pressure .............. 50

ix
Fig. 22 Loop Seal 1 Downflow Side Diff. Pressure ................ 51

Fig. 23 Loop Seal 1 Upflow Side Diff. Pressure ................. 52

Fig. 24 Loop Seal 2 Downflow Side Diff. Pressure ................ 53

Fig. 25 Loop Seal 2 Upflow Side Diff. Pressure .................. 54

Fig. 26 Loop Seal 3 Downflow Side Diff. Pressure ................ 55

Fig. 27 Loop Seal 3 Upflow Side Diff. Pressure .................. 56

Fig. 28 Core Heated Length Diff. Pressure ....................... 57

Fig. 29 Heater Rod Temperature .................................. 58

Fig. 30 Heater Rod Temperature ......................... ......... 59

Fig. 31 Maximum Clad Temperature ................................ 60

Fig. 32 SG Feedwater Mass Flowrate .............................. 61

Fig. 33 SG Mass Inventory ....................................... 62

Fig. 34 Hot Leg 1 Void Fractions ................................ 63

Fig. 35 Hot Leg 2 Void Fractions ................................ 64

Fig. 36 Hot Leg 3 Void Fractions ................................ 65

Fig. 37 Cold Leg 1 Void Fractions ............................... 66

Fig. 38 Cold Leg 2 Void Fractions ............................... 67

Fig. 39 Cold Leg 3 Void Fractions ............................... 68

Fig. 40 Guide Tube Diff. Pressure ............................... 69

Fig. 41 Downcomer-To-Upper Head Diff. Pressure .................. 70

Fig. 42 Pressure Vessel Diff. Pressure .......................... 71

Fig. 43 Cold Leg 1 To Hot Leg 1 Diff. Pressure .................. 72

Fig. 44 Pump 1 Diff. Pressure ................................... 73

Fig. 45 Cold Leg 2 To Hot Leg 2 Diff. Pressure .................. 74

x
Fig. 46 Pump 2 Diff. Pressure ................................... 75

Fig. 47 Cold Leg 3 To Hot Leg 3 Diff. Pressure .................. 76

Fig. 48 Pump 3 Diff. Pressure ................................... 77

Fig. 49 SG I Boiler Section Diff. Pressure ...................... 78

Fig. 50 S6 2 Boiler Section Diff. Pressure ...................... 79

Fig. 51 SG 3 Boiler Section Diff. Pressure ...................... 80

Fig. 52 Pressurizer Diff. Pressure .............................. 81

Fig. 53 LPSI Mass Flowrate ...................................... 82

Fig. 54 Integrated LPSI Mass Flow ............................... 83

Fig. 55 Primary and Secondary Pressures ......................... 84

Fig. 56 Mass Flow Rate .......................................... 85

Fig. 57 Core Inlet & Outlet Temperatures ........................ 86

Fig. 58 Upper Head Temperatures ................................. 87

Fig. 59 Loop 1 Temperature ...................................... 88

Fig. 60 Loop 2 Temperature .............. : ....................... 89

Fig. 61 Loop 3 Temperature ...................................... 90

Fig. 62 Bottom SG Downcomer Temperature ......................... 91

Fig. 63 RCP Rotational Speed ................................... 92

Fig. 64 Core Power ............................. ................. 93

Fig. 65 Time Step .................................... .......... 94

Fig. 66 Pressurizer Level ...................................... 95

Fig. 67 SG I Wide Range Level' .................................. 96

Fig. 68 Primary Side Mass Inventory ............................. 97

Fig. 69 SG Feedwater Mass Inventory ............................. 98
Fig. 70 SG Mass Inventory ....................................... 99

Fig. 71 Break Flowrate ......................................... 100

Fig. 72 Integrated Break Mass Flow ............................. 101

Fig. 73 Primary Pressure ....................................... 102

Fig. 74 SG Steamline Steam Flowrate ............................ 103

Fig. 75 Maximum Clad Temperature ............................... 104

Fig. 76 Core Collapsed Level ................................... 105

Fig. 77 Loop Seal I Downflow Side Diff. Pressure ............... 106

Fig. 78 Loop Seal 1 Upflow Side Diff. Pressure ................. 107

Fig. 79 Loop Seal 2 Downflow Side Diff. Pressure ............... 108

Fig. 80 Loop Seal 2 lpflow Side Diff. Pressure ................. 109

xii
1. Introduction

The International Code Assessment and Application Program (ICAP)

has been conducted by fourteen nations and multinational organizations

under the auspices of the USNRC[1]. For the pressurized water reactor

analysis, the USNRC selected two best estimate (BE) codes: RELAP5/MOD2

and TRAC/PF1/AOD1[2]. The goal of the program is to assess the

prediction capabilities of the current BE thermal hydraulic codes

utilizing the available facility test and plant data. At present the

ICAP activities in Korea help to quantify uncertainties in the codes so

that the codes may be used for regulatory purposes.

This report is a part of the Korean contribution to the ICAP. The

RELAP5/1OD3[3] Version 5m5 were used in the present calculations

simulating the test 9.1.b of the BETHSY facility [4-6].

The main goal of the calculation is the assessment of the

simulation capability of the code for the following phenomena occurring

during the small break LOCA experimental test, particularly for the

large core uncovery and fuel heat-up, requiring the implementation of

an ultimate procedure.

The report describes the results of the calculation performed by

the RELAP5/1OD3 codes and shows the comparisons with the major

variables obtained in the experiment. A brief description of the

BETHSY and 9.1.b test is provided in Section Z, and Section 3 describes

I
the features of .the RELAP5 code and modeling to be assessed. Section 4

discusses the results of the base calculations with the RELAP5/MOD3;-

The motivations for the sensitivity and nodalization studies and their

results are included in Section 5. The code efficiency is evaluated in

Section 6 through run statistics. The conclusions drawn from this

study are given in Section 7.

2
2. Facility and Test Description

2.1 Facility Description

The BETHSY integral test facility has been designed for the analysis

of PWR accident situations controlled by automatic circuits and/or

operator actions.

The main objectives of the BETHSY test program are to contribute to:

- improve the knowledge of the physical phenomena which occur during

PWR accidents, particularly when two-phase flow takes place 'at the

primary coolant system

- assess safety computer codes, especially the advanced code CATHARE

- validate the physical assumptions of event and state oriented Emergency

Operating Procedures.

2.1.1 General design

BETHSY is designed to model a 3 loop - 2775 NWt - Framatome PWR as

shown in Fig. 1. The overall scaling factor is 1/100 while the

elevations are 1/1, and the design pressures are 17.2 MPa and 8 IPa for

the primary and the secondary coolant systems which can play a role

during an accident transient.

2.1.2 Main characteristics

3
i) Pressure vessel

The cylindrical core consists of 428 full length - 17 x 17 design -

heater rods and 29 guide thimbles. The axial peaking factor is 1.5 and

the radially uniform core power is up to 3 MW (i.e. about 10% of the

scaled nominal value).

The core bypass is represented and the external downcomer is linked

to the upper head through calibrated orifices in order to simulate the

downcomer to upper head spray nozzles.

ii) Primary coolant piping and pumps

BETHSY has the same number of loops as the reference reactor. The

inner diameter of all the piping is 118mnnas given by the Froude number

conservation applied to the hot legs, and the elevation of the

horizontal part of the crossover leg is preserved. The primary coolant

pumps are capable of delivering the nominal flow rate but have also a

controllable rotation speed in order to obtain, when necessary, both

the right initial energy distribution at the primary side and to

simulate the pump coastdown. The elevation of the pump diffuser with

respect to the cold leg is preserved.

iii) Pressurizer

Connected either to an intact or broken loop, the pressurizer is

equipped with on-off and proportional heaters, the normal and the

auxiliary spray systems, a relief circuit with adjustable setpoints and

4
relief capacity.

iv) Secondary coolant system

Each of the three steam generators includes 34 U-tubes of the same

radial dimensions and height stepping (9 to 10.5 m) as in the reference

steam generators, and so arranged that the hydraulic diameter of the

secondary side is preserved and the tube lane is true to scale.

The main and auxiliary feedwater systems can operate at adjustable

flow rate and temperature, and the steam system in particular includes

isolation valves and steam dumps to the atmosphere or to the condenser

(adjustable setpoints and relief capacities).

v) Safety injection systems

All the emergency core cooling systems (HPIS, accumulators, LPIS)

are represented and BETHSY is designated for ECC water to be injected

not only in the cold legs but also at other locations such as the hot

legs, the top of the downcomer, the lower and the upper plenum. HPIS

and LPIS flow rates are controlled by the primary coolant system

pressure so as to obtain scaled flow rates at every time.

Three volume scaled accumulators pressurized with nitrogen can

supply the primary coolant system with room temperature water at a

pressure up to 7 Pa.

vi) Trace Heating

5
The primary coolant system and the steam generators are equipped

with trace. heaters in order to compensate for the heat losses which are

never to scale on an integral test facility and which could distort

certain phenomena especially in steady state conditions or along slow

transients.

vii) Instrumentation

Detailed information on thermal-hydraulic phenomena which take place

both at the primary and secondary side is provided by more than 1200

transducers whose signal is scanned at a sampling rate of 2 Hz.

viii) Control system

The BETHSY control system - distributed microcomputer type - enables

the facility to be operated from three operator stations and is

designed for an automatic control of sequences (simulation of automatic

reactor systems and operator actions).

2.2 Test Description

The test 9.1.b belongs to the multiple failure transient category,

and is involved in accident management studies : it consists in a 2"

cold leg break, while high pressure safety injection system (HPIS) is

assumed unavailable. This transient leads to a large core uncovery and

fuel heat-up, requiring the implementation of an ultimate procedure.

6
In the presently studied scenario, the start of the procedure is

delayed, and the following trigger criterion is used : when the maximum

heater rod cladding temperature reaches 450 C, the 3 steam generator

steam dump to atmosphere are fully opened (condenser is unavailable).

This action allows the primary coolant circuit to depressurize, up

to the accumulator injection threshold, then to LPIS actuation.

The end of the test is reached as soon as a safe state of the

primary coolant circuit is recovered, i.e. when the conditions

required for the actuation of the residual heat removal system are

obtained.

7
3. Code and Modeling Description

3.1 Code Description

The RELAP5/tOD2 code has been developed for best-estimate

transient simulation of PWRs and associated systems. The code is based

on a non-homogeneous and non-equilibrium model for one dimensional,

two-phase system that is solved by a fast, partially implicit numerical

scheme to permit economical evaluation of system transients. Recently,

the RELAP5/MOD3 code development program has been initiated to develop

a code version suitable for the analysis of all transients and

postulated accidents in PWR systems including both large and small

break LOCAs as well as the full range of operational transients.

Although the emphasis of the RELAP5/MOD3 development is on large break

LOCA, improvements to existing code models, based on the results of

assessments against small break LOCA and operational transient test

data, are also being made.

In the present assessment the RELAP5/MOD3 Version 5m5 was used.

3.2 Modeling Description

The nodalization used to simulate the BETHSY Test facility with

the RELAP5 code is shown in Fig. 2. The model is based on 261 volumes

8
connected by 272 junctions and 263 heat structures.

In the reactor vessel element (volumes 11 to 22) the volumes

corresponding to the downcomer, the lower plenum, the core, the upper

plenum, the upper head, the guide tubes, and the downcomer bypass are

defined. The core is modeled by one channel arranged in 7 hydraulic

volumes, in which only one series of heat structures is adopted to

simulate the fuel assembly.

The three loops of the BETHSY system are represented by the two

intact loops (volumes 41 to 59) and the broken loop ( volumes 31 to 39)

in an almost symmetrical way. In fact, each of the three loops present

the hot leg, the SG inlet and outlet plena, the SG U-tube channel, the

loop seal, the reactor coolant pump, the cold leg. In addition, the

pressurizer is connected to the broken loop hot leg by means of the

surge line element and the break system is connected to the broken loop

cold leg.

In the volumes representing the pressurizer vessel, an additional

heat structure is introduced to simulate the effects of the

proportional and back-up heaters.

The three steam generator secondary sides (volumes 60 to 89) are

simulated using an identical schematization. They can be subdivided

into the downcomer, the boiling section, and the steam dome. The steam

and feedwater lines are simulated by using Time Dependent Junctions

(i.e. with imposed flow rates) because they must be excluded during

the transient phase of the calculation. In fact, in the experimental

9
test, the two mentioned lines are closed in coincidence with the

reactor scram signal, few seconds after break opening, to isolate the

SG secondary side. Steam dump systems are also connected to the SG

steam dome using Time Dependent Junction in which the operational

setpoints and conditions are specified to be the same as the

experiment.

The steam generators as well as the pressurizer are provided with

two systems devoted to the control of the pressure and the liquid level

during the steady-state period and to maintain them at the specified

initial values.

The physical boundaries of the entire system, i.e., the reactor

containment and the relief and safety discharge tanks, are reproduced

by means of Time Dependent Volumes with constant internal conditions

during the calculation.

On the BETHSY loop, heat losses are compensated by electrical

trace heating, located on every component and piping of the primary

coolant system (except downcomer to upper head bypass, pumps, hot and

cold legs spool pieces), and the steam generators (except their

external downcomers). This trace heating system was compensated by

modeling the heat structure surfaces as insulated boundaries.

To allow the accumulator injection to start correspondingly to the

cold leg pressure specified in the experiment, a valve is arranged on

each of the accumulator surge lines.

The choked flow option is specified in the valve simulating the

10
break and to avoid the code calculating mass flow rates to be

inconsistent with the experimental data, the subcooled and two-phase

discharge coefficients are chosen as 0.85 and 1.0, respectively.

11
4. Base Calculations

A major safety issue in PWR design is the Loss-of-coolant

accident, in which a break in the primary coolant circuit leads to

depressurization, boiling of the coolant, consequent reduced cooling of

the reactor core, and unless remedial measures are taken, overheating

of the fuel rods. The control of LOCAs in PWR is in general considered

to be ensured by existing ECCSs and by the secondary side of the steam

generators as additional heat sink in particular for small break LOCAs.

In the present study the RELAP5/1OD3 code was used for the base

calculations and their results are shown in the figures from 3 to 68.

The calculated results for the principal events are compared with

the experimental values in Table 3. All the major phenomena observed

during the experiment were reproduced by the code.

i) Primary and Secondary Pressures

Fig. 3 and Fig. 4 show the primary and secondary pressures in

comparison with the experimental values. The code predicts well "tEi

primary and secondary pressure trend, whereas, despite a good

qualitative agreement, it highlights some differences in the behavior

of the primary and secondary depressurization in the region between

2000 and 2500 seconds due to earlier opening of steam dump systems than

experiment.

When the RCS pressure reaches the hot leg saturation pressure at

12
about 7.5 NPa boiling appears in the upper head, the upper plenum and

the hot legs. The upper head draining is complete at about 1000

seconds and the upper plenum level reaches the hot leg nozzle as shown

in Fig. 5 and Fig.6, respectively. At this time two-phase natural

circulation is settled, and the RCS pressure drops to 7.25 NPa. The

primary pressure depressurization became slower after flashing started

in the primary loop hot side. The primary pressure remained higher

than the secondary pressure all through the transient.

From 900 to 1700 seconds the mixture level in the downcomer and in

the core remains fairly constant as shown in Fig. 7. At 1770 seconds

the water level in the downflow side of the loop seal cross-over leg is

such that a manometric unbalancing is built between hot and cold legs.

This pressure difference leads to a liquid level depression in the

pressure vessel which causes the mixture level drop below the hot leg

elevation.

ii) Break Flow Rate

Fig. 8 and Fig.9 show that the break flow rate is well reproduc-d

by the code with the break discharge coefficient of 0.85 and 1.0 for

subcooled liquid and two-phase flow, respectively. However the

calculated break flow rate between 1500 and 2500 seconds leads to an

excessive mass discharge from the primary system and therefore from the

pressure vessel. This may cause faster depressurization, consequently

earlier opening of steam generator steam dump system and earlier

13
accumiulator injection compared with the test as shown in Figs. 10 to

12.

iii) SG U-tube differential Pressure

Figs. 13 to 21 show the differential pressures in SG U-tubes,

inlet plenum, upflow and downflow side. The agreement between measured

and calculated data is acceptable concerning the downflow side, but the

weak liquid holdup in the upflow side of the SG U-tubes was observed

particularly in loop 1.

iv) Loop Seal Cross-over Legs

In the experiment, loop seal clearing occurred in the cross-over

leg of the loop 2 (intact), while it occurred first in that of the loop

2 and next in that of the loop I (broken) in the present calculation as

shown in Figs. 22 to 27. The reason for this behavior are not yet

well understood. Possible geometrical discrepancies have been checked

on BETHSY : no differences in elevation larger than 1 cm were observed

between 3 loops ( loop seal + cold leg). A temperature differences as

small as 2 C between intermediate legs could result in the same 1 cm

discrepancy on the liquid level in the downflow side, and lead to

asymmetrical loop seal clearing [7]. It is particularly noticeable

that during the two other 2' cold leg break test performed on BETHSY

(Test 4.2a), loop seal clearing was observed first on the broken loop 1

then on the other intact loop 3 [8].

14
v) Core Thermal-Hydraulic Responses

The differential pressures in the core and the upper plenum are

presented in Fig. 28 and Fig. 6 respectively, in which the code

achieves a good simulation of the core level depression. One can

observe, however, that the first core uncovery and consequent recovery

occurred at about same time, whereas the second core level depression

is anticipated earlier about 100 seconds. The reason for this behavior

resides in the simultaneous occurrence of several effects. The

duration of the first core heatup, associated with loop seal clearing,

was almost identical. However it is considered that the first loop

seal clearing occurred partially in loop 2 and the faster linear

depressurization predicted by the calculation after loop seal clearing

lead to an early second core uncovery and to the anticipated vessel

mass inventory boil-off.

The core level was depressed manometrically, concurrently with the

level drop in cross-over legs, and took a minimum immediately before

the loop seal clearing started. This minimum core level was lower than

the cross-over leg liquid level which was at the bottom of the leg.

Fig. 29 and Fig. 30 show rod surface temperatures at the

average-power bundles. The core liquid level depression resulted in

rod temperature excursions starting from about 2200 seconds. The peak

cladding temperature was about 1075 K (vs. 1000 K in the experiment)

for the average-powered bundles as shown in Fig. 31. After the loop

seal clearing, the core liquid level recovered quickly and heater rods

15
were quenched.

vi) Transient Behavior of Other Variables

The transient behavior of the other variables are shown in Figs.

32 to 68. The variables, such as void fractions, flow rates, pressure

differences, and fluid temperatures in the primary and secondary loops,

etc., were in good agreement with the experiment.

However a large discrepancy occurred in the SG auxiliary feedwater

flowrate and SG mass inventory as shown in Fig. 32 and Fig. 33. The

calculated auxiliary feedwater flowrate was generally underpredicted

with large fluctuation. During the calculation the auxiliary feedwater

flowrate was controlled by the SG narrow range liquid level same as the

experiment. This discrepancy may cause the large differences in the SG

mass inventory, whereas, it didn't affect much in the primary system

transient.

After the accumulator injection into two intact loops, calculated

accumulator inject flowrate was larger than the test and this may cause

the depletion of the mass inventory in the accumulator tank bffoie

reaching the accumulator isolation set point (1.5 MPa) as shown in Fig.

11 and Fig. 12. Moreover, the requiring CPU time highly increases

(i.e., about 10 times longer than before the accumulator injection) to

proceed to the next step since the time step size is too small. The

identical problem has been occurred after the Low Pressure Safety

Injection, therefore the calculation was terminated by the user due to

16
requiring too much CPU time.

17
5. Sensitivity and Nodalization Studies

The base calculations agreed well with the test data. However the

timing order of the principal phenomena, the loop seal clearing and

refilling, and the auxiliary feedwater flowrate has to be pointed out.

5.1 Sensitivity

In Figs. 69 to 80 the results from the change of the auxiliary

feedwater control logic and of the break discharge coefficient are

represented as "CALC:AUX" and "CALC:CD1.0" respectively.

i) Auxiliary Feedwater Control Logic

In the experiment the auxiliary feedwater flowrate was controlled

by the SG narrow range liquid level. However the results from the base

calculation showed that the underprediction of the auxiliary feedwater

flowrate and large difference in SG mass inventory. Thus the auxiliaiy

feedwater control logic is now changed from the SG narrow range liquid

level into the wide range liquid level. The results shows that the

nearly identical auxiliary feedwater flowrate to the test is observed

even with relatively larger SG mass inventory than the test as shown in

Fig. 69 and Fig. 70.

18
ii) Break Flow Discharge Coefficient

In the base calculation the break discharge coefficient for the

subcooled liquid was 0.85. In order to take a look at the effects of

this coefficient the break discharge coefficient of 1.0 is used. As is

to be expected larger coefficient shown in Figs. 71 to 76 leads to an

excessive mass discharge from the primary system and this may cause

faster depressurization, earlier opening of the SG steam dump system,

and earlier accumulator injection.

As shown in Figs. 77 to 80 the occurrence of the loop seal

clearing was only on the loop 1 (broken). Therefore it may be

considered that the occurrence of the loop seal clearing is dependent

not only on the break flowrate but also on the flow resistance of the

loop seal cross-over legs which would determine the vapor flow

partition among the loops. The detailed reason for this behavior are

not jet well understood.

5.2 Nodalization

In the base calculation the loop seal clearing and refilling have

occurred as is observed'in the test, however the complete loop seal

clearing was not appeared in the intact loop 2 and the second loop seal

clearing was appeared in the broken loop. This was different from the

test which was observed in the intact loop only. Therefore the

19
nodalization may be necessary to evaluate the effectiveness of the

nodalization and to quantify their effects on the loop seal behavior.

In this calculation the number of the volumes increased twice than the

base case, particularly in the three loop seal cross-over legs. The

calculated results shows no differences in predicting the loop seal

clearing and refilling behavior. Thus it is expected from this that

the nodalization in the base calculation was sufficient to predict this

phenomena.

20
6. Run Statistics

CRAY2S/4-128 for calculation using RELAP5/HOD3 Code was used. The

size of the time step was chosen to be 10E-6 and 1OE-1 seconds at the

minimum and the maximum time step, respectively, for all calculations.

During the calculation the water property errors were occurred about at

2585 seconds. Therefore, restart calculation with reduced time step of

0.05 seconds were applied for the next 50 seconds to overcome this. It

is also noted that the required CPU time vs the transient time is

extremely increased by about 5 to 10 times just after the accumulator

injection to cold legs have started. Similar trend occurred when the

Low Pressure Safety Injections have started.

The computational efficiency is summarized in Table 4 from the major

edit for base calculations and can be obtained as follows.

Calculation Computer Time Number of Time Number of Grind Time

(CPU),sec Step (DT), Volume (N) CPU/(NiDT-)

RELAP5/11OD3 27271.3 151456 261 0.000689

21
7. Conclusions

The BETHSY Test 9.1.b has been analyzed using the RELAP5/MOD3

version 5m5 codes to assess the code's ability for a 2 inch cold leg

break LOCA, particularly for the large core uncovery and fuel heat-up,

requiring the implementation of an ultimate procedure, to improve

common understanding of PWR thermal-hydraulic response during such a

transient and to identify areas for desirable model improvements based

on comparisons between data and predictions.

The present study demonstrates the code's capability to predict,

with sufficient accuracy, the major phenomena occurring in the

depressurization transient, both from a qualitative and quantitative

point of view. In addition, it was shown that the actuation of

accumulator and LPSI resulting from RCS depressurization through SO

steam dump could be an effective means to mitigate the accident with

above initiating event.

Based on this result, analyses of the various sequences of even~s

may provide an useful information on the implementation of an ultimate

procedure for accident mitigation and be used to validate the physical

assumptions of Emergency Operating Procedures.

22
References

1. Guidelines and Procedures for the International Code Assessment and

Applications Program, NUREG-1271, April 1987.

2. U.S. Regulatory Commission Compendium of ECCS Research for Realistic

LOCA Analysis, NUREG-1230, May 1987.

3. "Appendix A RELAP5 Input Data Requirements," EG&G Idaho Inc.,1990.

4. "BETHSY General Description," Note SETh/LES/90-97, April 1990.

5. Gully, Ph. and Deruaz, R.,"BETHSY Measurement System," Note SETh/LES/

87-27, Oct. 1987.

6. Bazin, D.,"BETHSY : Data Base," Note SETh/LES/87-28, March 1988.

7. Chataing, T. and Clement, T.,"T' Cold Leg Break Without HPSI and With

Delayed Ultimate Procedure," Note SETh/LES/90-104, June 1990.

8. Bazin,P. et al,"Investigation of PWR Accident Situations at BETHSY

Facility," Nuclear Engineering and Design, Vol. 124, pp. 285-297,1990.

23
Table 1. Specified Operational Setpoints and Conditions

For BETHSY Test 9.1.b

Reactor Scram Signal

Safety Injection (SI) Signal

Core Power Trip Starts

Initiation of RC Pump Coastdown

High Pressure Charging

High Pressure Safety Injection

Main feedwater termination

Turbine Bypass Valve Closure

Auxiliary Feedwater Starts

Full Opening of 3 Steam Dumps To

Atmosphere

Accumulator Injection

( 2 Intact Loops Only)

Accumulator Termination

Low pressure Safety Injection

( 2 Intact Loops Only)

Stable RHR Operating Conditions

Prevails (Termination of Transient)

13.1 MPa

11.9 lPa

17 sec After Scram Signal

300 sec After Scram Signal

Not Actuated

Not Actuated

With SI Signal

With SI Signal

30 sec After SI Signal

At Max. Core Cladding

Temperature of 450 C

4.18 MPa

1.5 MPa

0.91 MPa

Core Outlet Temp. < 177 C

PZR Pressure < 2.5 MiPa

Saturation Margin > 20 C

24
Table 2. Comparison of Initial Conditions

Parameter Units Measured Calculated

PRIMARY LOOP

Core Differential Temperature K 3.58 3.49

= (Hot-Leg Temperature) - (Cold-Leg

Temperature)

Hot-Leg Pressure MPa 15.51 15.55

Hot-Leg Temperature K 563.3 564.8

Mass Flow Rate Per Loop kg/s 50.0 51.1

Pump Differential Pressure MPa 0.476

Pump Rotational Speed rpm 2940 2808.8

PRESSURE VESSEL

Core Power kW 2587 2587

Core Differential Pressure IPa 0.1313

Upper Head Temperature K 561.3

Lower Plenum Temperature K 561.3

Core Inlet Temperature K 559.8 561.3

PRESSURIZER

Pressure MPa 15.51 15.51

Liquid Level m 4.08 4.00

Liquid Volume m3 0.407

Vapor Volume m3 0.273

Temperature (Bottom) K 599.5

Primary System Total Mass Inventory kg 1960 1948.8

Primary System Total Volume m3 2.86

SECONDARY SYSTEM

SG Steam Dome Pressure MPa 6.91 6.91

Steam Flow Rate cm3/s 620 620

Feedwater Flow Rate cm3/s 620 620

Feedwater Temperature K 491.1 491.1

Downcomer Water Level m 13.45 13.43

Secondary Side Mass Inventory

For Each SG kg 820 820.0

Secondary Side Total Volume m3 6.0615 6.062

25
Table 2. Comparison of Initial Conditions

Parameter Units Measured Calculated

EMERGENCY CORE COOLING SYSTEM

Accumulator Pressure MPa 4.18 4.18

Accumulator Liquid Temperature K 290 290

Accumulator Liquid Volume m3 0.286 0.286

Accumulator Gas Volume m3 0.137 0.137

EXTERNAL CIRCUITS

Trace Heating kW 107.5

Pump Connected Cooling Circuits RW 25 25

26
Table 3. Chronology of Main Events

(Unit :aSecond)

IMeasured JCalcula

Transient Initiation 0 0

Scram Signal (P=13.1 KPa) 41 32

Pressurizer Empty 50 60

Safety Injection Signal Generated (P=11.9 MPa) 54 58

Main Feedwater Off 54 58

Turbine Bypass Valve Closure 54 58

Core Power Decay Starts 17 s After Scram Signal 58 49

Auxiliary Feedwater On (30 s After SI Signal) 82 88

Voiding Appears in Hot Leg 1 126 125

Pump Coastdown Starts 300 s After SI Signal 356 358

End of Pump Coastdown 971 973

Start of the First Core Uncovery 1830 1850

First Loop Seal Clearing in Loop 2 1944 1q95

Start of the Second Core Uncovery 2180 2080

Ultimate Procedure Initiation

(Max. Core Cladding Temperature Reaches 450 C) 2562 2503

27
Table 3. Chronology of Main Events

(Unit : Second)

Measured Calculated

Atmospheric Steam Dump Opening (3 SG) in 5 s 2567 2503

Loop Seal Reformation in Loop 2 2750 2525

Accumulator Injection Starts (P=4.2 MPa) 2962 2803

Minimum Primary Mass Inventory (400 kg) 2970 2805

Second Loop Seal Clearing in Loop 2 3040 2965 *

Loop Seal Reformation in Loop 2 3680 3555 *

Accumulator Isolation (P=1.5 MPa) 3831 3525

LPIS Starts at P=0.91 HPa (On Intact Loop Only) 5177 5015

End of the Test (RHRS Stable Operating

Conditions Are Reached) 8330 5245 **

* :Appeared in Loop 1 (broken)

** :Calculation terminated by user due to requiring too much CPU time

28
Table 4. Run Statistics Data in Base Case

Transient time CPU Time Attempted

(sec) (sec) ADV

0 4.4 0

500 2069.5 12478

1000 3571.2 20790

1500 5177.8 29597

2000 8102.8 45865

2500 8737.6 49511

3000 10031.5 56627

3250 10149.2 63043

3500 18521.9 103696

4000 23737.5 132438

4500 25431.3 141517

5000 27271.3 151456

29
Broken loop

CL break'

location surge line

SGI

HL break

location

ACC : accumulator

nozzle

SI : safety injection

nozzle

NS normal spray

nozzle

spool pieces

vessel

ACC S downcomer

spool /

pieces.1

\ ./

Intact loops

spool p~ieces

AC(

SI

NS

Fig. 1 General Structure of BETHSY Test Facility
15,41

r.A8-091 54 8 4

Fesdwcfe~r

45-4731Break 7688

L Loop-c 

72

Fig. 2 Nodal ization of BETHSY for RELAP5/MOD3 Code
BETHSY TEST 9.1.b (2 inch SBLOCA)

aUE

L

L

E

20

18

15

13

10

wN 7.5

5.0

2.5

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 3 Primary Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA) 10

0)

0~

4-) in

LO

(n

9.0

8.0

7.0

6.0

5.0

4.0

3.0

2.0

1.0

C.3

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 4 SG Steam Dome Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA) 10

a-

-a

(U

CL

0-

8.0

6.0

4.0

2.0

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 5 Upper Head Diff. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA) 30

X

E'

L

(D

CCL

25

20

15

10

5.0

w,

0

0 1000 2000 3000 4000 5000 6000 7000 8000

T i me (s)

Fig..6, Upper Plenum DiFf. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA)

0.

0)

0~

0

10

9.0

8.0

7.0

6.0

5.0

4.0

3.0

2.0

1.0

0

CA)

0 1000 2000 3000 4000 5000 6000 7000 8000

T i me (s)

Fig. 7 Core Collapsed Level
BETHSY TEST 9.1.b (2 inch SBLOCA)

Co

(D

L

0

3.0

2.5

2.0

1.5

1.0

0.500

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 8 Break Flowrate
BETHSY TEST 9.1.b (2 inch SBLOCA) 2500

2000

0)

x

0)

0)

Cu

1500

1000

030

500

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 9 Integrated Break Mass Flow
BETHSY TEST 9.1.b (2 inch SBLOCA)

0)

U,

C0

-P

U)

1.0

0.750

0.500 E

0.250

0

w40

LW66oa

- CALC:LI

-- CALC:L2 .... EXPT:LI

EXPT:L2

-0.250L

! S..JUU"

0 1000 2000 3000 4000 5000 6000 7000 8000

T i me (s)

Fig. 10 SG Steamline Steam Flowrate
BETHSY TEST 9.1.b (2 inch SBLOCA) 5.0

0~a_

a)

L

0

E4

E

C.

C.

4.0

3.0

2.0

1.0

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 11 Accumulator Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA)

z

fn

0

C0

4.,

0

S

U

U

400

350

300

250

200

150

100

50

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 12 Accumulator Mass
4-)

4-)

1

0D

4-n

100

BETHSY TEST 9.1.b (2 inch SBLOCA)

-CALC

EXPT

50L

41.3

0

-50

-100

-150

-200

-250

-300

"'---S.-

I' " I. - - - - - - - - - - - --

t I I I I I I

m m m i I

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 13 SG 1 U-tube Inlet-To-Outlet Oiff. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA) 10

a_

C3

C:

C-!

(I,

8.0

6.0

CA~

4.0

2.0

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 14 SG 1 Inlet Plenum DiFf. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA)

Ct,

0~

4:

0-

-0

L9

a,

250

200

150

100

50

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 15 SG 1 U-tube Upflow Side Diff. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA)

CL

0~I

0~

-0

0s

I100

50

0

-50

-100

-150

-200

-250

-300

$:,,

..Ln

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 16 SG 2 U-tube Inlet-To-Outlet DiFf. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA) 10

a_

C

a)

(MJ

LO

(I,

8.0

6.0

4.0

2.0

a)

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 17 SG 2 Inlet Plenum Diff. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA)

C',

az

aU)

-o

cn

0

(4~

0~

a,

-D

IC~~J

LD(n

250

200

150

100

50

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 18 SG 2 U-tube Upflow Side Oiff. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA)

0~

Lo

(-

100

50

0

-50

-100

-150

-200

-250

-300

0o

0 1000 2000 3000 4000 5000 6000 7000 8000

T i me (s)

Fig. 19 SG 3 U-tube Inlet-To-Outlet Diff. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA) 10

- CALC

8- EXPT

_I.io~ I "I

S ~ 1• Jrl, "

rn °, ?r',

6. i I''I,• 

Q- I•4

c -o 4 . 0"

CL

2.0 " in

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 20 SG 3 Inlet Plenum DiFF. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA)

(n

250

200

150

100

50

0

C.,

0 1000 2000 3000 .4000 5000 6000 7000 8000

T i me (s)

Fig. 21 SG 3 U-tube Upflow Side Diff. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA)

(U

0-

0~

0)

-j

40

30

20

UY

10

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time (s)

Fig. 22 Loop Seal 1 DownFlow Side DiFf. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA)

CL

0~

0-

0

0

-J

20

15

10

5.0

0

C-"

0 1000 2000 3000 4000 5000 6000 7000 8000

T i me (s)

Fig. 23 Loop Seal I Upflow Side DiFI. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA)

(n

0

C

0

(Da

0~

0

-j

40

30

20 'J1

10

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 24 Loop Seal 2 Downflow Side Diff. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA)

03

0~

0

(D

(n

0-

0I

0

0i

20

15

10

5.0

0

,-

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 25 Loop Seal 2 Upflow Side DifF. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA)

(0

M

Cl)

7.

C>

C4)

01

40

30

20

cn

L,

10

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 26 Loop Seal 3 Downflow Side DiFf. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA) 20

Cr3

CI-

(n,

CL

0

0

-J

15

10

5.0

C,.

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 27 Loop Seal 3 Upflow Side Diff. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA) 150

0~

4-,

0)

C

0)

-J

-o

U,

-4-,

(C

0)

0)

L

0

100

50

U, -:3

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 28 Core Heated Length DIFF. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA)

CL

E

(TI

0~

1100

1000

900

800

700

600

500

00

400

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 29 Heater Rod Temperatures
(2 inch SBLOCA)

BETHSY TEST 9.1.b 1100

C-

(ID

(ID

--"

"0

4-,

a)

1000

9O00

800

700

6OO

500

S,

400

1000 2000 3000

0

Time(s)

Heater Rod Temperatures Fig. 30
BETHSY TEST 9.1.b (2 inch SBLOCA)

(U

U,

E

:,

E

E

1100

1000

900

800

700

600

500

400

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 31 Maximum Clad Temperaturte
BETHSY TEST 9.1.b (2 inch SBLOCA)

0,

LL

LoC,

0.600

0.500

0.400

0.300

0.200

0.100

0

0r)

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 32 SG Feedwater Mass Flowrate
BETHSY TEST 9.1.b (2 inch SBLOCA) 1100

0) Jr

I0

C

C

1000

900

800

C,)

or)

(n

700

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 33 SG Mass Inventory
BETHSY TEST 9.1.b (2 inch SBLOCA) 1.0

0.800

0

0

0.600

0.400 C.3

0.200

0

0 1000 2000 3000 4000 5000 6000 7000 8000

T i me (s)

Fig. 34 Hot Leg 1 Void Fractions
BETHSY TEST 9.1.b (2 inch SBLOCA)

1.0

0.800

C

LL

0

0.600

c') 0.400

0.200

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

F i g. 35 Hot Leg 2 Void Fractions
BETHSY TEST 9.1.b (2 inch SBLOCA)

1.0

0.800

C0

-o0-

0

0.600

0.400

M,

0.200

0

0 1000 2000 3000 4000 5000 6000 7000 8000

T ime(s)

Fig. 36 Hot Leg 3 Void Fractions
BETHSY TEST 9.1.b (2 inch SBLOCA)

1.0

0.800

C:0

0.600

0.400

C")

0.200

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig.37 Cold Leg 1 Void Fractions
BETHSY TEST 9.1.b (2 inch SBLOCA) 1.0

0.800

L

0

4-,

0

0.600

0.400 -'4

0.200

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 38 Cold Leg 2 Void Fractions
BETHSY TEST 9.1.b (2 inch SBLOCA)

1.0

0.800

C

0

04-

~0

"0

0.600

00 0.400

00

0.200

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time (s)

Fig. 39 Cold Leg 3 Void Fractions
BETHSY TEST 9.1.b (2 inch SBLOCA)

CL

al)

-0

ED

30

25

20

15

10

5.0

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 40 Guide Tube 0iff . Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA) 150

0-

-1

0~

(0

a,

L

U,

0~

0

IL

U,

S

0

U

C

0

In

100

K - CALC

EXPT

50 L

0 1' I I . I I I : I

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 41 Oowncomer-To-Upper Head Diff. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA) 200

aQ)

150

100

50

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig.42 Pressure Vessel DIff. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA)

0~

0

0.

U,

200

150

100

50

0

-50

-100

- CALC

3⁄4

!I -- CALC

-" EXPT

i -

I I I I I I I

I I I I

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 43 Cold Leg 1 To Hot Leg 1 DiFf. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA) 100

-CALC

EXPT

0L -- - - - - -- - - - -

r

CL

E

0-

-100

-200

-300 C'3

-400

-500

1'

-1 I I I I t t t

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. '44 Pump I Diff. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA)

0M

0~

xr

0~

_0

0

U)

200

150

100

50

0

-50

-100

0 1000 2000 3000 4000 5000 6000 7000 8000

T i me (s)

Fig. 45 Cold Leg 2 To Hot Leg 2 0IFf. Pressure
100

BETHSY TEST 9.1.b (2 inch SBLOCA)

-- CALC

EXPT

0 1 -am - - -*-

(0 I

CL

-100 L

-200

Cal

0..

-300

-400

-500 j I I I I I I I

0 1000 2000 3000 4000 5000 6000 7000 8000

T i me (s)

Fig. 46 Pump,2 DiFf. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA)

4-)

0~

0)

U)

200

150

100

50

0

-50

-100

-,)

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 47 Cold Leg 3 To Hot Leg 3 DiFf. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA)

100

0

SCALC

EXPT

-1-- 11 ----------------

fC.

CL

C3

M

CL

EL ".4

-100

-200

-300

-400

-500

1~

j I II I I I I

0 1000 2000 3000 4000 5000 6000 7000 8000

T i me (s)

Fig. 48 Pump 3 Diff. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA)

20

Ct,

C:

0

C.)

c,

f0

m

L9

Zn

15

10

5.0

-,400

0

0 1000 2000 3000' 4000 5000 6000 7000 8000

Time(s)

Fig. 49 SG 1 Boiler Section DiFF. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA) 20

CL

CL

f-a

LD

ZC

15

10

5.0

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 50 SG 2 Bolier Section DiFf. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA)

0~

z

0~

c

0

4.,

C.,

U,

U,

L

a,

0

to

rr,

tn

30

25

20

15

10

5.0

00

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 51 SG 3 Bolier Section DIFF. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA)

IL

30

25

20

15

10

00

5.0

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 52 Pressurizer Di•f. Pressure
BETHSY TEST 9.1.b (2 inch-SBLOCA)

1.0

0,

N

0)

z

0)

-I-,

Co

C0

IL

0,

0,

Co

-4

U,

a-

-J

0.800

0.600

0.400

0.200

00

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 53 LPSI Mass Flowrate
BETHSY TEST 9.1.b (2 inch SBLOCA)

000

Wz

4000

3500

3000

2500

2000

1500

1000

500

0

K -- CALC -- EXPT

/

/

I

/

I

I

I

/

I

1

I

I

I

I

I

I

I

/

J.

I I

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 54 Integrated LPSI Mass Flow
BETHSY TEST 9.1.b (2 inch SBLOCA) 16

14

12

(0

0)

CL

10

8.0

6.0

00

4.0

2.0

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 55 Primary and Secondary Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA) 200

0)

N%

0,

0)

150

100

50

0O

U,

0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 56 Mass Flow Rate
BETHSY TEST 9.1.b (2 inch SBLOCA)

700

600

CL

E

a,

500

00Cm)

400

300

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 57 Core Inlet & Outlet Tempertures
BETHSY TEST 9.1.b (2 inch SBLOCA) 600

a)

CL

E()

700

600

00"-

500

400

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 58 Upper Head Temperatures
BETHSY TEST 9.1.b (2 inch SBLOCA) 800

0,

C700

600

500

0000

400

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 59 Loop 1 Temperature
BETHSY TEST 9.1.b (2 inch SBLOCA) 800

700

4-,

a)1

CkQ)

600

C0 500

400

300

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 60 Loop 2 Temperature
BETHSY TEST 9.1.b (2 inch SBLOCA) 800

700

z

a,

L

-4-,

L

a,

0~.

5

a,

I600

500

to

400

300

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 61 Loop 3 Temperature
BETHSY TEST 9.1.b (2 inch SBLOCA)

800

W

CL

E

700

600

'-A

500

400

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 62 Bottom SG Downcomer Temperature
BETHSY TEST 9.1.b (2 inch SBLOCA)

0-

0)

0~

0-

-Ia:

3000

2500

2000

1500

1000

500

CALC:P1

EXPT:P1

I

tNO

0 I I I

0 1000 2000 3000 4000 5000 6000 7000 8000

T i me (s)

Fig. 63 RCP Rotational Speed
BETHSY TEST 9.1.b (2 inch SBLOCA) 3000

2500

CL)

2000

1500

1000

Co

500

0

1000 2000. 3000 4000 5000 6000 7000 6000

T i me (s)

F ig.- 64 Core Power
BETHSY TEST 9.1.b (2 inch SBLOCA) O. 500

0.400

0.300

Q)

.E 0.200

0.100

0 1000 2000 3000 4000 5000 6000 700

Time(s)

0 8000

Fig. 65 Time Step
BETHSY TEST 9.1.b (2 inch SBLOCA) 5.0

I- CALC

-J

L

a)

N

L

aI)

4.0

3.0

2.0

1.0

to

(.11

0 I I I I I I I

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 66 Pressurizer Level
BETHSY TEST 9.1.b (2 inch SBLOCA)

(0

S

a,

a,

-J

C,)

15

14

13

12

11

10

9.0

0 1000 2000 3000 4000 5000 6000 7000 8000

Time(s)

Fig. 67 SG 1 Wide Range Level
BETHSY TEST 9.1.b (2 inch SBLOCA)

4-)

C

i-n

(a

CL

2000

1500

1000

500

0

0 1000 2000 3000 4000 5000 6000 7000 8000

T i me (s)

Fig. 68 Primary Side Mass Inventory
BETHSY TEST 9.1.b (2 inch SBLOCA)

4-)

0

LL

000

cnn

0.600

0.500

0.400

0.300

0.200

0.100

0

4000

Time(s)

Fig. 69 SG Feedwater Mass Flowrate
BETHSY TEST 9.1.b (2 inch SBLOCA) 1100

0)

0

43

0)

LD

(n,

1000

900

800

700

to

600

0 500 1000 1500 2000 2500 3000 3500 4000

Time(s)

Fig. 70 SG Mass Inventory
BETHSY TEST 9.1.b (2 inch SBLOCA) 3.0

'-I

',O

0')

a0

a)

L

c...

2.5

2.0

1.5

1.0

0.500

0

0 500 1000 1500 2000 2500 3000 3500 4000

T i me (s)

Fig. 71 Break Flowrate
BETHSY TEST 9.1.b (2 inch SBLOCA) 2500

2000

I-A

0)

z

0,

0,

1500

1000

500

0

0 500 1000 1500 2000 2500 3000 3500 4000

Time(s)

Fig. 72 Integrated Break Mass Flow
BETHSY TEST 9.1.b (2 inch SBLOCA) 16

14

c~3

0~

L

(5)

L

0~

L

E

C0~

12

10

8.0

6.0

4.0

2.0

0

0 500 1000 1500 2000 2500 3000 3500 4000

Time(s)

Fig. 73 Primary Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA)

d)

E

0

-0

En

0

C

(n)

Lu

E)

1.0

0.

0.

0.250

0

-0.251

-0

0 500 1000 1500 2000 2500 3000 3500 4000

Time(s)

Fig. 74 SG Steami ne Steam Flowrate
BETHSY TEST 9.1.b (2 inch SBLOCA)

1100 - CALC:BASE -- -. EXPT -d 1000 ... CALC:CDI.0

: CALC:AUX

8900

800(

_ /

Soo' -o 700 ,

2 600 ,

2 I.

(0 500 ... .. . -,.

400

0 500 1000 1500 2000 2500 3000 3500 4000

Time(s)

Fig. 75 Maximum Clad Temperaturte
BETHSY TEST 9.1 .b (2 inch SBLOCA) 8.0

2

0,

Lj

7.0

6.0

5.0

4.0

3.0

2.0

1.0

'-a

Cal

0

0 500 1000 1"500 2000 2500 3000 3500 4000

Time(s)

Fig. 76 Core Collapsed Level
BETHSY TEST 9.1.b (2 inch SBLOCA)

I-i

0)

CL

0~

0

Cl

0

0

0

-J

30

20

40

10

0

0 500 1000 1500 2000 2500

Time(s)

3000 3500 4000

Fig. 77 Loop Seal I Downflow Side DIFf. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA)

(0

(4-

0

I20

15'

10

5.0

0

0 500 1000 1500 2000 2500 3000 3500 4000

T i me (s)

Fig. 78 Loop Seal I Upflow Side Di£f. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA)

00

Aý

a)

_0

Ci0

X

0-.

0

0

-j

30

20

40

10

0

0 500 1000 1500 2000 2500 3000 3500 4000

Time(s)

Fig..79 Loop Seal 2 Oownflow Side DiFf. Pressure
BETHSY TEST 9.1.b (2 inch SBLOCA)

3.

(0

0~

0-

0

0~

1

20

15

10

5.0

0

0 500 1000 1500 2000 2500 3000 3500 4000

Time(s)

Fig. 80 Loop Seal 2 Upflow Side DifIf. Pressure

Appendix
* This contains a RELAP5 model of the French experimental facility *

* BETHSY. The intended use of the model is for simulation of BETHSY *

* test 9.1.b which studies the 2 inch cold leg break without hpsi *

* and with delayed ultimate procedure. *

= 2 inch cold leg break bethsy test 9.1.b

100 new stdy-st

101 run

102 si si

105 2. 4.

110 nitrogen

115 1.0

120 13010000 0.0 water primary

121 60010000 7.1057 water secndry

122 70010000 7.1057 water seclopb

123 80010000 7.1057 water seclopc

201 500.0 1.e-6 0.05 3 20 2000 2000

* minor edit variables

301 p 091050000

302 p 068010000

303 p 078010000

304 p 088010000

305 p 034010000

306 p 034220000

307 p 044010000

308 p 044220000

309 p 054010000

310 p 054220000

314 tempf 031010000

315 tempf 039010000

316 tempf 041010000

317 tempf 049010000

318 tempf 051010000

319 tempf 059010000

323 mflowj 012010000

324 mflowj 099010000

325 mflowj 301000000

326 mflowj 401000000

110
327 mflowj 501000000

328 mflowj 039010000

329 mflowj 049010000

330 mflowj 059010000

331 mflowj 608000000

332 mflowj 708000000

333 mflowj 808000000

337 pmpvel 36

338 pmphead 36

339 cntrlvar 424

340 cntrlvar 425

341 cntrlvar 1

342 cntrlvar 4

343 cntrlvar 159

344 cntrlvar 199

345 cntrlvar 319

346 cntrlvar 2

347 cntrlvar 22

348 cntrlvar 330

349 mflowj 601000000

350 mflowj 606000000

351 cntrlvar 266

* self initialization controller cards

140 0 3 3

143 606 266 706 276 806 286

145 601 263 701 273 801 283

* trips

407 time 0 it null 0 99999. n 0.

507 time 0 it null 0 10000.0 1

* hydradynamic components

*lower plenum components

, component 11 - lower portion of lower plenum

111
0110000

0110001

0110101

0110200

0111101

0112101

0111110

0112110

0111201

0112201

lowerpl branch

2 0

0.0 1.00 0.15323 0.(

003 15745056. 559.8

022010000 011000000 0.0

011000000 012000000 0.0

.045 0. 1.

.01587 0. 1.

7.480417 7.590417 0. , ]

3.364479 3.4044795 0. ,

) -90. -1.0w

0.0

0.01.

1.

[0.43635

10.43636

0 4.57e-5 .0.039...00100

0.0 01100

0.0 01100

* component 12 - upper portion of lower plenum

0120000

0120001

0120101

0120200

0121101

0122101

0121110

0122110

0121201

0122201

upperlp branch

2 0

0.0 1.054 0.0620907

003 15737400. 559.8

012010000 013000000

012010000 014000000

.01130 0.

.004 0.

4.161302 4.221302 0.

1.41488 1.64488 0.

0.0 90. 1.054 4.57e-5 0.01543

.0428 1.5 1.5 01100

0.0 13.5 13.5 01000

1. 1.

1. 1.

* 10.06651

* .3698466

00100

*core and core bypass components

* component 13 - core

0130000

0130001

0130101

0130101

0130103

0130201

0130301

0130302

0130303

0130304

0130305

0130306

core pipe

7

0.0 1

0.0428 6

0.0 7

0.0 6

0.11 1

0.788 2

0.78 3

0.52 4

0.78 5

0.788 6

*volume areas

*junction areas

*volume length

112
0130307

0130401

0130402

0130403

0130601

0130701

0130702

0130703

0130704

0130705

0130706

0130707

0130801

0130802

0130803

0130901

0131001

0131101

0131201

0131202

0131203

0131204

0131205

0131206

0131207

0131300

0131301

0131302

0131303

0131304

0131305

0131306

0131401

0.35

0.004708

0.0

0.018066

90.0

.11

.788

.78

.52

.78

.788

.35

4.57e-5

4.57e-5

4.57e-5

.31

00100

01000

003 ]

003 1

003 1

003 1

003 ]

003 1

003 1

0

4.161303

4.173902

4.189569

4.194801

4.201244

4.214391

.0113

7 1

6

7

7

1

2

3

4

5

6

7

.01130

.01130

.06584

.31

*volume volume

*vert angle

*delta z

1

6

7

*roughness diam

7

6

[5712976.

[5699616.

[5673800.

[5659048.

.5644392.

.5618848.

.5604872.

4.191303

4.193902

4.209569

4.204801

4.201244

4.214391

0.

6 *junction loss coef

*volume flags pvbfe

*junction flags vcahs

* 559.8 0. 0. 0. 1

.560.2 0. 0. 0. 2

561.1 0. 0. 0. 3

562.0 0. 0. 0. 4

562.5 0. 0. 0. 5

563.0 0. 0. 0. 6

* 563.3 0. 0. 0. 7

;4ý40.

0.

0.

0.

0.

0.

1.

1

2

3

4

5

6

*

*

*

*

*

*

10.06651

10.0665

10.0665

1.0.0665

10.0665

10.06651

1. 6

* component 14 - core bypass

0140000

0140001

0140101

0140201

0140301

0140302

0140303

0140304

0140305

0140306

cbypass pipe

7

1.421e-2

0.0 6

0.11 1

0.788

0.78

0.52 4

0.78 , 0.788

7 *volume areas

*junction areas

*volume length

.5

113
0140307

0140401

0140601

0140701

0140702

0140703

0140704

0140705

0140706

0140707

0140801

0140901

0140901

0141001

0141101

0141201

0141202

0141203

0141204

0141205

0141206

0141207

0141300

0141301

0141302

0141303

0141304

0141305

0141306

0141401

0.35

0.0

90.0

.11

.788

.78

.52

.78

.788

.35

4.57e-5

1.072

16.0

00000

01000

003

003

003

003

003

003

003

0

1.4149

1.4104e

1. 4172M

1.4153]

1.4164.

0. 5013M .02

77 *

7 *

1 *

2

3

4

5

6

7

.0247

1.072

16.0

7

6

15723096.

15709768.

15683984.

15669224.

15654520.

15638920.

15614888.

olume volume

vert angle

delta z

7

6

6

56(

560

561

561

562

562

*roughness diam

*junction loss coef

*junction loss coef

*volume flags pvbfe

*junction flags vcahs

.8 0.0 0.

).1 0.0 0.

1.5 0.0 0.

.0 0.0 0.

-.5 0.0 0.

.0 0. 0. 0

.5 0.0 0.

0. 1

0. 2

0. 3

0. 4

0. 5

.6

0. 7

1.4038

1.41076

1.44268

1.47611

1.40702

0.590595

0.

0. 1

0. 2

0. 3

0. 4

0. 5

0. 6

1.

*

*

*

*

*

*

.3698466

.369632

.369634

.369634

.3696346

.369635

1. 6

*upper plenum components

* component 99 upper plenum 1

0990000

0990001

0990101

0990200

0991101

0992101

0993101

0994101

0991201

0992201

upplenl branch

4 0

0.0 0.5525 5.0302e-2

003 15600120. 563.

014010000 099000000

013010000 099000000

099010000 015000000

099010000 017000000

1.41158 1.585256 0.

3.49723 3.54723 0.

0.0 90. 0.5525 4.57e-5 .2380 00000

0.0 13.5 13.5 01000

0.0 1.5 1.5 01100

0.0 0.0 0.0 01000

0.0 0.92 .998 01000

.3696344

* 10.06651

114
0993201

0994201

0991110

0992110

0993110

0994110

2.344489

1.582433

.004

.238

.2081

.0603

2.559943 0.

1.582433

0. 1.

0. 1.

0. 1.

0. 1.

* 10.18996

0. * .246178

1.

1.

1.

* component 15 upper plenum 2

0150000

0150001

0150101

0150200

0151101

0152101

0153101

0154101

0151201

0152201

0153201

0154201

0151110

0152110

0153110

0154110

upplen2 branch

4 0

0.0 1.051 .091564 0.0 90.

003 15596200. 563.3

015010000 016000000 0.08706

015010000 031000000 0.010936

015010000 041000000 0.010936

015010000 051000000 0.010936

-0.8027-4 -0.10387-4 0. *

1.051 4.57e-5 .182 00000

0.0 0.0

.46 .834

.46 .834

.46 .834 -. 002072645

01000

01002

01002

01002

6.171221

6.261221

6.261221

.2081

.118

.118

.118

6.541802 0. *

6.641802 O. *

6.641802 O. *

0. 1. 1.

0. 1. 1.

0. 1. 1.

0. 1. 1.

3.39708

3.39708

3.39708

* component 16 - flow area from upper plenum to upper head

0160000

0160101

0160200

upplen2 snglvol

0.0 2.206 .11263

003 15586312. 563.0

0.0 90.0 2.206 4.57e-5 .129 000000

* component 17 - guide tubes

0170000

0170101

0170200

gtubes snglvol

.00 3.257 9.0671e-3 0.0 90. 3.257 4.57e-5 .0603 00000

003 15586824. 563.0

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

* component 18 - upper head

0180000 uphead branch

115
0180001

0180101

0180200

0181101

0182101

0183101

0181201

0182201

0183201

0181110

0182110

0183110

3 0

0.0 0.4475 4.9072e-2 0.0 90.0

003 15595592. 563.0

0.4475 4.57e-5 0.0 00000

016010000

017010000

018000000

-5.4422-4

-6.05085

-0.0639743

.003 0.

.0203 0.

.170 0.

018000000

018000000

019000000

-5.5422-

-6.05085

-0.0763554

7.0686e-6

7.063e-4

0.0

-4 0. *

0. *

0. *

0.0 0.0

0.92 .998

0.0 0.0 -. 00201577

.246176

2439847

01100

01000

01100

1. 1.

1. 1.

1. 1.

* component 19 - upper head to downcomer bypass

0190000

0190101

0190200

dcbypas snglvol

0.0 1.37786 8.9259e-2

003 15591856. 560.0

0.0 -90. -1.37786 4.57e-5 .135 00000

* component 200 - junction to downcomer bypass

2000000 dcbyjun sngljun

2000101 019010000 021000000 2.454e-4 1.15 1.15 01000

2000201 0 -17.334Z -44.0342 0. * .243605

2000110 6.25e-3 0. 1. 1.

* component 21 - downcomer bypass

0210000

0210001

0210101

0210201

0210301

0210302

0210303

0210401

0210402

0210403

0210601

0210602

0210603

0210701

dcbypas pipe

3

0.0 3

0.0 2

1.7614 1

1.142635 2

0.2095 3

3.7831e-3 1

2.4414e-3 2

0.9697e-3 3

-18.2 1

-21.6 2

-90.0 3

-. 55049 1

*nvol

*volume area

*jun area

*volume length

*volume volume

*vert angle

*delta z

116
0210702

0210703

0210801

0210901

0210902

0211001

0211101

0211201

0211202

0211203

0211300

0211301

0211302

0211401

-. 42005 -. 2095

4.57e-5

0.1

0.0

00000 3

01000 2

003 152

003 152

003 152

0

-2.023346

-2.02334

.0492

2

3

0.0 0.1

0.0

730808

741144

743320

3 *roughness diam

1 *junction f-loss 2 *volume flags

*junction vcahs

560.0 0.0 0.

560.0 0.0 0.

560.0 0.0 0.

r-loss

0.

0.

0.

1

2

3

-2.02334(

-2.02334

0. 1.

3 0.1*

0. 2*

1. 2

.24359

.2435797

* component 20 - downcomer inlet

0200000 0200001

0200101

0200200

0201101

0202101

0203101

0204101

0205101

0201201

0202201

0203201

0204201

0205201

0201110

0202110

0203110

0204110

0205110

dcinlet branch

5 0

0.0 0.927 .0433233 0.0 -90. -0.927 4.57e-5 0.0 00000

003 15757472. 560.

021010000 020000000 0.0 0.0 0.0 01100

039010000 020000000 1.0936e-2 .834 .46 01001

049010000 020000000 1.0936e-2 .834 .46 01001

059010000 020000000 1.0936e-2 .834 .46 01001

020010000- 022000000 0.0 0.10 0.10 01100

-0.93435 -0.934447 0. * .243576

6.510582 6.810582 0. * 3.397646

6.510582 6.810582 0. * 3.397646

6.510582 6.810582 0. * 3.397646

8.442823 8.862246 0. * 10.43632

0.0 0. 1. 1.

.118 0. 1. 1.

.118 0. 1. 1.

.118 0. 1. 1.

.1731 0. 1. 1.

* component 22 - downcomer

0220000

0220001

0220101

0220201

dcomer

7

0.0

0.0

pipe

7

6

*=nvol

,*volume area

*junction area

0220301 1.011625 4 *volume length

117
0220302

0220303

0220304

0220401

0220402

0220403

0220404

0220601

0220602

0220603

0220604

0220701

0220702

0220703

0220704

0220801

0220802

0220901

0220902

0220903

0220904

0221001

0221101

0221201

0221202

0221203

0221204

0221205

0221206

0221207

0221300

0221301

0221302

0221303

0221304

0221305

0221306

0221401

0221402

.31919

.4602

1.054

23.9771e-3

7.5115e-3

10.8295e-3

27.9758e-3

-90.0 4

-55.8 5

-46.0 6

-90.0 7

-1.011625 4 -. 26396 5 -. 33003 6

-0.85412 7

4.57e-5

4.57e-5

0.0 0.0

.054 .054

.017 .017

.285 .285

00000 7

01000 6

003 15•

003 15,

003 15•

003 15'

003 15'

003 15,

003 15'

5

6

7

4

5

6

7

*volume volumes

*vertical angles

*delta z

.1731 6 *r(

4.5e-2 7

3 *junction f4 *junction f5 *junction f6 *junction f-

*volume I

*junction

720472. 560.0

725952. 560.0

W30440. 560.0

735920. 560.0

737624. 560.0

p38816. 560.0

735168. 560.0

)ughness diam

77

7

7

7

7

7

-loss i

-loss , -loss i

-loss , flags

vcahs

0.0

0.0

0.0

0.0

0.0

0.0

0.0

--loss

--loss

r-loss

--loss

0.

0.

0.

0.

0.

0.

0.

0. 1

0. 2

0. 3

0. 4

0. 5

0. 6

0. 7

0

8.382818 8.764339 0.

8.382813 8.764312 0.

8.382808 8.764285 0.

8.436977 8.768767 0.

8.436996 8.758048 0.

8.436994 8.786994 0.

.1731 0. 1.

4.5e-2 0. 1.

1

2

3

4

5

6

1.

1.

5

6

10.43633

10.43633

10.43633

10.43634

10.43634

10.43635

* primary loop piping components single loop-a

* component 31 - single loop (loop a) hot leg

118
0310000

0310101

0310200

hotlgal snglvol

1.0936e-2 1.1941

003 15576088.

0.0 0.0 0.0 0.0 4.57e-5 .118 00000

563.3

-component 32 - pressure surge line nozzle in single loop

0320000

0320001

0320101

0320200

hotlga2 branch

0 1

1.0936e-2 0.5

003 15576080.

0.0 0.0 0.0 0.0

563.3

4.57e-5 .118 00000

* component 33 - single loop hot leg to sg

0330000 hotlga3 pipe

0330001 3

0330101 1.0936e-2 3 *volume area

0330201 1.0936e-2 2 *junction area

0330301 0.79775 1 *volume length

0330302 1.44800 2

0330303 0.5506 3

0330401 0.0 3 *volume volumes

0330601 0.0 1 *vert angle

0330602 90. 2

0330603 50. 3

0330701 0.0 1 *delta z

0330702 1.44800 2

0330703 0.4637 3

0330801 4.57e-5 .118 3 *rough diam

0330901 0.117 0.117 1 *junction f-loss r-loss

0330902 0.065 0.065 2 *junction f-loss r-loss

0331001 00000 3 * vol flags

0331101 01000 2 * vcahs

0331201 003 15636072. 563.3 0.0 0. 0. 1

0331202 003 15651056. 563.3 0.0 0. 0. 2

0331203 003 15654440. 563.3 0.0 0. 0. 3

0331300 0

0331301 6.28299 6.41299 0. 1 * 3.397625

0331302 6.26303 6.54904 0. 2 * 3.39762

0331401 .118 0. 1. 1. 2

* component 301 - h.1. junction to pressurizer surge nozzle

119
3010000

3010101

3010201

3010110

hotlg4a sngljun

031010000 032000000 0.0

0 6.17222 6.25222 0.

.118 0. 1. 1.

0.0 0.0 01000

* 3.39708

* component 302 - h.l. junction from pressurizer surge nozzle

3020000 hotlg5a sngljun

3020101 032010000 033000000 0.0 0.0 0.0 01000

3020201 0 6.262985 6.342985 0. * 3.39763

3020110 .118 0. 1. 1.

* component 303 - junction from surge line to h.1. nozzle (tripvalve)

3030000 prsurgj sngljun

3030101 032010000 090000000 0.0 0.0 0.0. 01000

3030201 0 -0.83763-4 -1.29763-4 0. * -5.45044-4

3030110 .0429 0. 1. 1.

* component 35 - single loop cold leg pump suction piping

0350000 pumpsa

0350001

0350101 0.0

0350201 1.0931

0350301 0.418w

0350302 1.9401

0350303 2.22M

0350304 0.820

0350305 2.069'

0350401 4.5811

0350402 21.217•

0350403 24.3091

0350404 8.9671

0350405 22.634M

0350601 -50.0(

0350602 -90.

0350603 0.0

0350604 90.

0350701 -. 340•

0350702 -1.94(

0350703 -2.12(

0350704 0.0

pipe

5

3e-2 9

1585

7

Oe-3

5e-3

5e-3

Oe-3

Oe-3 0

4

015

015

5

4

1

2

3

4

5

1

2

3

4

5

1

3

4

5

1

2

3

4

*volume areas

*junction areas

*volume lengths

*vertical angle

*delta z

120
0350705

0350801

0350901

0350902

0350903

0350904

0351001

0351101

0351201

0351202

0351203

0351204

0351205

0351300

0351301

0351302

0351303

0351304

0351401

1.967:

4.57e-

.065

0.0

.117

.117

00000

01000

003

003

003

003

003

0

6.2058

6.2058

6.2057

6.2057

.118

1 5

-5 0.0

.065

0.0

.117

.117

5

4

15284064.

15292512.

15307552.

15305400.

15298072.

36 6.3719

32 6.4618

75 6.4714

'16 6.3457

0.

5 *volume roughnes diam

1 *f-loss r-loss

2 *f-loss r-loss

3

4

* volume flags

*junction vcahs

560.0 0.0 0.

560.0 0.0 0.

560.0 0.0 0.

560.0 0.0 0.

560.0 0.0 0.

0. 1

0. 2

0. 3

0. 4

0. 5

I5

'55

6

'16

1.

0. 1

0. 2

0. 3

0. 4

1.

*

*

*

*

4

3.3976

3.397604

3.39761

3.397614

* component 37 - single loop pump discharge piping

0370000 cldlgal pipe

0370001 2

0370101 1.0936e-2 2 *volume areas

0370201 1.0936e-2 1 *juntion areas

0370301 1.05 1 *volume lengths

0370302 0.859 2 *volume lengths

0370401 0.0 2 *volume volumes

0370501 0.0 2 *horiz angle

0370601 0.0 2 *vertical angle

0370701 0.0 2 *delta z

0370801 4.57e-5 0.0 2 *roughness diam

0370901 0.0 0.0 1 *junction f-loss r-loss

0371001 00 2 *volume fe

0371101 01000 1 *junction vcahs

0371201 003 15757504. 560.0 0.0 0. 0. 1

0371202 003 15757496. 560.0 0.0 0. 0. 2

0371300 0

0371301 6.185816 6.275816 0. 1 * 3.39763

0371401 .118 0. 1. 1. 1

* component 38 - single loop accumulator nozzle

121
0380000

0380001

0380101

0380200

0381101

0382101

0381201

0382201

0381110

0382110

accnoza branch

2 0

1.0936e-2 0.5 0.0 0.0 0.0 0.0 4.57e-5 .118 00000

003 15757488. 560.0

037010000 038000000 1.0936e-2 0.0 0.0 01000

038010000 039000000 1.0936e-2 0.0 0.0 01000

6.18582 6.26582 0. * 3.397636

6.18582 6.26582 0. * 3.39764

.118 0. 1. 1.

.118 0. 1. 1.

* component 39 - single loop cold leg piping

0390O00

0390001

0390101

0390101

0390301

0390302

0390401

0390601

0390701

0390801

0390901

0391001

0391101

0391201

0391202

0391300

0391301

0391401

cldlga2 pipe

2

1.0936e-2 2

1.0936e-2 1

.78406 1

.53586 2

0.0 2

0.0 2

0.0 2

4.57e-5 0.0

.144 .144 1

00000 2

01000 1

003 15757480.

003 15747464.

0

6.17582 6.3158:

.118 0.

*volume areas

*junction areas

*volume lengths

*=volume volumes

*vertical angle

*delta z

2 *roughness diam

*junction f-loss

*volume flags

*junction vcahs

560.0 0.0 0.

560.0 0.0 0.

2 0. 1 * 3.39764

1. 1. 1

r-loss

0. 1

0. 2

* component 36 - inlet portion of single loop pump

0360000 pumpa pump

0360101 0.0 0.350 0.02062 0.0

0360108 035010000 1.0936e-2 0.0

0360109 037000000 1.0936e-2 0.0

0360200 003 15534160. 560.0

0360201 0 6.20575 5.60145 0.

0360202 0 6.23 6.51 0.

0360110 .118 0. 1. 1.

0360111 .118 0. 1. 1.

41.518 0.232 00000

0.0 01000

0.0 01000

* 3.39762

* 3.397625

0360301 0 0 0 -1 0 000 0

122
0360302 311. 0.9899 6.3056e-2 78.0 144.75 37.3 750.0 0. 0. 4.65e-2 0. 0

* bethsy pump single phase homologous curves *

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

• hatn

0361100 1 1

0361101

0361102

0361103

. ban

0361200 2 1

0361201

0361202

0361203

• hvn

0361300 1 2

0361301

0361302

0361303

• bvn

0361400 2 2

0361401

0361402

0361403

* had

0361500 1 3

• bad

0361600 2 3

• hvd

0361700 1 4

0361701

0361702

0361703

• bvd

0361800 2 4

• hat

0361900 1 5

• bat

0362000 2 5

• hvt

0362100 1 6

0362101

0362102

0362103

• bvt

0362200 2 6

0.0

0.5

0.8

0.925

0.0

0.5

0.8

0.925

0.0

0.5

0.8

0.925

0.0

0.5

0.8

0.925

-1.

-1.

-1.0

-. 500

-. 225 -. 100

-1.0

0.0

0.0

.0

.125

.250

.600

0.0

1.3257 0.1 1.3317

1.2603 0.6 1.2223

1.1279 0.825 1.1146

1.0583 0.95 1.0437

0.5139 0.1 0.5633

0.7610 0.6 0.8105

0.9093 0.825 0.9216

0.9710 0.95 0.9834

-0.5772 0.1 -0.4471

0.0733 0.6 0.2035

0.5450 0.825 0.5969

0.8238 0.95 0.8852

-0.5772 0.1 -0.4145

0.2362 0.6 0.3989

0.7243 0.825 0.7579

0.8972 0.95 0.9333

1.3257 0.0 1.3257

0.5139 0.0 0.5139

1.3257 -. 900 1.2801

1.0978 -. 400 1.0522

0.9725 -. 200 0.9611

0.9156 -. 075 0.9042

0.5139 0.00 0.5139

1.3257 1.00 1.3257

0.5139 1.00 0.5139

0.2 1.3273 0.3 1.3135

0.7 1.1780 0.75 1.1536

0.85 1.1009 0.875 1.0870

0.975 1.0287 0.987 1.0215

0.2 0.6128 0.3 0.6622

0.7 0.8599 0.75 0.8846

0.85 0.9340 0.875 0.9463

0.975 0.9957 0.987 1.0017

0.2 -0.3169 0.3 -0.1868

0.7 0.3572 0.75 0.4471

0.85 0.6508 0.875 0.7066

0.975 0.9485 0.987 0.9795

0.2 -0.2518 0.3 -0.0891

0.7 0.5616 0.75 0.6429

0.85 0.7915 0.875 0.8263

0.975 0.9707 0.987 0.9886

-. 800 I.2346 -. 700 1.1889 -. 300 1.0067 -. 275 0.9953 -. 175 0.9497 -. 150 0.9383 -. 050 0.8928 -.025 0.8814

0.4 1.2909

0.775 1.1409

0.9 1.0728

1.0 1.0135

0.4 0.7116

0.775 0.8969

0.9 0.9587

1.0 1.0081

0.4 -0.0567

0.775 0.4951

0.9 0.7643

1.0 1.0135

0.4 0.0735

0.775 0.6836

0.9 0.8611

1.0 1.0081

-. 600 1.1434 -. 250 0.9839 -. 125 0.9269

0.00 0.8700

0.8700

0.9269

0.9839

1.1434

0.5139

.025 0.8814 '050 0.8928 .075 0.9042 .100 0.9156

.150 0.9383 .175 0.9497 .200 0.9611 .225 0.9725

.275 0.9953 .300 1.0067 .400 1.0522 .500 1.0978

.700 1.1889 .800 1.2346 .900 1.2801 1.00 1.3257

1.000 0.5139 --

123
*

*

*

*

*

the following four curves were not provided in the bethsy data base

the values used were estimated from the relap5/mod2 manual examples

* har

0362300 1 7

* bar

0362400 2 7

* hvr

0362500 1 8

* bvr

0362600 2 8

-1.0 0.1

-1.0 -1.5

-1.0 0.1

-1.0 -1.5

0.0 1.3257

0.0 .5139

0.0 -. 5772

0.0 -. 5772

0363000 0 0.0 0.0 0.1 0.0 0.2 0.0 0.3 0.50

0363001 0.4 1.00 0.6 1.0 0.7 1.0 0.8 1.00

0363002 0.9 1.00 1.0 0.0

0363100 0 0.0 0.0 0.1 0.0 0.2 0.0 0.3 0.50

0363101 0.4 1.00 0.6 1.0 0.7 1.0 0.8 1.00

0363102 0.9 1.00 1.0 0.0

* two-phase difference tables from semiscale

0364100 1 1 0.0 0.00 0.1 0.83 0.2 1.09

0364101 0.5 1.02 0.6 1.015 0.7 1.01

0364102

0364200 1

0364201

0364300 1

0364301

0364302

0364400 1

0364401

0364402

0364500 1

0364501

0364502

0364600 1

0364601

0364602

0364700 1

0364800 1

0364900 2

0365000 2

0.9

2 0.0

0.4

3 -1.0

-0.7

-0.25

4 -1.0

-0.7

-0.35

5 0.0

0.4

0.8

6 0.0

0.4

0.8

7 0.0

8 0.0

1 0.0

2 0.0

0.94

0.00

0.21

-1.06

-2.36

-1.69

-1.16

-0.31

0.00

0.00

-0.65

-1.19

0.11

0.13

-0.51

0.0

0.0

0.0

0.0

1.0

0.1

0.8

-0.9

-0.6

-0.1

-0.9

-0.6

-0.2

0.2

0.6

1.0

0.1

0.5

0.9

1.0

1.0

1.0

1.0

1.00

-0.04

0.67

-1.24

-2.79

-0.50

-0.78

-0.17

0.05

-0.34

-0.95

-1.47

0.13

0.07

-0.91

0.0

0.0

0.0

0.0

0.2

0.9

-0.8

-0.5

0.0

-0.8

-0.5

0.0

0.25

0.6

1.0

0.00

0.80

-1.77

-2.91

0.00

-0.05

-0.17

0.11

0.15

-0.04

-1.47

0.3 0.11

1.0 1.0

-0.4 -2.67

0.7 -0.23

124
0365100 2 3 0.0 0.0 1.0 0.0

0365200 2 4 0.0 0.0 1.0 0.0

0365300 2 5 0.0 0.0 1.0 0.0

0365400 2 6 0.0 0.0 1.0 0.0

0365500 2 7 0.0 0.0 1.0 0.0

0365600 2 8 0.0 0.0 1.0 0.0

, pump speed controller for steady calculation

0366100 0 cntrlvar, 425

0366101 0.0 0.0

0366102 2400.0 2400.0

20542400 mserr sum 1.0 0.0 1

20542401 51.1 -1.0 mflowj,301000000

20542500 rcpspp integral 0.1 311. 0

20542501 cntrlvar,424

* primary loop piping components -single loop b

* component 41 - single loop (loop b) hot leg

0410000 hotlgbl snglvol

0410101 1.0936e-2 1.1941 0.0 0.0 0.0 0.0 4.57e-5 .118 00000

0410200 003 15576088. 563.3

, component 42 - single loop

0420000 hotlgb2 snglvol

0420101 1.0936e-2 0.5 0.0 0.0 0.0 0.0 4.57e-5 .118 00000

0420200 003 15576080. 563.3

* component 43 - single loop hot leg to sg

0430000 hotlgb3 pipe

0430001 3

0430101 1.0936e-2 3 *volume area

125
0430201

0430301

0430302

0430303

0430401

0430601

0430602

0430603

0430701

0430702

0430703

0430801

0430901

0430902

0431001

0431101

0431201

0431202

0431203

0431300

0431301

0431302

0431401

1.0936e-2

0.79775

1.44800

0. 5506

0.0

0.0

90.

50.

0.0

1.44800

0.4637

4.57e-5

0.117 0.

0.065 0.

00000 3

01000 2

003 1556

003 1556

003 1556

0

6.26299 6

6.26303 6

.118 C

2

1

2

3

3

1

2

3

1

2

3

.118

117

065

30072.

35056.

35440.

*junction area

*volume length

*volume volumes

*vert angle

*delta z

3 *rough diam

1 *junction f-loss

2 *junction f-loss

* vol flags

* vcahs

563.3 0.0 0.

563.3 0.0 0.

563.3 0.0 0.

r-loss

r-loss

0.

0.

0.

1

2

3

.41299 0. 1

.56904 0. 2 I. 1. 1.

* 3.397625

* 3.39762

2

* component 401 - h.l. junction to hot leg

4010000

4010101

4010201

4010110

hotlg4b sngljun 041010000 042000000 0.0 0.0 0.0 01000

0 6.261222 6.331222 0. * 3.39708

.118 0. 1. 1.

* component 402 - h.l. junction from pressurizer surge nozzle

4020000 hotlg5b sngljun

4020101 042010000 043000000 0.0 0.0 0.0 01000

4020201 0 6.261298 6.3412985 0. * 3.39763

4020110 .118 0. 1. 1.

* component 45 - single loop cold leg pump suction piping

0450000 pumpsa pipe

0450001 5

126
0450101

0450201

0450301

0450302

0450303

0450304

0450305

0450401

0450402

0450403

0450404

0450405

0450601

0450602

0450603

0450604

0450701

0450702

0450703

0450704

0450705

0450801

0450901

0450902

0450903

0450904

0451001

0451101

0451201

0451202

0451203

0451204

0451205

0451300

0451301

0451302

0451303

0451304

0451401

0.0

1.0936e-2

0.4189

1.94015

2.22285

0.820

2.0697

4.5810e-3

21.2175e-3

24.3095e-3

8.9670e-3

22.6340e-3

-50.00

-90.

0.0

90.

-. 3404

-1.94015

-2.12015

0.0

1.9671

4.57e-5

.065

0.0

.117

.117

00000 5

01000 4

003 152

003 152

003 153

003 153

003 15Z

0

5

4

1

2

3

4

5

1

2

3

4

5

1

3

4

5

1

2

3

4

5

0.0

.065

0.0

.117

.117

84064.

92512.

07552.

05400.

98072.

*volume areas

*junction areas

*volume lengths

*vertical angle

*delta z

5 *volume roughnes diam

1 *f-loss r-loss

2 *f-loss r-loss

3

4

* volume flags

*junction vcahs

560.0 0.0 0.

560.0 0.0 0.

560.0 0.0 0.

560.0 0.0 0.

560.0 0.0 0.

0. 1

0. 2

0. 3

0. 4

0. 5

6.210586

6.210582

6.210575

6.210571

.118

6.350195

6.4701855

6.470146

6.3705716

0. 1.

0. 1

0. 2*

0. 3*

0. 4*

1. 4

3.3976

3.397604

3.39761

3.397614

* component 47 - single loop pump discharge piping

0470000

0470001

0470101

0470201

cldlgal pipe

2

1.0936e-2 2

1.0936e-2 1

*volume areas

*jumtion areas

127
0470301

0470302

0470401

0470501

0470601

0470701

0470801

0470901

0471001

0471101

0471201

0471202

1.05

0.859

0.0

0.0

0.0

0.0

4.57e-5

0.0

00

01000

003 1!

003 1l

1

2

2

2

2

2

0.0 2

0.0 1

8

5757504.

5757496.

*volume lengths

*volume lengths

*volume volumes

*horiz angle

*vertical angle

*delta z

*roughness diam

*junction f-loss r-loss

*volume fe

*junction vcahs

560.0 0.0 0.

560.0 0.0 0.

0. 1

0. 2

0471300 0

0471301 6.190581 6.2805816 0. 1 * 3.39763

0471401 .118 0. 1. 1. 1

* component 48 - single loop accumulator nozzle

0480000

0480001

0480101

0480200

0481101

0482101

0481201

0482201

0481110

0482110

accnoza branch

2 0

1.0936e-2 0.5 0.0 0.0 0.0 0.0 4.57e-5 .118 00000

003 15757488. 560.0

047010000 048000000 1.0936e-2 0.0 0.0 01000

048010000 049000000 1.0936e-2 0.0 0.0 01000

6.180582 6.270582 0. , 3.397636

6.180582 6.270582 0. * 3.39764

.118 0. 1. 1.

.118 0. 1. 1.

* component 49 - single loop cold leg piping

0490000

0490001

0490101

0490201

0490301

0490302

04904W1

0490601

0490701

0490801

0490901

0491001

0491101

cldlgaZ

2

1. 0936e-2

1. 0936e-2

.78406

.53586

0.0

0.0

0.0

4.57e-5

.144 .14

00000 2

01000 1

pipe

2 *volume areas

1 *junction areas

1 *volume lengths

2

2 *=volume volume,

2 *vertical angle

2 *delta z

S

4.0 2 *roughness diam

1 *junction f-loss

*volume flags

*junction vcahs

r-loss

128
0491201

0491202

0491300

0491301

0491401

003 15757480. 560.0 0.0 0.

003 15747464. 560.0 0.0 0.

0

6.180582 6.320582 0. 1 * 3.39764 .118 0. 1. 1. 1

0. 1

0. 2

* component 46 - inlet portion of single loop pump

0460000 pumpb pump

0460101 0.0 0.350 0.02062 0.0 41.518 0.232 00000

0460108 045010000 1.0936e-2 0.0 0.0 01000

0460109 047000000 1.0936e-2 0.0 0.0 01000

0460200 003 15534160. 560.0

0460201 0 6.200575 6.360145 0. * 3.39762

0460202 0 6.23 6.51 0. * 3.397625

0460110 .118 0. 1. 1.

0460111 .118 0. 1. 1.

0460301 36 36 36 -1 36 000 0

0460302 311. 0.9899 6.3056e-2 78.0 144.75 37.3 750.0 0. 0. 4.65e-2 0. 0

* primary loop piping components - single loop c

* component 51 " single loop (loop c) hot leg

0510000 hotlgcl snglvol

0510101 1.0936e-2 1.1941 0.0 0.0 0.0 0.0 4.57e-5 .118 00000

0510200 003 15576088. 563.3

* component 52 - pressure surge line nozzle in single loop

0520000 hotlgc2 snglvol

0520101 1.0936e-2 0.5 0.0 0.0 0.0 0.0 4.57e-5 .118 00000

0520200 003 15576080. 563.3

* component 53 - single loop hot leg to sg

0530000 hotlgc3 pipe

129
0530001

0530101

0530201

0530301

0530302

0530303

0530401

0530601

0530602

0530603

0530701

0530702

0530703

0530801

0530901

0530902

0531001

0531101

0531201

0531202

0531203

0531300

0531301

0531302

0531401

3

1.0936e-2

1.0936e-2

0.79775

1.44800

0.5506

0.0

0.0

90.

50.

0.0

1.44800

0.4637

4.57e-5

0.117 0.

0.065 0.

00000 3

01000 2

003 1556

003 1556

003 1556

0

3

2

1

2

3.

3

1

2

3

1

2

3

118

117

065

i0072.

5056.

5440.

411299

561904 ).

*volume area

*junction area

*volume length

*volume volumes

*vert angle

*delta z

3 *rough diam

1 *junction f-loss

2 *junction f-loss

* vol flags

* vcahs

563.3 0.0 0.

563.3 0.0 0.

563.3 0.0 0.

r-loss

r-loss

0.

0.

0.

1

2

3

6.261299

6.261303

.118

6.

6.

C L.

0. 1

0. 2

1. 2

3.397625

3.39762

* component 501 - h.l. junction to pressurizer surge nozzle

5010000 hotlg4c sngljun 5010101 051010000 052000000 0.0 0.0 0.0 01000

5010201 0 6.261222 6.331222 0. * 3.39708

5010110 .118 0. 1. 1.

* component 502 - h.l. junction from pressurizer surge nozzle

5020000 hotlg5c sngljun

5020101 052010000 053000000 0.0 0.0 0.0 01000

5020201 0 6.261298 6.3312985 0. * 3.39763

5020110 .118 0. 1. 1.

* component 55 - single loop cold leg pump suction piping

130
0550000

0550001

0550101

0550201

0550301

0550302

0550303

0550304

0550305

0550401

0550402

0550403

0550404

0550405

0550601

0550602

0550603

0550604

0550701

0550702

0550703

0550704

0550705

0550801

0550901

0550902

0550903

0550904

0551001

0551101

0551201

0551202

0551203

0551204

0551205

0551300

0551301

0551302

0551303

0551304 0551401

pumpsc pipe

5

0.0

1. 0936e-2

0.4189

1.94015

2.22285

0.820

2.0697

4.5810e-3

21.2175e-3

24.3095e-3

8.9670e-3

22.6340e-3

-50.00

-90.

0.0

90.

-. 3404

-1.94015

-2.12015

0.0

1.9671

4.57e-5

.065

0.0

.117

.117

00000 5

01000 4

003 152

003 152

003 153

003 153

003 152

5

4

1

2

3

4

5

1

2

3

4

5

1

3

4

5

1

2

3

4

5

0.0

.065

0.0

.117

.117

*volume areas

*junction areas

*volume lengths

*vertical angle

*delta z

5 *volume roughnes diam

1 *f-loss r-loss

2 *f-loss r-loss

3

4

84064. 5'

.92512. 5'

07552. 51

05400. 5'

98072. 5'

.370195

.4701855

.470146

.3505716

0. 1.

volume flags

junction vcahs

60.0 0.0 0.

60.0 0.0 0.

60.0 0.0 0.

60.0 0.0 0.

60.0 0.0 0.

0. 1

0. 2

0. 3

0. 4

0. 5

0

6.200586

6.200582

6.200575

6.200571

.118

6

6

6

6

0.

0.

0.

0.

1

2

3

4

"*

"*

3.3976

3.397604

3.39761

3.397614

1. 4

* component 57 - single loop pump discharge piping

0570000 cldlgal pipe

0570001 2

131
057010]

0570201

0570301

0570302

0570401

0570501

0570601

0570701

0570801

0570901

0571001

0571101

0571201

0571202

0571300

0571301

0571401

1. 0936e-2

1. 0936e-2

1.05

0.859

0.0

0.0

0.0

0.0

4.57e-5 0.

0.0 0.(

00 2

01000 1

003 157

003 157

0

6.190581 6.

.118 (

2

1

1

2

2

2

2

2

2

1

*volume areas

*juntion areas

*volume lengths

*volume lengths

*volume volumes

*horiz angle " *vertical angle *delta z

*roughness diam

*junction f-loss r-loss

*volume fe

*junction vcahs

560.0 0.0 0.

560.0 0.0 0.

.00

37504.

57496.

0. 1

0. 2

.2805816 0. 1 * 3.39763

). 1. 1. 1

* component 58 - single loop accumulator nozzle

0580000

0580001

0580101

0580200

0581101

0582101

0581201

0582201

0581110

0582110

accnozc branch

2 0

1.0936e-2 0.5 0.0 0.0 0.0 0.0 4.57e-5 .118 00000

003 15757488. 560.0

057010000 058000000 1.0936e-2 0.0 0.0 01000

058010000 059000000 1.0936e-2 0.0 0.0 01000

6.180582 6.270582 0. * 3.397636

6.180582 6.270582 0. * 3.39764

.118 0. 1. 1.

.118 0. 1. 1.

* component 59 - single loop cold leg piping

059O000

0590001

0590101

0590201

0590301

0590302

0590401

0590601

0590701

0590801

0590901

cldlgc2 pipe

2

1.0936e-2 2 *volume areas

1.0936e-2 1 *junction areas

.78406 1 *volume lengths

.53586 2

0.0 2 *--volume volumes

0.0 2 *vertical angle

0.0 2 *delta z

4.57e-5 0.0 2 *roughness diam

.144 .144 1 *junction f-loss r-loss

132
0591001

0591101

0591201

0591202

0591300

0591301

0591401

00000 2

01000 1

003 1!

003 f.

0

6.180582

.118

5757480.

5747464.

*volume flags *junction vcahs

560.0 0.0 0.

560.0 0.0 0.

0.1

0. 2

6.320582 0. 1 * 3.39764-

0. 1. 1. 1

* component 56 - inlet portion of broken loop pump

0560000

0560101

0560108

0560109

0560200

0560201

0560202

0560110

0560111

pumpc pump 0.0 0.35 0.02062 0.0 41.518 0.232 00000

055010000 1.0936e-2

057000000 1.0936e-2

003 15534160. 560.0

0 6.200559 6.360128

0 6.23 6.51

.118 0. 1. 1.

.118 0. 1. 1.

0.0 0.0 01000

0.0 0.0 01000

0. * 3.39762

-. 3.39762

-1 36 000 0560301 36 36 36 0

0560302 311. 0.9899 6.3056-2 78.0 144.75 37.3 750.0 0. 0. 4.65e-2 0. 0.

, description of primary system steam generator components

, single loop a : broken loop

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

0340000

0340001

0340101

0340102

0340103

0340201

0340301

0340302

0340303

0340304

0340305

0340306

0340307

0340308

0340309

stmgena 22

0.0

1.0342e-2

0.0

1.0342e-2

0.798

0.2

0.4

0.6

0.8

1.0

1.5

0.725

1.5

pipe

1

21

22

21

1

2

3

4

5

6

10

12

16

133
0340310 1.0 17

0340311 0.8 18

0340312 0.6 19

0340313 0.4 20

0340314 0.2 21

0340315 - 01798----- 22

0340401 35.0607e-3 1

0340402 0.0 21

0340403 35.0607e-3 22

0340601 90. 11

0340602 -90. 22

0340701 0.7523 1

0340702 0.2 2

0340703 0.4 3

0340704 0.6 4

0340705 0.8 5

0340706 1.0 6

0340707 1.5 10

0340708 0.685 11

0340709 -0.685 12

0340710 -1.5 16

0340711 -1.0 17

0340712 -0.8 18

0340713 -0.6 19

0340714 -0.4 20

0340715 -0.2 21

0340716 -0.7523 22

0340801 4.57e-5 .229 1

0340802 1.Oe-6 1.968e-2 21

0340803 4.57e-5 .229 22

0340901 .182 .530 1

0340901 0.0 0.0 1

0340902 0.0 0.0 10

0340903 .078 .078 11

0340903 0.0 0.0 11

0340904 0.0 0.0 20

0340905 .530 .182 21

0340905 0.0 0.0 21

0341001 00 22

0341101 11000 1 *ccfl on

0341102 01000 20 *ccfl off for j's 2-20

0341103 11000 21 *ccfl on

0341201 0 15510264. 1274710. 2443832. 0. 0. 1

0341202 0 15496888. 1265522. 2443912. 0. 0. 2

0341203 0 15484768. 1249498. 2443962. 0. 0. 3

0341204 0 15471200. 1229853. 2444046. 0. 0. 4

0341205 0 15456160. 1209553. 2444166. 0. 0. 5

0341206 0 15449608. 1290901. 2444320. 0. 0. 6

134
0341207

0341208

0341209

0341210

0341211

0341212

0341213

0341214

0341215

0341216

0341217

0341218

0341219

0341220

0341221

0341222

0341300

0341301

0341302

0341303

0341304

0341305

0341306

0341307

0341308

0341309

0341310

0341311

0341312

0341313

0341314

0341315

0341316

0341317

0341318

0341319

0341320

0341321

0341401

0341402

0341403

0 15440416. 12

0 15429320. 12

0 15318176. 12

0 15307000. 12

0 15398832. 12

0 15398768. 12

0 15306760. 12

0 15317744. 12

0 15328736. 12

0 15239736. 12

0 15ZA8904. 12

0 15255504. 12

0 15260640. 12

0 15264304. 12

0 15266504. 12

0 15270096. 12

0

6.06659 6.06659 0.

6.04233 6.04233 0.

6.00105 6.00105 0.

6.051265 6.051265 0.

6.002835 6.002835 0.

6.05996 6.05996 0.

6.01923 6.01923 0.

6.09331 6.09331 0.

6.07625 6.07625 0.

6.06467 6.06467 0.

6.0599 6.0599 0.

6.05599 6.05599 0.

6.0507 6.0507 0.

6.04723 6.04723 0.

6.04499 6.04499 0.

6.04358 6.04358 0.

6.04293 6.04293 0.

6.04252 6.04252 0.

6.042175 6.042175 0.

6.041915 6.041915 0.

6.04171 6.04171 0.

1.968e-2 0. 1.

1.968e-2 0. 1.

1.968e-2 0. 1.

•72667.

•60562.

•52372.

A6720.

A4427.

42560.

40036.

.38388.

37328.

36668.

36374.

36190.

36035.

35918.

35825.

35824.

1 *

2*

3*

4*

5 *

6*

7*

8*

9*

10 *

11 *

12 *

13 *

14 *

15 *

16 *

17 *

18 *

19 *

20 *

21 *

0.725

1.

0.725

2444538. 0.

2444800. 0.

2445062. 0.

2445328. 0.

2445520. 0.

2445522. 0.

2445332. 0.

2445072. 0.

2444812. 0.

2444554. 0.

2444336. 0.

2444180. 0.

2444060. 0.

2443974. 0.

2443922. 0.

2443836. 0.

0. 7

0. 8

0.9 9 .. 0. 10

0. 11 0.. -12

0. 13

0. 14

0. 15 0. 16

0. 17

0. 18

0. 19

0. 20

0. 21

0. 22

3.397596

3.397594

3.39759

3.39759

3.39759

3.397585

3.39758

3.39758

3.39758

3.39758

3.39758

3.39758

3.397585

3.397585

3.39759

3.39759

3.39759

3.39759

3.39759

3.39759

3.39759

1 *ccfl on

20 *ccfl off for i's 2-20

21 *ccfl on

* steamgenerator inlet junction

3040000 sgina sngljun

3040101 033010000 034000000 1.0936e-2 0.0 0.0 01100

135
3040201 0 6.26308 6.41928 0. * 3.397615

3040110 .118 0. 1. 1.

* steam generator outlet junction

3050000 sgouta sngljun

3050101 034010000 035000000 1.093578e-2 0.0 0.0 01100

3050201 0 6.20596 6.40623 0. * 3.3976

3050110 .118 0. 1. 1.

• single loop b

0440000 stmgenb pipe

0440001 22

0440101 0.0 1

0440102 1.0342e-2 21

0440103 0.0 22

0440201 1.0342e-2 21

0440301 0.798 1

0440302 0.2 2

0440303 0.4 3

0440304 0.6 4

0440305 0.8 5

0440306 1.0 6

0440307 1.5 10

0440308 0.725 12

0440309 1.5 16

0440310 1.0 17

0440311 0.8 18

0440312 0.6 19

0440313 0.4 20

0440314 0.2 21

0440315 0.798 22

0440401 35.0607e-3 1

0440402 0.0 21

0440403 35.0607e-3 22

0440601 90. 11

0440602 -90. 22

0440701 0.7523 1

0440702 0.2 2

0440703 0.4 3

0440704 0.6 4

0440705 0.8 5

0440706 1.0 6

136
0440707 1.5

0440708 0.685

0440709 -0.685

0440710 -1.5

0440711 -1.0

0440712 -0.8

0440713 -0.6

0440714 -0.4

0440715 -0.2

0440716 -0.7523

0440801 4.57e-5

0440802 1.0e-6

0440803 4.57e-5

0440901

0440901

0440902

0440903

0440903

0440904

0440905

0440905

0441001

0441101

0441102

0441103

0441201

0441202

0441203

0441204

0441205

0441206

0441207

0441208

0441209

0441210

0441211

0441212

0441213

0441214

0441215

0441216

0441217

0441218

0441219

0441220

0441221

0441222

0441300

.182

0.0

0.0

.078

0.0

0.0

.530

0.0

00

11000

01000

11000 00000000000000000000000

10

11

12

16

17

18

19

20

21

22

.229 

1

1.968e-2 21

.229 22

.530 

1

0.0 

1

0.0 10

.078 11

0.0 11

0.0 20

.182 21

0.0 21

22

1 *ccfl on

20 *ccfl off for j's 2-20

21 *ccfl on

15510264. 1274710. 2443832. 0.

15496888. 1265522. 2443912. 0.

15484768. 1249498. 2443962. 0.

15471200. 1229853. 2444046. 0.

15466160. 1209553. 2444166. 0.

15449608. 1290901. 2444320. 0.

15440416. 1272667. 2444538. 0.

15429320. 1260562. 2444800. 0.

15318176. 1252372. 2445062. 0.

1.5307+7 1246720. 2445328. 0.

15398832. 1244427. 2445520. 0.

15398768. 1242560. 2445522. 0.

15306760. 1240036. 2445332. 0.

15317744. 1238388. 2445072. 0.

15328736. 1237328. 2444812. 0.

15299736. 1236668. 2444554. 0.

15288904. 1236374. 2444336. 0.

15275504. 1236190. 2444180. 0.

15260640. 1236035. 2444060. 0.

15264304. 1235918. 2443974. 0.

15266504. 1235825. 2443922. 0.

15270096. 1235824. 2443836. 0.

0. 1

0. 

2

0. 

3

0. 4

0. 

5

0. 

6

0. 

7

0. 8

0. 

9

0. 10

0. 11

0. 12

0. 13

0. 14

0. 15

0. 16

0. 17

0. 18

0. 19

0. 20

0. 21

0. 22

137
0441301

0441302

0441303

0441304

0441305

0441306

0441307

0441308

0441309

0441310

0441311

0441312

0441313

0441314

0441315

0441316

0441317

0441318

0441319

0441320

0441321

0441401

0441402

0441403

6.06659 6.06659 0.

6.04233 6.04233 0.

6.00105 6.00105 0.

6.051265 6.051265 0.

6.002835 6.002835 0.

6.05996 6.05996 0.

6.01923 6.01923 0.

6.09331 6.09331 0.

6.07625 6.07625 0.

6.06467 6.06467 0.

6.0599 6.0599 0.

6.05599 6.05599 0.

6.0507 6.0507 0.

6.04723 6.04723 0.

6.04499 6.04499 0.

6.04358 6.04358 0.

6.04293 6.04293 0.

6.04252 6.04252 0.

6.042175 6.042175 0.

6.041915 6.041915 0.

6.04171 6.04171 0.

1.968e-2 0. 1.

1.968e-2 0. 1.

1.968e-2 0. 1.

1 *

2*

3*

4*

5 *

6*

7*

8 *

9*

10 *

11 *

12 *

13 *

14 *

15 *

16 *

17 *

18 *

19 *

20 *

21 *

0.725

1.

0.725

3.397596

3.397594

3.39759

3.39759

3.39759

-3i397585-

3.39758

3.39758

3.39758

3.39758

3.39758

3.39758

3.397585

3.397585

3.39759

3.39759

3.39759

3.39759

3.39759

3.39759

3.39759

1 *ccfl

20 *ccfl

21 *ccfl

on

off for j's 2-20

on

* steam generator inlet junction

4040000 sginb sngljun

4040101 043010000 044000000 1.0936e-2 0.0 0.0 01100

4040201 0 6.26308 6.40928 0. * 3.397615

4040110 .118 0. 1. 1.

* steam generator outlet junction

4050000 sgoutb sngljun

4050101 044010000 045000000 1.093578e-2 0.0 0.0 01100

4050201 0 6.20596 6.40623 0. * 3.3976

4050110 .118 0. 1. 1.

* single loop -c

0540000 stmgenc pipe

138
0540001

0540101

0540102

0540103

0540201

0540301

0540302

0540303

0540304

0540305

0540306

0540307

0540308

0540309

0540310

0540311

0540312

0540313

0540314

0540315

0540401

0540402

0540403

0540601

0540602

0540701

054070Z

0540703

0540704

0540705

0540706

0540707

0540708

0540709

0540710

0540711

0540712

0540713

0540714

0540715

0540716

0540801

0540802

0540803

0540901

0540901

0540902

0540903

22

0.0 

1

1.0342e-2 21

0.0 22

1.0342e-2 21

0.798 

1

0.2 

2

0.4 

3

0.6 

4

0.8 

5

1.0 

6

1.5 10

0.725 12

1.5 16

1.0 17

0.8 18

0.6 19

0.4 20

0.2 21

0.798 22

35.0607e-3 

1

0.0 21

35.0607e-3 22

90. 11

-90. 22

0.7523 

1

0.2 

2

0.4 

3

0.6 

4

0.8 

5

1.0 

6

1.5 10

0.685 11

-0.685 12

-1.5 16

-1.0 17

-0.8 18

-0.6 19

-0.4 20

-0.2 21

-0.7523 22

4.57e-5 .229 

1

1.0e-6 1.968e-2 21

4.57e-5 .229 22

.182 .530 

1

0.0 0.0 

1

0.0 0.0 10

.078 .078 11

139
0540903

0540904

0540905

0540905

0541001

0541101

0541102

0541103

0541201

0541203

0541203

0541204

0541205

0541206

0541207

0541208

0541209

0541210

0541211

0541212

0541213

0541214

0541.15

0541216

0541217

0541218

0541219

0541220

0541221

0541223

0541300

0541301

0541302

0541303

0541304

0541305

0541306

0541307

0541308

0541309

0541310

0541311

0541312

0541313

0541314

0541315

0541316

0541317

0.0

0.0

.530

0.0

00

11000

01000

11000

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

6.0665Y

6.04233

6.00105

6.05126

6.00283

0.0 11

0.0 20

.182 21

0.0 21

22

1 *ccfl on

20 *ccfl off for j's 2-20

21 *ccfl on

15514264. 1274710. 2443832. 0.

15496888. 1265522. 2443913. 0.

15484768. 1249498. 2443962. 0.

15471200. 1229853. 2444046. 0.

15456160. 1209553. 2444166. 0.

15449608. 1290901. 2444320. 0.

15440416. 1272667. 2444538. 0.

15329320. 1260562. 2444800. 0.

15318176. 1252372. 2445062. 0.

1.5307+7 1246720. 2445328. 0.

15338832. 1244427. 2445520. 0.

15338768. 1242560. 2445522. 0.

15336760. 1240036. 2445332. 0.

15337744. 1238388. 2445072. 0.

15338736. 1237328. 2444812. 0.

15239736. 1236668. 2444554. 0.

15238904. 1236374. 2444336. 0.

15255504. 1236190. 2444180. 0.

15260640. 1236035. 2444060. 0.

15264304. 1235918. 2443974. 0.

15266504. 1235825. 2443922. 0.

15670096. 1235824. 2443836. 0.

0.1

0. 2

0. 3

0. 4

0. 5

0. 6

0. 7

0. 8

0. 9

0. 10

0. 11

0. 12

0. 13

0. 14

0. 15

0. 16

0. 17

0. 18

0. 19

0. 20

0. 21

0. 22

6.06659 0.

6.04233 0.

6.00105 0.

55 6.051265 0.

35 6.002835 0.

6.05996

6.01923

6.09331

6.07625

6.06467

6.0599

6.05599

6.0507

6.04723

6.04499

6.04358

6.04293

6.05996

6.01923

6.09331

6,07625

6.06467

6.0599

6.05599

6.0507

6.04723

6.04499

6.04358

6.04293

0.

0.

0.

0.

0.

0.

0.

0.

0.

0.

0.

0.

1

2

3

4

5

6

7

8

9

10

11

12

13

14

15

16

17

3.397596

3.397594

3.39759

3.39759

3.39759

3.397585

3.39758

3.39758

3.39758

3.39758

3.39758

3.39758

3.397585

3.397585

3.39759

3.39759

3.39759

140
0541318

0541319

0541320

0541321

0541401

0541402

0541403

6.04252

6.042175

6.041915

6.04171

1.968e-2

1.968e-2

1. 968e-2

6.04252 0.

6.042175 0.

6.041915 0.

6.04171 0.

0. 1.

.0. 1.

0. 1.

18 *

19 *

20 *

21 *

0.725

1.. .

0.725

3.39759

3.39759

3.39759

3.39759

1 *ccfl on

.20 *ccfl off-for j's 2-20

21 *ccfl on

* component 504 steam generator inlet junction

5040000

5040101

5040201

5040110

sginc sngljun

053010000 054000000 1.0936e-2 0.0 0.0 01100

0 6.26308 6.41928 0. * 3.397615

.118 0. 1. 1.

* component 505 steam generator outlet junction

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

5050000

5050101

5050201

5050110

sgouta sngljun 054010000 055000000 1.093578e-2 0.0 0.0 01100

0 6.20596 6.40623 0. * 3.3976

.118 0. 1. 1. *

*

*

pressurizer and pressurizer surge line

* component 90 pressurizer surge line

0900000

0900001

0900101

0900102

0900103

0900201

0900301

0900302

0900303

0900401

0900402

0900403

0900601

0900602

prsurg

3

0.0

1.445e-3

0.0

1.445e-3

0.850

0.0

2.69

1. 11865e-3

9.0406e-3

3.86375e-3

90.

0.92

pipe

1

2

3

2

1

2

3

1

2

3

1

2

*volume areas

*junction areas

*volume lengths

*volume volumes

*vertical angles

141
0900603

0900701

0900702

0900703

0900801

0900901

0901001

0901101

0901201

0901202

0901203

0901300

0901301

0901302

0901401

90.

0.850

0.1

2.69

4.57e-I

2.05

00

01000

003

003

003

3

1 *elevation changes 2

3

5 0.0429 3 *roughi

Z.05 Z *junctii 3 *volume fe

2 *junction vcahs

15546480. 563.0 0.0 0.

15544504. 563.0 0.0 0.

15536800. 563.0 0.0 1.6(

ness diam

on loss coef

0. 1

0. 2

)0417-5 0. 3

k -5.41856-4

k -5.38514-4

0

-5.88719-4

-5.8603-4

.0429 0.

-5.8872-4

.016745

1. 1.

0.

0.

2

12

* component 91 - pressurizer

0910000

0910001

0910101

0910201

0910202

0910301

0910302

0910303

0910304

0910401

0910402

0910403

0910404

0910601

0910801

0910901

0911001

0911101

0911201

0911202

0911203

0911204

0911205

0911300

0911301

0911302

0911303

0911304

preszr

5

0.0

3.1276

3.4636e

0.105

0.892

5.4145

0.105

2.1616e

2.7890e

0.1875N

2.4245e

90.

4.57e-5

0.0

00

01000

0

0

0

0

0

0

-2.7007

-5.002(

-. 40690

-4.875N

P•

5

e-2 •

ipe

,volume areas

L *junction areas

,-2 4

1 *volume lengths

2

4

5

e-3 1 *volume volumes

e-2 2

35 4

3-3 5

5 *vertical angles

5 0.210 5 *roughness diam

0.0 4 *junction loss coef

5 *volume flags fe

4 *junction flags vcahs

15528088. 1512193. 2.444+6 0.0

15525984. 1512645. 2444076. 0.

15518704. 1512336. 2452160. 0.5

15512504. 1512835. 2452946. 1.0

15510744. 1512734. 2452922. 1.0

0.

0.

0.

0.

0.

1

2

3

4

5

823-5

51-5

1

9-7

1.078118-4

.612779

-3.83528-5

-4.87571-7

0. 1

0. 2

0. 3*

0. 4*

-5.36641-4

-5.28403-4

-1.353289-4

-1.717944-6

142
0911401 .210 0. 1. 1. 4

* component 93 trip valve for pzr steady state

0930000

0930101

0930201

0930300

0930301

pzrvlv

91010000

1

trpvlv

507

valve

94000000

0.0 0.0

0.02 10.

0.0

10. 01100

* component 94 time dependent volume for pzr stp

0940000

0940101

0940200

0940Z01

pzr-tmdp

0. 1.

002

0 15.5:

tmdpvol

100. 0.

0

le6 1.0

90. 1. 0. 0. 11

* component 901 - pressurizer to surge line

9010000

9010101

9010201

9010110

prtosur sngljun 090010000 091000000 0.0 0.0

0 -5.88604-4 .001109272 0.

.0429 0. 1. 1.

0.0 01100

* -5.37312-4

* steam generator secondary system components - single loop a

* component 60 - sg riser

0600000

0600001

0600101

0600201

0600301

0600302

0600303

0600304

tubebun pipe

10

0.0 10

0.0 9

0.2 1

0.4 2

0.6 3

0.8 4

*volume areas

*junction areas

*volume lengths

*volume lengths

*volume lengths

*volume lengths

143
0600305 1.0 5 *volume lengths

0600306 1.5 9 *volume lengths

0600307 1.8025 10 *volume lengths

0600401 0.01151 1 *volume volumes

0600402 0.02303 2 *volume volumes

0600403 0..03451 3 .*volume volumes

0600404 0.04605 4 *volume volumes

0600405 0.05756 5 *volume volumes

0600406 0.08635 9 *volume volumes

0600407 0.10376 10 *volume volumes

0600601 90. 10 *vertiical angles

0600801 4.57e-5 0.03503 10 *roughness diam

0600901 0.709 0.709 9 *junction resistance

0601001 00100 10 *flags pvbfe

0601101 01000 9 *flags vcahs

0601201 0 7028456. 1248771. 2582846. .042479 0. 1

0601202 0 7026396. 1249808. 2582862. .0791885 0. 2

0601203 0 7023096. 1250779. 2582890. .100384 0. 3

0601204 0 7018676. 1251212. 2582926. .1024675 0. 4

0601205 0 7013236. 1251169. 2582972. .1001885 0. 5

0601206 0 7016020. 1250842. 2583030. .137237 0. 6

0601207 0 7017640. 1250435. 2583100. .1617664 0. 7

0601208 0 6999476. 1250028. 2583166. .20956 0. 8

0601209 0 6991468. 1249626. 2583234. .253402 0. 9

0601210 0 6982900. 1249192. 2583306. .319663 0. 10

0601300 0

0601301 .291368 .293318 0. 1 * 8.3189

0601302 .296823 .3436065 0. 2 * 8.32017

0601303 .3058306 .414301 0. 3 * 8.32394

0601304 .318744 .485924 0. 4 * 8.32663

0601305 .335345 .542248 0. 5 * 8.32915

0601306 .3635625 .6048185 0. 6 * 8.33147

0601307 .4178196 .661324 0. 7 * 8.33338

0601308 .444346 .713936 0. 8 * 8.33501

0601309 .565791 .775627 0. 9 * 8.33651

0601401 .03503 0. 1. 1. 9

• component 61 - lower steam dome

0610000 istmdom pipe

0610001 3

0610101 0.0 3 *volume area

0610201 0.0 2 *junction area

0610301 0.158 1 *volume length

0610302 0.7925 2

0610303 0.900 3

144
0610401 0.010393

0610402 0.03861

0610403 0.04385

0610601 90.

0610801 4.57e-5

0610901 0.0 (

0611001 00000

0611101 01000 2

0611201 0 69

0611202 0 69

0611203 0 69

1 *volume volumes

2 *volume volumes

3 *volume volumes

3

.249 3.0

177848.

165112.

169880.

3 *rough diam

2 *junction f-loss r-loss

* vol flags

2 vcahs

1248987. 2583346. .1070403 0. 1

1248752. 2583374. .124302 0. 2

1248488. 2583418. .1005756 0. 3

0611300

0611301

0611302

0611401

0

.426618

.432377

.249

1.27186 0.

1.227373 0.

0. 1. 1.

1 * 8.28098

2 * 8.30996

2

. component 62 - middle steam dome and separator

*22222222222222222.22.22•.2222222..

0620000

0620001

0620101

0620200

0621101

0622101

0623101

0621201

0622201

0623201

0621110

0622110

0623110

mstmdom branch

3 0

0.0 2.16 0.59549 0.0

0 6953520. 1248202.

90. 2.16 4.57e-5 .249

2583470. .64374

00

062010000

062000000

061010000

-0.49608

.3790846

.50494

.800

.539

.249

068000000 .502655 .816

063000000 44.915e-2 .060

062000000 4.8695e-2 0.0

.04985623 0. * .283642

2.01394252 0. * 8.05382

2.84995 0. * 8.2958 ). 1. 1.

O. 1. 1.

O. 1. 1.

.452

.014

).0

01000

01002

01000

(

(

(

* component 63 - upper downcomer

*2**222222**22222222*2*2222*222222*

0630000

0630101

0630200

updwnc snglvol

0.0 0.3375

0 6953596.

.14922 0.0 -90. -. 3375

1248164. 2583470. .594008

4.57e-5 .539 00

* component 64 - upper feedwater ring

0640000 ufwring snglvol

0640101 0.0 1.6055 0.15856 0.0. -90. -1.6055 4.57e-5 0.176 00

145
0640Z00 0 6965196. 1248192. 2583464. .388591

* component 65 - lower feedwater ring

0650000

0650001

0650101

0650200

0651101

0652101

0651201

0652201

0651110

0652110

lfwring branch

2 0

0.0 .8275 .08172 0.0 -90. -. 8275

0 6970192. 1246853. 2583416. .022155

064010000 065000000 .09648 0.0 0.0

065010000 066000000 3.0415e-2 .339 .459

.2679376 .09100312 0. * 8.05953

.651864 0.076746 0. * 10.24751

.176 0. 1. 1.

.05983 0. 1. 1.

4.57e-5 .176 00

01000

01000

* component 66 - 11 tube region

0660000

0660101

0660200

dclltube snglvol

0.0 1.9815 0.06336

0 6988432. 1247671.

0.0 -90.

2583348.

-1.9815 4.57e-5 .05983 00

.071796 *

* component 67 - sg-dc bottom part (4 tube region and bottom annulus)

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

*

0670000

0670001

0670101

0670201

0670301

0670302

0670303

0670304

0670305

0670306

0670307

0670401

0670402

0670403

0670404

0670405

0670406

0670407

0670601

dc4tube

9

0.0

0.0

1.481

1.5

1.0

0.8

0.6

0.4

0.2

8.6429e-3

8.7538e-3

5.8359e-3

4.6687e-3

3.5015e-3

2.3343e-3

4.0563e-3

-90.

pipe

9

1

4

5

6

7

8

9

1

4

5

6

7

8

9

9

*volume areas

*junction areas

*volume lengths

*volume lengths

*volume lengths

*volume lengths

*volume lengths

*volume lengths

*volume lengths

*volume volumes

*volume volumes

*volume volumes

*volume volumes

*volume volumes

*volume volumes

*volume volumes

*vertiical angles

146
0670801

0670901

0670902

0671001

0671101

0671201

0671202

0671203

0671204

0671205

0671206

0671207

0671208

0671209

0671300

0671301

0671302

0671303

0671304

0671305

0671306

0671307

0671308

0671401

4.57e-5 0.04

0.0 0.0

0.5 1.0

00100 9

01000 8

0.... 6986060.

0 6995548.

0 7005052.

0 7004576.

0 7012532.

0 7018268.

0 7022724.

0 7025876.

0 7028420.

31 9 *roughness diam

7 *junction resistance

8 *junction resistance

*flags pvbfe

*flags vcahs

1247739. 2583284. .051734

1247816. 2583204. .048732

1247899. 2583124. .046789

1247988. 2583046. .044765

1248050. 2582978. .043300

1248102. 2582930. .042422

1248145. 2582894. .043589

1248196. 2582866. .059889

1248220. 2582846. .027817

'431

'5

6

p3

)4

'46

0.

0.

0.

0.

0.

0.

0.

0.

0.

1

2

3

4

5

6

7

8

9

0

2.913655

2.910042

2.905814

2.901764

2.998793

2.997078

2.99953

2.934037

.0431

1.79785

1.791977

1.799384

1.793686

1.79058

1.7928

1.7996

1.79198

0.

0.

0.

0.

0.

0.

0.

0.

0.

1.

I *

2*

3*

4*

5*

6*

7*

8*

8.31366

8.30743

8.30815

8.30803

8.30793

8.30804

8.3067

8.31625

1. 8

* component 609 - feedwater source

6090000 feedwtr tmdpvol

6090101 1.0e6 1.0 0.0 0.0 0.0 0..0 0.0 0.0 11

6090200 103 0

6090201 0.0 6.910e6 491.1

* component 68 • top of steam dome

0680000

0680101

0680200

tstmdom snglvol

0.0 0.4 0.13404

0 6952032. 1247984.

0.0 90. 0.4 4.57e-5 .653 00

2583424. 1.

* component 69 - steamline

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

0690000

.0690001

stmline

2

pipe

147
0690101

0690201

0690301

0690401

0690601

0690701

0690801

0690901

0691001

0691101

0691201

0691202

0691300

0691301

0691401

0.0 2

0.0 1

.15.825 2

34.25e-3 2

-90. 2

-8.049 2

4.57e-5 0O

2.888 2.I

00 2

01000 1

0 69411

0 6941;

0

6.25976 6.

.0525 0.

*volume areas

*junction areas

*volume lengths

*volume volumes

*vertical angles *delta z

2 *roughness diam

I *junction loss coef

* fe

.0525

388

!84.

772.

*vcahs

1247946. 2583452.

1247971. 2583498.

1. 1. 0. 1

0. 2

.49588 0. 1 * .283683

• 1. 1. 1

* feedwater

* component 601 - feedwater junction

6010000

6010101

6010200

6010201

6010202

6010203

6010204

6010205

6010206

6010207

6010208

6010209

6010210

6010211

6010212

6010213

6010214

6010215

6010216

6010217

6010218

6010219

6010220

609000000

1

-1.Oe+75

-1.1e+10

-1.Oe+10

-1.0e+9

-1.Oe+8

-1.0e+7

-1.Oe+6

-8.0e+5

-6.0e+5

-4.0e+5

-2.Oe+5

0.0

2.0e+5

4.0e+5

6.0e+5

8.0e+5

1.0e+6

1.Oe+7

1.Oe+8

1.Oe+9

"fedwtr"

065000000

0

tmdpjun

0.0

cntrlvar 263 * feedctl

0.0

0.0

-1. Oe+10

-1. Oe+9

-1. Oe+8

-1. Oe+7

-1. Oe+6

-8.0e+5

-6.Oe+5

-4.Oe+5

-2.Oe+5

0.0

2.Oe+5

4.0e+5

6.0e+5

8.0e+5

1.Oe+6

1.Oe+7

1. Oe+8

1.Oe+9

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

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

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

148
6010221 1.0e÷10 1.0Oe+10 0.0 0.0

* component 602 - junction between 11-tube and 4-tube regions

6020000

6020101

6020201

6020110

sgdwnc sngljun

066010000 067000000 .005836 1.5 1.5

0 3.3464 2.72928 0. * 8.25925

.0431 0. 1. 1.

01000

* component 603 - downcomer to tube bundle

6030000 sgdcbot sngljun

6030101 067010000 060000000 .025761 1.0 0.5 01000

6030201 0 .758816 .5368226 0. * 8.30314

6030110 .02 0. 1. 1.

* component 604 - steamdome to downcomer

6040000 sgdctop sngljun

6040101 063010000 064000000 .09648 0.0 0.0 01000

6040201 0 6.98816 .01109985 0. * 8.05694

6040110 .176 0. 1. 1.

* component 605 - tube bundle to steam dome

6050000 ristodm sngljun

6050101 060010000 061000000 .084496 0.0 0.0 01000

6050201 0 .1872706 .329899 0. * 8.31636

6050110 0.328 0. 1. 1.

* component 608 - top steam dome to steam line

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

6080000

6080101

6080201

6080110

tostmln sngljun

068010000 069000000 .0011401 0.0 0.0 01100

0 6.396664 6.48532 0. * .2836816

.0381 0. 1. 1. *

149
, component 606 - steamline outlet

6060000 "trb st n" valve

6060101 069010000 607000000 1.14e-3 0.0 0.0 00000

6060201 1 0. .5234 0

6060300 srvvlv

6060301 266 0 * steamctl.. .tcctl

6060401 0.0 0. 0.0

6060402 1.0 9357.2735 0.0 * this must be doubled

6060110 .0525 0. 1. 1.

* component 607 - steamline sink volume

6070000 stmsink tmdpvol

6070101 l.0e6 1.0 0.0 0.0 0.0 0.0 0.0 0.0 10

6070200 102 0

6070201 0.0 1.013e5 1.0

*steam generator secondary system components - single loop b

* component 70 - sg riser

0700000 tubebun pipe

0700001 10

0700101 0.0 10 *volume areas

0700201 0.0 9 *junction areas

0700301 0.2 1 *volumne lengths

0700302 0.4 2 *volume lengths

0700303 0.6 3 *volume lengths

0700304 0.8 4 *volume lengths

0700305 1.0 5 *volume lengths

0700306 1.5 9 *volume lengths

0700307 1.8025 10 *volume lengths

0700401 0.01151 1 *volume volumes

0700402 0.02303 2 *volume volumes

0700403 0.03454 3 *volume volumes

0700404 0.04605 4 *volume volumes

0700405 0.05756 5 *volume volumes

0700406 0.08635 9 *volume volumes

150
0700407 0.10376 10 *volume volumes

0700601 90. 10 *vertiical angles

0700801 4.57e-5 0.03503 10 *roughness diam

0700901 0.709 0.709 9 *junction resistance

0701001 00100 10 *flags pvbfe

0701101 01000 9 *flags vcahs

0701201 0 7028456. 1248771. 2582846. .042479 0. 1

0701202 0 7026396. 1249808. 2582862. .0791885 0. 2

0701203 0 7023096. 1250779. 2582890. .100384 0. 3

0701204 0 7018676. 1251212. 2582926. .1024675 0. 4

0701205 0 7013236. 1251169. 2582972. .1001885 0. 5

0701206 0 7016020. 1250842. 2583030. .137237 0. 6

0701207 0 7017640. 1250435. 2583100. .1617664 0. 7

0701208 0 6999476. 1250028. 2583166. .20956 0. 8

0701209 0 6991468. 1249626. 2583234. .253402 0. 9

0701210 0 6982900. 1249192. 2583306. .319663 0. 10

0701300 0

0701301 .291368 .253318 0. 1 * 8.3189

0701302 .2968235 .3436065 0. 2 * 8.32017

0701303 .3058306 .414301 0. 3 * 8.32394

0701304 .318744 .485924 0. 4 * 8.32663

0701305 .3353457 .542248 0. 5 * 8.32915

0701306 .3635625 .6048185 0. 6 * 8.33147

0701307 .3908196 .661324 0. 7 * 8.33338

0701308 .417346 .713936 0. 8 * 8.33501

0701309 .444791 .775627 0. 9 * 8.33651

0701401 .03503 0. 1. 1. 9

* component 71 - lower steam dome

0710000 Istmdom pipe

0710001 3

0710101 0.0 3 *volume area

0710201 0.0 2 *junction area

0710301 0.158 1 *volume length

0710302 0.7925 2

0710303 0.900 3

0710401 0.010393 1 *volume volumes

0710402 0.03861 2 *volume volumes

0710403 0.04385 3 *volume volumes

0710601 90. 3

0710801 4.57e-5 .249 3 *rough diam

0710901 0.0 0.0 2 *junction f-loss r-loss

0711001 00000 3 * vol flags

0711101 01000 2 , vcahs

0711201 0 6977848. 1248987. 2583346. .1070403 0. 1

151
0711202 0

0711203 0

0711300 0

0711301

0711302

0711401 .•

6975112. 1248752. 2583374.

6969880. 1248488. 2583418.

.124302 0. 2

.1005756 0. 3

426618

432377

A49

1.27186 0. 1 * 8.28098

1.227373 0. 2 * 8.30996

0. 1. 1. 2 .

* component 72 - middle steam dome and separator

0720000

0720001

0720101

0720200

0721101

0722101

0723101

0721201

0722201

0723201

0721110

0722110

0723110

mstmdom branch

3 0

0.0 2.16 0.59549 0.0 90. 2.16 4.57e-5 .249

0 6953520. 1248202. 2583470. .64374

072010000 078000000 .502655 .816 .452 01000

072000000 073000000 44.915e-2 .060 .014 01002

071010000 072000000 4.8695e-2 0.0 0.0 01000

-0.49608 .04985623 0. * .283642

.3790846 2.01394252 0. * 8.05382

.50494 2.04995 0. * 8.2958

.800 0. 1. 1.

.539 0. 1. 1.

.249 0. 1. 1.

00

* component 73 - upper downcomer

0730000

0730101

0730200

updwnc snglvol

0.0 0.3375

0 6953596.

.14922 0.0 -90. -. 3375

1248164. 2583470. .594008

4.57e-5 .539 00

* component 74 - upper feedwater ring

0740000

0740101

0740200

ufwring snglvol

0.0 1.6055 0.15856

0 6965196. 1248192.

0.0 -90. -1.6055 4.57e-5 0.176 00

2583464. .388591

* component 75 - lower feedwater ring

0750000

0750001

0750101

lfwring branch

2 0

0.0 .8275 .08172 0.0 -90. -. 8275 4.57e-5 .176 00

152
0750200 0 6970192. 1246853. 2583416. .022155

0751101 074010000 075000000 .09648 0.0 0.0 01000

0752101 .075010000 076000000 3.0415e-2 .339 .459 01000

0751201 .2679376 .09100312 0. , 8.05953

0752201 .651864 0.086746 0. * 10.24751

0751110 .176 0. 1. 1.

0752110 .05983 0. 1. 1.

* component 76 - 11 tube region

0760000 dclltube snglvol

0760101 0.0 1.9815 0.06336 0.0 -90. -1.9815 4.57e-5 .05983 00

0760200 0 6988432. 1247671. 2583348. .071796

* component 77 - sg-dc bottom part (4 tube region and bottom annulus)

0770000 dc4tube pipe

0770001 9

0770101 0.0 9 *volume areas

0770201 0.0 8 *junction areas

0770301 1.481 1 *volume lengths

0770302 1.5 4 *volume lengths

0770303 1.0 5 *volume lengths

0770304 0.8 6 *volume lengths

0770305 0.6 7 *volume lengths

0770306 0.4 8 *volume lengths

0770307 0.2 9 *volume lengths

0770401 8.6429e-3 I *volume volumes

0770402 8.7538e-3 4 *volume volumes

0770403 5.8359e-3 5 *volume volumes

0770404 4.6687e-3 6 *volume volumes

0770405 3.5015e-3 7 *volume volumes

0770406 2.3343e-3 8 *volume volumes

0770407 4.0563e-3 9 *volume volumes

0770601 -90. 9 *vertiical angles

0770801 4.57e-5 0.0431 9 *roughness diam

0770901 0.0 0.0 7 *junction resistance

0770902 0.5 1.0 8 *junction resistance

0771001 00100 9 *flags pvbfe

0771101 01000 8 *flags vcahs

0771201 0 6986060. 1247739. 2583284. .0517344 0. 1

0771202 0 6995548. 1247816. 2583204. .0487328 0. 2

0771203 0 7005052. 1247899. 2583124. .0467894 0. 3

0771204 0 7004576. 1247988. 2583046. .0447651 0. 4

153
0771205

0771206

0771207

0771208

0771209

0771300

0771301

0771302

0771303

0771304

0771305

0771306

0771307

0771308

0771401

0 70

0 70:

0 70;

0 70

0 70

0

2.941365

2.940042

2.945814

2.941764

2.948793

2.947078

2.94953

2.944037

.0431

12532.

18268.

22724.

25876.

?8420.

1248050.

1248102.

1248145.

1248196.

1248220.

2582978.

2582930.

2582894.

2582866.

2582846.

.0433005

.0424226

.0435893

.0598894

.02781746

0.

0.

0.

0.

0.

5

6

7

8

9

1.779785

1.7791977

1.7799384

1.7793686

1.779058

1.77928

1.77196

1.798198

0.

0.

0.

0.

0.

0.

0.

0.

0.

1.

1

2

3

4

5

6

7

8

*

*

*

*

*

*

*

*

8.31366

8.30743

8.30815

8.30803

8.30793

8.30804

8.3067

8.31625

1. 8

* component 709 - feedwater source

7090000 feedwtr tmdpvol

7090101 1.Oe6 1.0 0.0 0.0 0.0 0.0 0.0 0.0 11

7090200 103 0

7090201 0.0 6.910e6 491.1

* component 78 - top of steam dome

0780000

0780101

0780200

tstmdom snglvol

0.0 0.4 0.13404

0 6952032. 1247984.

0.0 90. 0.4 4.57e-5 .653 00

2583424. 1.

* component 79 - steamline

0790000

0790001

0790101

0790201

0790301

0790401

0790601

0790701

0790801

0790901

0791001

stmline pipe

2

0.0 2

0.0 1

15.825 2

34.25e-3 2

-90. 2

-8.049 2

4.57e-5 0.0525

2.888 2.888

00 2

*volume areas

*junction areas

*volume lengths

*volume volumes

*vertical angles

*delta z

2 *roughness diam

I *junction loss coef

* fe

154
0791101

0791201

0791202

0791300

0791301

0791401

01000 1 *vcahs

0 6941284. 1247946. 2583452. 1.

0 6931772. 1247971. 2583498. 1.

0

6.25976 6.49588 0. 1 * .283683

.0525 .0. 1. 1. 1 -

0. 1

0. 2

* feedwater

* component 701 - feedwater junction

7010000

7010101

7010200

7010201

7010202

7010203

7010204

7010205

7010206

7010207

7010208

7010209

7010210

7010211

7010212

7010213

7010214

7010215

7010216

7010217

7010218

7010219

7010220

7010221

709000000

1

-1.Oe+75

-1.le+10

-1.0e+10

-1.Oe+9

-1.Oe+8

-1.0e+7

-1.Oe+6

-8.0e+5

-6.0e+5

-4.0e+5

-2.0e+5

0.0

2.0e+5

4.0e+5

6.0e+5

8.0e+5

1.0e+6

1.Oe+7

1.Oe+8

1.0e+9

1.Oe+10

"fedwtr"

075000000

0

0.0

0.0

-1.Oe+10

-1.Oe+9

-1.Oe+8

-1.Oe+7

-1.Oe+6

-8.0e+5

-6.0e+5

-4.0e+5

-2.0e+5

0.0

2.Oe+5

4.0e+5

6.0e+5

8.0e+5

1.Oe+6

1.0e+7

1.Oe+8

1.Oe+9

1.0e+10

tmdpjun 0.0

cntrlvar

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

0.0

0.0

0.0

0.0

0.0

0.0

273 * feedctl

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

0.0

0.0

0.0

0.0

0.0

0.0

* component 702 - junction between 11-tube and 4-tube regions

7020000

7020101

7020201

7020110

sgdwnc sngljun

076010000 077000000 .005836

0 3.3464 2.801928 0.

.0431 0. 1. 1.

1.5 1.5

* 8.25925

01000

155
* component 703 - downcomer to tube bundle

7030000

7030101

7030201

7030110

sgdcbot sngljun

077010000 070000000 .025761

0 .758816 .5368226 0.

.02 0. 1. 1.

1.0 0.5

* 8.30314

01000

* component 704 - steamdome to downcomer

7040000 sgdctop sngljun

7040101 073010000 074000000 .09648 0.0 0.0 01000

7040201 0 6.98816 .01109985 0. * 8.05694

7040110 .176 0. 1. 1.

* component 705 - tube bundle to steam dome

7050000 ristodm sngljun

7050101 070010000 071000000 .084496 0.0 0.0 01000

7050201 0 .1872706 .329899 0. * 8.31636

7050110 0.328 0. 1. 1.

* component 708 - top steam dome to steam line

7080000 tostmIn sngljun

7080101 078010000 079000000 .0011401 0.0 0.0 01100

7080201 0 6.396664 6.48532 0. * .2836816

7080110 .0381 0. 1. 1.

* component 706 - steamline outlet

7060000

7060101

7060201

7060300

7060301

7060401

7060402

079010000

1

276

"trb st n"

707000000

0.

srvvlv0

0.0

1.0

valve

1. 14e-3

.5234

0.0 0.0 00000

0

steamctl... tcctl

0. 0.0

9357.2735 0.0 * this must be doubled

156
7060110 .0525 0. 1. 1.

* component 707 - steamline sink volume

7070000 stmsink tmdpvol

7070101 1.Oe6 1.0 0.0 0.0 0.0 0.0 0.0 0.0 10

7070200 102 0

7070201 0.0 1.013e5 1.0

*steam generator secondary system components - single loop c

* component 80 - sg riser

080O000

0800001

0800101

0800201

0800301

0800302

0800303

0800304

0800305

0800306

0800307

0800401

0800402

0800403

0800404

0800405

0800406

0800407

0800601

0800801

0800901

0801001

0801101

0801201

0801202

0801203

0801204

0801205

tubebun

10

0.0 1

0.0 1

0.2

0.4

0.6

0.8

1.0

1.5

1.8025

0.01151

0.02303

0.03454

0.04605

0.05756

0.08635

0.10376

90.

4.57e-5

0.709

00100

01000

0 70

0 70

0 70

0 70

0 70

pipe

10

1

2

3

4

5

9

10

1

2

3

4

5

9

10

10

0.031

0.709

10

9

128456.

)26396.

23096.

'18676.

13236.

*volume areas

*junction areas

*volume lengths

*volume lengths

*volume lengths

*volume lengths

*volume lengths

*volume lengths

*volume lengths

*volume volumes

*volume volumes

*volume volumes

*volume volumes

*volume volumes

*volume volumes

*volume volumes

*vertiical angles

503 10 *roughness diam

9 *junction resistance

*flags pvbfe

*flags vcahs

1248771. 2582846. .04247T

1249808. 2582862. .079181

1250779. 2582890. .1003M

1251212. 2582926. .102146

1251169. 2582972. .100181

9

35

75

35

0.

0.

0.

0.

0.

1

2

3

4

5

157
0801206

0801207

0801208

0801209

0801210

-0801300

0801301

0801302

0801303

0801304

0801305

0801306

0801307

0801308

0801309

0801401

0

0

0

0

0

0

7016020.

7017640. - 6999476.

6991468.

6982900.

1250842.

1250435.

1250028.

1249626.

1249192.

2583030.

2583100.

2583166.

2583234.

2583306.

.137237

.1617664

.20956

.253402

.319663

0.

0.

0.

0.

0.

6

7

8

9

10

.291368

.2968235

.3058306

.318744

.3353457

.3635625

.3908196

.417346

.444791

.03503

.253318

.3436065

.414301

.485924

.542248

.6048185

.661324

.713936

.775627

.0.

0. 1

0. 2*

0. 3*

0. 4*

0. 5*

0. 6*

0. 7*

0. 8*

0. 9*

1.

8.3189

8.32017

8.32394

8.32663

8.32915

8.33147

8.33338

8.33501

8.33651

1. 9

* component 81 - lower steam dome

0810000

0810001

.0810101

0810201

0810301

0810302

0810303

0810401

0810402

0810403

0810601

0810801

0810901

0811001

081.1101

0811201

0811202

0811203

0811300

0811301

0811302

0811401

lstmdom

3

0.0

0.0

0.158

0.7925

0.900

0.010393

0.03861

0.04385

90.

4.57e-5

0.0 (

00000

01000 2

0 6J

0 6c

0 6c

0

.426618

.432377

.249

pipe

3

2

1

2

3

1

2

3

3

.249 D.0

)77848.

•65112.

)69880.

*volume area

*junction area

*volume length

*volume

*volume

*volume

volumes

volumes

volumes

3 *rough diam

2 *junction f-loss

* vol flags

* vcahs

1248987. 2583346. .

1248752. 2583374. .:

1248488. 2583418. .:

r-loss

1070403

124302.

1005756

0.1

0. 2

0. 3

1.271086 0. 1 * 8.28098

1.227373 0. 2 * 8.30996

0. 1. 1. 2

* component 82 - middle steam dome and separator

*

158
0820000

0820001

0820101

0820200

0821101 - 0822101

0823101

0821201

0822201

0823201

0821110

0822110

0823110

mstmdom branch

3 0

0.0 2.16 0.59549 0.0 90. 2.16 4.57e-5 ;-249

0 6953520. 1248202. 2583470. .64374

082010000 088000000 .502655 .816 .452 01000

082000000-- 083000000 44:915e-2--:060 -:014-01002-

00

081010000

-0.49608

.3790846

.50494

.800

.539

.249

082000000 4.8695e-2 0.0 0.0

.04985623 0. * .283642

2.01394252 0. * 8.05382

2.04995 0. * 8.2958

01000

0.

0.

0.

1. 1.

1. 1.

1. 1.

* component 83 - upper downcomer

0830000

0830101

0830200

updwnc snglvol

0.0 0.3375

0 6953596.

.14922 0.0 -90. -. 3375

1248164. 2583470. .594008

4.57e-5 .539 00

* component 84 - upper feedwater ring

0840000

0840101

0840200

ufwring snglvol

0.0 1.6055 0.15856

0 6965196. 1248192.

0.0 -90. -1.6055 4.57e-5 0.176 00

2583464. .388591

* component 85 - lower feedwater ring

0850000

0850001

0850101

0850200

0851101

0852101

0851201

0852201

0851110

0852110

lfwring branch

2 0

0.0 .8275 .08172 0.0 -90. -. 8275

0 6970192. 1246853. 2583416. .022155

084010000 085000000 .09648 0.0 0.0

085010000 086000000 3.0415e-2 .339 .459

.2679376 .09100312 0. * 8.05953

.651864 0.076746 0. * 10.24751

.176 0. 1. 1.

.05983 0. 1. 1.

4.57e-5 .176 00

01000

01000

* component 86 - 11 tube region

159
0860000

0860101

0860200

dclltube snglvol

0.0 1.9815 0.06336

0 6988432. 1247671.

0.0 -90.

2583348.

-1.9815 4.57e-5 .05983 00

.071796

, component 87 - sg-dc bottom part (4 tube region and bottom annulus)

0870000

0870001

0870101

0870201

0870301

0870302

0870303

0870304

0870305

0870306

0870307

0870401

0870402

0870403

0870404

0870405

0870406

0870407

0870601

0870801

0870901

0870902

0871001

0871101

0871201

0871202

0871203

0871204

0871205

0871206

0871207

0871208

0871209

0871300

0871301

0871302

0871303

0871304

0871305

dc4tube 1

9

0.0 E

0.0 8

1.481 1

1.5 4

1.0 , 0.8 E

0.6

0.4

0.2

8.6429e-3

8.7538e-3

5.8359e-3

4.6687e-3

3.5015e-3

2.3343e-3

4.0563e-3

-90.

4.57e-5

0.0 0

0.5 1

00100

01000

0 698

0 69.

0 700

0 70(

0 70)

0 701

0 702

0 702

0 70,

0

2.943655

2.940042

2.945814

2.941764

2.948793

)ipe

1

4

5

6

7

8

9

9

0.04:

1.0

1.0

9

8

56060.

15548.

15052.

14576.

[2532.

18268.

•2724.

•5876.

M420.

*volume areas

*junction areas

*volume lengths

*volume lengths

*volume lengths

*volume lengths

*volume lengths

*volume lengths

*volume lengths

*volume volumes

*volume volumes

*volume volumes

*volume volumes

*volume volumes

*volume volumes

*volume volumes

*vertiical angles

31 "9 *roughness diam

7 *junction resistance

8 *junction resistance

*flags pvbfe

*flags vcahs

1247739. 2583284. .0517&

1247816. 2583204. .004873

1247899. 2583124. .04678!

1247988. 2583046. .044761

1248050. 2582978. .04330(

1248102. 2582930. .04242

1248145. 2582894. .04358w

1248196. 2582866. .05988!

1248220. 2582846. .02781

14

51

0526

933

94

746

0.

0.

0.

0.

0.

0.

0.

0.

0.

1

2

3

4

5

6

7

8

9

1.79785

1.791977

1.799384

1.793686

1.79058

0.

0.

0.

0.

0.

1 *

2*

3*

4*

5*

8.31366

8.30743

8.30815

8.30803

8.30793

160
0871306

0871307

0871308

0871401

Z.947078

2.94953

2.944037

.0431

1.7928

1.7996

1.79198

0.

0. 6 * 8.30804

0. 7 * 8.3067

0. 8 * 8.31625

1. 1. 8

* component 809 - feedwater source

8090000

8090101

8090200

8090201

feedwtr tmdpvol

1.Oe6 1.0 0.0 0.0 0.0 0.0 0.0 0.0 11

103 0

0.0 6.910e6 491.1

* component 88 - top of steam dome

0880000 tstmdom snglvol

0880101 0.0 0.4 0.13404 0.0 90. 0.4 4.57e-5 .653

0880200 0 6952032. 1247984. 2583424. 1.

* component 89 - steamline

0890000 stmline pipe

0890001 2

0890101 0.0 2 *volume areas

0890201 0.0 1 *junction areas

0890301 15.825 2 *volume lengths

0890401 34.25e-3 2 *volume volumes

0890601 -90. 2 *vertical angles

0890701 -8.049 2 *delta z

0890801 4.57e-5 0.0525 2 *roughness diam

0890901 2.888 2.888 1 *junction loss coef

0891001 00 2 * fe

0891101 01000 1 *vcahs

0891201 0 6941284. 1247946. 2583452. 1. 0. 1

0891202 0 6931772. 1247971. 2583498. 1. 0. 2

0891300 0

0891301 6.25976 6.49588 0. 1 * .283683

0891401 .0525 0. 1. 1. 1

* feedwater

00

161
* component 801 - feedwater junction

8010000

8010101

8010200

8010201

8010202

8010203

8010204

8010205

8010206

8010207

8010208

8010209

8010210

8010211

8010212

8010213

8010214

8010215

8010216

8010217

8010218

8010219

8010220

8010221

809000000

1

-1.Oe+75

-1.le+10

-1.Oe+10

-1.Oe+9

-1.Oe+8

-1.Oe+7

-1.0e+6

-8.0e+5

-6.0e+5

-4.0e+5

-2.0e+5

0.0

2.0e+5

4.0e+5

6.0e+5

8.0e+5

1.Oe+6

1.Oe+7

1.Oe+8

1.0e+9

1.Oe+10

"fedwtr"

085000000

0

0.0

0.0

-1.0e+10

-1. Oe+9

-1.0e+8

-1.Oe+7

-1.Oe+6

-8.0e+5

-6.0e+5

-4.0e+5

-2.0e+5

0.0

2.0e+5

4.0e+5

6.0e+5

8.0e+5

1.Oe+6

1.Oe+7

1.Oe+8

1.0e+9

1.Oe+l0

tmdpjun 0.0-

cntrlvar

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

0.0

0.0

0.0

0.0

0.0

0.0

283 * feedctl

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

0.0

0.0

0.0

0.0

0.0

0.0

* component. 802 - junction between 11-tube and 4-tube regions

8020000 sgdwnc sngljun

8020101 086010000 087000000 .005836 1.5 1.5 01000

8020201 0 3.3464 2.801928 0. *" 8.25925

8020110 .0431 0. 1. 1.

* component 803 - downcomer to tube bundle

8030000 sgdcbot sngljun

8030101 087010000 080000000 .025761 1.0 0.5 01000

8030201 0 .758816 .5358226 0. * 8.30314

8030110 .02 0. 1. 1.

162
* component 804 - steamdome to downcomer

8040000

8040101

8040201

8040110

sgdctop sngljun

083010000 084000000 .09648 0.0 0.0 01000

- 0 6.98816 .01109985 0. * 8.05694

.176 0. 1. 1.

* component 805 - tube bundle to steam dome

8050000 ristodm sngljun

8050101 080010000 081000000 .084496 0.0 0.0 01000

8050201 0 .1872706 .329899 0. * 8.31636

8050110 0.328 0. 1. 1.

• component 808 - top steam dome to steam line

8080000 tostmln sngljun

8080101 088010000 089000000 .0011401 0.0 0.0 01100

8080201 0 6.396664 6.48532 0. * .2836816

8080110 .0381 0. 1. 1.

* component 806 - steamline outlet

8060000

8060101

8060201

8060300

8060301

8060401

8060402

8060110

089010000

1

"trb st n"

807000000

0.

srvvlv0

valve

1. 14e-3

.5234

0.0 0.0 00000

0

286 .&

0.0

1.0

.0525 0. 1. 1.

steamctl.. .tcctl

0. 0.0

9357.2735 0.0

* component 807 - steamline sink volume

8070000

8070101

8070200

8070201

stmsink tmdpvol l.Oe6 1.0 0.0 0.0 0.0 0.0

102 0

0.0 1.013e5 1.0

0.0 0.0 10

163
*reactor vessel heat structures

*core heater rod heat structures

10131000 12 8 2 1

10131100 0 1

10131101 4 0.00415

10131102 3 0.00475

10131201 2 4

10131202 1 7

10131301 1.0 4

10131302 0.0 7

10131401 623. 5

10131402 573. 8

10131501 0 0 0 0

10131502 0 0 0 0

10131503 0 0 0 0

10131504 0 0 0 0

10131505 0 0 0 0

10131506 0 0 0 0

10131507 0 0 0 0

10131508 0 0 0 0

10131509 0 0 0 0

10131510 0 0 0 0

10131511 0 0 0 0

10131512 0 0 0 0

10131601 013020000 0

10131602 013020000 0

10131603 013030000 0

10131604 013040000 0

10131605 013050000 0

10131606 013060000 0

10131607 013060000 0

10131701 1 0.076480 0

10131702 1 0.049032 0

10131703 1 0.068217 0

10131704 1 0.087402 0

10131705 1 0.105168 0

10131706 1 0.113701 0

10131707 1 0.113701 0

10131708 1 0.105168 0

10131709 1 0.087402 0

10131710 1 -0.068217 0

10131711 1 0.049032 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

0

0

0

0

1

2

3

4

5.

6

7

8

9

10

11

12

6.744 1

3.321 2

3.321 5

3.321 7

3.321 10

3.321 11

6.744 12

1

1

1

1

1

1

1

0

0

0

0

0

0

0

0

0

0

0

1

2

3

4

5

6

7

8

9

10

11

164
10131712 1 0.076480 0 0 12

10131801 0.0 10. 10. 0. 0. 0. 0. 1.0 12

10131901 1.178e-2 10. 10. 0. 0. 0. 0. 1.0 12

*core baffle heat structure

10141000 7 4 2 1 0.214572 0

10141100 0 1

10141101 3 .215772

10141201 1 3

10141301 0.0 3

10141401 588.8 4

10141501 013010000 00000 1 1 0.11 1

10141502 013020000 00000 1 1 0.788 2

10141503 013030000 00000 1 1 0.78 3

10141504 013040000 00000 1 1 0.52 4

10141505 013050000 00000 1 1 0.78 5

10141506 013060000 00000 1 1 0.788 6

10141507 013070000 00000 1 1 0.35 7

10141601 014010000 00000 1 1 0.11 1

10141602 014020000 00000 1 1 0.788 2

10141603 014030000 00000 1 1 0.78 3

10141604 014040000 00000 1 1 0.52 4

10141605 014050000 00000 1 1 0.78 5

10141606 014060000 00000 1 1 0.788 6

10141607 014070000 00000 1 1 0.35 7

10141701 0 0.0 0.0 0.0 7

10141801 0.0 10. 10. 0. 0. 0. 0. 1.0 7

10141901 0.0 10. 10. 0. 0. 0. 0. 1.0 7

l owest part of pressure vessel

10110000 1 4 2 1 0.250000 0

10110100 0 1

10110101 3 0.282000

10110201 1 3

10110301 0.0 3

10110401 558.8 4

10110501 011010000 00000 1 1 1.54900 1

10110601 000000000 00000 0 1 1.549 1

10110701 0 0.0 0.0 0.0 1

10110801 0.0 10. 10. 0. 0. 0. 0. 1.0 1

10110901 0.0 10. 10. 0. 0. 0. 0. 1.0 1

165
* lowest Znd-part of pressure vessel

10120000 1 4 2 1 0.171500 0

10120100 0 1

10120101 3 0.181500

10120201 1 3

10120301 0.0 3

10120401 558.8 4

10120501 012010000 00000 1 1 0.51985 1

10120601 022070000 00000 1 1 0.51985 1

10120701 0 0.0 0.0 0.0 1

10120801 0.0 10. 10. 0. 0. 0. 0. 1.0 1

10120901 0.0 10. 10. 0. 0. 0. 0. 1.0 1

* pressure vessel surrounded by core bypass volume

10140000

10140100

10140101

10140201

10140301

10140401

10140501

10140502

10140503

10140504

10140505

10140506

10140507

10140601

10140602

10140603

10140604

10140605

10140606

10140607

10140701

10140801

10140901

7 4

0 1

3

1 3

0.0 3

558.8 4

014010000

014020000

014030000

014040000

014050000

014060000

014070000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

0 0.0

0.0 10. 10.

0.0 10. 10.

2 1 0.171500 0

0.199500

00000

00000

00000

00000

00000

00000

00000

00000

00000

00000

00000

00000

00000

00000

0.0

0. 0. 0.

0. 0. 0.

1

1

1

1 :

1 :

1:

1

0

0

0

0: 0:

0:

0:

.0 7

1.0

1.0

1. 1

1-

1.

1.

1

1

1

I

1

1

1

7

7

0.12353

0.86882

0.86000

0.57334

0.86000

0.86882

0.12353

0.12353

0.86882

0.86000

0.57334

0.86000

0.86882

0.12353

1

2

3

4

5

6

7

1

2

3

4

5

6

7

0.

0

0 *

* upper part of pressure vessel

10990000 1

10990100 0

4 2 1 0.171500 0

1

166
10990101 3 0.199500

10990201 1 3

10990301 0.0 3

10990401 558.8 4

10990501 099010000 00000 1 1 0.55248 1

10990601 000000000 00000 0 1 --...0.55248---1

10990701 0 0.0 0.0 0.0 1

10990801 0.0 10. 10. 0. 0. 0. 0. 1.0 1

10990901 0.0 10. 10. 0. 0. 0. 0. 1.0 1

* upper plenum of pressure vessel

10150000 1 4 2 1 0.171500 0

10150100 0 1

10150101 3 0.199500

10150201 1 3

10150301 0.0 3

10150401 558.8 4

10150501 015010000 00000 1 1 1.02406 1

10150601 000000000 00000 0 1 1.02406 1

10150701 0 0.0 0.0 0.0 1

10150801 0.0 10. 10. 0. 0. 0. 0. 1.0 1

10150901 0.0 10. 10. 0. 0. 0. 0. 1.0 1

* extended upper plenum structure

10160000 1 4 2 1 0.171500 0

10160100 0 1

10160101 3 0.199500

10160201 1 3

10160301 0.0 3

10160401 558.8 4

10160501 016010000 00000 1 1 0.75747 1

10160601 000000000 00000 0 1 0.75747 1

10160701 0 0.0 0.0 0.0 1

10160801 0.0 10. 10. 0. 0. 0. 0. 1.0 1

10160901 0.0 10. 10. 0. 0. 0. 0. 1.0 1

* upper plenum to upper head side structure ( partl )

*=*=*==*=*=* *=*=*=*=*=* =* =*= *=*********,,,,•,,,

10161000 1 4 2 1 0.129000 0

10161100 0 1

10161101 3 0.146000

10161201 1 3

10161301 0.0 3

167
10161401

10161501

10161601

10161701

10161801

10161901

558.8 4

016010000

019010000

0 0.0

0.0 10. 10. -.0. 0 .10;.-10.

00000

00000

0.0

0. 0. 0.

0. 0. 0.

0.0 1

0. 1.0 1

0. 1.0 1

0.57534 1

0.57534 1

*upper plenum to upper head side structure ( part 2)

10162000 1 4 2 1 0.100000 0

1016Z100 0 1

10162101 3 0.105000

10162201 1 3

10162301 0.0 3

10162401 558.8 4

10162501 016010000 00000 1 1 0.86798 1

10162601 019010000 00000 1 1 0.86798 1

10162701 0 0.0 0.0 0.0 1

10162801 0.0 10. 10. 0. 0. 0. 0. 1.0 1

10162901 0.0 10. 10. 0. 0. 0. 0. 1.0 1

*upper plenum to upper head side structure ( part 3): rectangular

10163000 1 4 1 1 0.000000 0

10163100 0 1

10163101 3 0.010000

10163201 1 3

10163301 0.0 3

10163401 558.8 4

10163501 016010000 00000 1 1 0.01670 1

10163601 018010000 00000 1 1 0.01670 1

10163701 0 0.0 0.0 0.0 1

10163801 0.0 10. 10. 0. 0. 0. 0. 1.0 1

10163901 0.0 10. 10. 0. 0. 0. 0. 1.0 1

*upper plenum to upper head-side structure ( part 4): rectangular

10164000 1 4 1 1 0.000000 0

10164100 0 1

10164101 3 0.035000

10164201 1 3

10164301 0.0 3

10164401 558.8 4

10164501 016010000 00000 1 1 0.12900 1

10164601 019010000 00000 1 1 0.12900 1

168
10164701 0 0.0 0.0 0.0 1

10164801 0.0 10. 10. 0. 0. 0. 0. 1.0 1

10164901 0.0 10. 10. 0. 0. 0. 0. 1.0 1

*--upper head structure ( part 1 )

10180000 1 4 2 1 0.190000 0

10180100 0 1

10180101 3 0.218000

10180201 1 3

10180301 0.0 3

10180401 558.8 4

10180501 018010000 00000 1 1 0.37030 1

10180601 000000000 00000 0 1 0.37030 1

10180701 0 0.0 0.0 0.0 1

10180801 0.0 10. 10. 0. 0. 0. 0. 1.0 1

10180901 0.0 10. 10. 0. 0. 0. 0. 1.0 1

* upper head structure ( part 2 )

10190000 1 4 2 1 0.190000 0

10190100 0 1

10190101 3 0.218000

10190201 1 3

10190301 0.0 3

10190401 558.8 4

10190501 019010000 00000 1 1 2.72586 1

10190601 000000000 00000 0 1 2.72586 1

10190701 0 0.0 0.0 0.0 1

10190801 0.0 10. 10. 0. 0. 0. 0. 1.0 1

10190901 0.0 10. 10. 0. 0. 0. 0. 1.0 1

* upperhead to downcomer structure

10210000 3 4 2 1 0.024600 0

10210100 0 1

10210101 3 0.030150

10210201 1 3

10210301 0.0 3

10210401 558.8 4

10210501 021010000 00000 1 1 9.25200 1

10210502 021020000 00000 1 1 6.00900 2

10210503 021030000 00000 1 1 1.10200 3

10210601 000000000 00000 0 1 9.25200 1

10210602 000000000 00000 0 1 6.00900 2

169
10210603

10210701

10210801

10210901

000000000

0 0.0

0.0 10. 10.

0.0 10. 10.

00000

0.0

0. 0. 0.

0. 0. 0.

0 1

0.0 3

0. 1.0 3

0. 1.0 3

1.10200 3

* upper downcomer : connecting cold legs

10200000 1 4 2 1 0.125000 0

10200100 0 1

10200101 3 0.164150

10200201 1 3

10200301 0.0 3

10200401 558.8 .4

10200501 020010000 00000 1 1 0.92300 1

10200601 000000000 00000 0 1 0.923 1

10200701 0 0.0 0.0 0.0 1

10200801 0.0 10. 10. 0. 0. 0. 0. 1.0 1

10200901 0.0 10. 10. 0. 0. 0. 0. 1.0 1

internal trefoil shaped-p=i--*==,=,s iup**=*=, *d,=,==*=* =,,,= * internal trefoil shaped pieces in upper downcomer :Recangular

10201000

10201100

10201101

10201201

10201301

10201401

10201501

10201601

10201701

10201801

10201901

1 4

0 1

3

1 3

0.0 3

558.8 4

020010000

000000000

0 0.0

0.0 10. 10.

0.0 10. 10.

1 1 0.000000 0

0.003000

00000

00000

0.0

0. 0. 0.

0. 0. 0.

11

0 1

0.0 1

0. 1.0 1

0. 1.0 1

0.33000 1

0.33 1

************h*e****t*****=*=*=*=*=*=*=*=*=*=*=*=* *=*= * downcomier heat structure

10220000

10220100

10220101

10220201

10220301

10220401

10220501

10220502

10220503

10220504

6 4

0 1

3

1 3

0.0 3

558.8 4

022010000

022020000

022030000

022040000

2 1 0.086500 0

0.105000

00000

00000

00000

00000

1

1

1

1

1

1

1

1

1.41700

1.41700

1.41700

1.41700

1

2

3

4

170
10220505 022050000

10220506 022060000

10220601 000000000

10220602 000000000

10220603 000000000

10220604--- .000000000

10220605 000000000

10220606 000000000

10220701 0 0.0

10220801 0.0 10. 10.

10220901 0.0 10. 10.

00000

00000

00000

00000

00000

00000

00000

00000

0.0

0. 0.

0. 0.

1 1"

0 1

0 1

0 1

0 1

0 1 0 1

0.0 6

0. 1.0 6

0. 1.0 6

0.40900

0.58900

1.41700

1.41700

1.41700

1.41700

0.40900

0.58900

5

6

1

2

3

4

5

6

0.

0.

* lower downcomer : connecting lower plenum

10221000

10221100

10221101

10221201

10221301

10221401

10221501

10221601

10221701

10221801

10221901

1 4 2 1 0.199000 0

0 1

3

1 3

0.0 3

558.8 4

022070000

000000000

0 0.0

0.0 10. 10.

0.0 10. 10.

0.247000

00000

00000

0.0

0. 0. 0.

0. 0. 0.

1 1

0 1

0.0 1

0. 1.0 1

0. 1.0 1

0.80202 1

0.80202 1

* loop heat structures

* iht str no. 31, 32, 33

10311000

10311100

10311101

10311201

10311301

10311400

10311401

10311501

10311502

10311503

10311504

10311505

21 6 2 1 0.059 0

0 1

5 0.075

1 5

0.0 5

0

563.300 6

031010000 10000 1 1 1.1941

032010000 10000 1 1 0.5

033010000 10000 1 1 0.7977

033020000 0 1 1 1.4480

033030000 0 1 1 0.5506

1

2

3

4

5

171
10311506

10311507

10311508

10311509

10311510

10311511

10311512

10311513

10311514

10311515

10311516

10311517

10311518

10311519

10311520

10311521

10311601

10311602

10311603

10311604

10311605

10311606

10311607

10311608

10311609

10311610

10311611

10311612

10311613

10311614

10311615

10311616

10311617

10311618

10311619

10311620

10311621

10311701

10311801

10311901

034010000

034220000

041010000

042010000

043010000

043020000

043030000

044010000

044220000

051010000

052010000

053010000

053020000

053030000

054010000

054220000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

0

0.

0.

0

0

10000

10000

10000

0

0

0

0

10000

10000

10000

0

0

0

0

10000

10000

10000

0

0

0

0

10000

10000

10000

0

0

0

0

10000

10000

10000

0

0

0

0

0

10.0

10.0

1 1

1 1

1 1

1 1

1 1

1

1 1

1 1

1 1

1 1

1 1

1 1

1 1

1 1

1 1

1 1

0 1

0 1

0 1

0 1

0 1

0 0 11

0 1

0 1

0 1

0 1

0 1

0 1

0 1

0 1

0 1

0 1

0 1

0 1

0 1

0 1

0

10.0 0. 0.

10.0 0. 0.

0.7980

0.7980

1.1941

0.5

0.7977

i-..-m480-

0. 5506

0.7980

0.7980

1.1941

0.5941

0.7977

1.4480

0. 5506

0.7980

0.7980

1.1941

0.5

0.7977

1.4480

0.5506

0.7980

0.7980

1.1941

0.5

0.7977

1.4480

0.5506

0.7980

0.7980

1.1941

0.5941

0.7977

1.4480

0.5506

0.7980

0.7980

0

0. 1.

0. 1.

6

7

8

9

10

-11

12

13

14

15

16

17

18

19

20

21

1

2

3

4

5

6

7

8

9

10

11

12

13

14

15

16

17

18

19

20

21

21

21

21

0.

0.

x~xxxxxxx~x7~

*k ht str no. 35, 45, 55

10351000

10351100

10351101

10351201

15 6

0

5

1

2 1 0.059 0 1

0.075

5

172
10351301 0.0

10351400

10351401 559.000

10351501 035010000 0

10351502 035020000 0

10351503-..-035030000 0

10351504 035040000 0

10351505 035050000 10000

10351506 045010000 0

10351507 045020000 0

10351508 045030000 0

10351509 045040000 0

10351510 045050000 10000

10351511 055010000 0

10351512 055020000 0

10351513 055030000 0

10351514 055040000 0

10351515 055050000 0

10351601 000000000 0

10351602 000000000 0

10351603 000000000 0

10351604 000000000 0

10351605 000000000 0

10351606 000000000 0

10351607 000000000 0

10351608 000000000 0

10351609 000000000 0

10351610 000000000 0

10351611 000000000 0

10351612 000000000 0

10351613 000000000 0

10351614 000000000 0

10351615 000000000 0

10351701 0 0

10351801 0. 10.0

10351901 0. 10.0

5

0

6

1

1

1-

1

1

1

1

1

1

1

1

1

1

I

1

1

1

1

1

1

1

1

1

1

1

1

1

1

1

0

0.

0.

0. 4189

1. 94015 --2.22285

0.820

2.0697

0.4189

1.94015

2.22285

0.820

2.0697

0.4189

1.94015

2.22285

0.820

2.0697

0.4189

1. 94015

2.22285

0.820

2.0697

0.4189

1.94015

2. 22285

0.820

2.0697

0.4189

1.94015

2.22Z85

0.820

2.0697

0

0. 0. 1.

0. 0. 1.

3

4

5

6

7

8

9

10

11

12

13

14

15

1

2

3

4

5

6

7

8

9

10

11

12

13

14

15

15

15

15

10.0

I10.0

0.

0.

* ht str no. 36-1, 46-1, 56-1

*

10361000

10361100

10361101

10361201

10361301

10361400

10361401

3 6

0

5

1

0.0

2 1 0.059 0

0.060

5

5

0

559. 6

173
10361501 036010000 0 1 1 0.350 1

10361502 046010000 0 1 1 0.350 2

10361503 056010000 0 1 1 0.350 3

10361601 000000000 0 2777 1 0.350 1

10361602 000000000 0 2777 1 0.350 2

10361603 .. .000000000 0 *.2777 1- .0.350- 3

10361701 0 0 0 0 3

10361801 0.. 10.0 10.0 0. 0. 0. 0. 1. 3

10361901 0. 10.0 10.0 0. 0. 0. 0. 1. 3

* lht str no. 36-2, 46-2, 56-2

10362000 3 6 2 1 0.059 0

10362100 0 1

10362101 5 0.06008

10362201 1 5

1036Z301 0.0 5

10362400 0

10362401 559. 6

10362501 036010000 0 1 1 0.35 1

10362502 046010000 0 1 1 0.35 2

10362503 056010000 0 1 1 0.35 3

10362601 000000000 0 2778 1 0.35 1

10362602 000000000 0 2778 1 0.35 2

10362603 000000000 0 2778 1 0.35 3

10362701 0 0 0 0 3

10362801 0. 10.0 10.0 0. 0. 0. 0. 1. 3

10362901 0. 10.0 10.0 0. 0. 0. 0. 1. 3

* ht str no. 37, 38, 39

10371000 15 6 2 1 0.059 0

10371100 0 1

10371101 5 0.075

10371201 1 5

10371301 0.0 5

10371400 0

10371401 559.000 6

10371501 037010000 0 1 1 1.05 1

10371502 037020000 10000 1 1 8.59 2

10371503 038010000 10000 1 1 0.5 3

10371504 039010000 0 1 1 0.78406 4

10371505 039020000 10000 1 1 0. 53586 5

10371506 047010000 0 1 1 1.05 6

10371507 047020000 10000 1 1 8.59 7

174
10371508

10371509

10371510

10371511

10371512

10371513

10371514

10371515

10371601

10371602

10371603

10371604

10371605

10371606

10371607

10371608

10371609

10371610

10371611

10371612

10371613

10371614

10371615

10371701

10371801

10371901

048010000 10000 1 1

049010000 0 1 1

049020000 10000 1 1

057010000 0 1 1

057020000 10000 1 1

058010000 10000 1 -.

059010000 0 1 1

059020000 0 1 1

000000000 0 0 1

000000000 0 0 1

000000000 0 0 1

000000000 0 0 1

000000000 0 0 1

000000000 0 0 1

000000000 0 0 1

000000000 0 0 1

000000000 0 0 1

000000000 0 0 1

000000000 0 0 1

000000000 0 0 1

000000000 0 0 1

000000000 0 0 1

000000000 0 0 1

0 0 0

0. 10.0 10.0 0. 0. 0.

0. 10. 10. 0. 0. 0. 0.

0.5

0.78406

0.53586

1.05

8.59

0.78406

0.53586

1.05

8.59

0.5

0.78406

0. 53586

1.05

8.59

0.5

0.78406

0.53586

1.05

8.59

0.5

0.78406

0.53586

0

0. 1.

1. 15

8

9

10

11

12

-13

14

15

1

2.

3

4

5

6

7

8

9

10

11

12

13

14

15

15

15

* steam generator tubes heat structures (single loop)

10341000 20 4 2 1 0.00984

10341100 0 1

10341101 3 0.01111

10341201 3 3

10341301 0.0 3

10341401 560. 4

10341501 034020000 10000 1 0 .42042 1

10341502 034030000 10000 1 0 .84084 2

10341503 034040000 10000 1 0 1.26126 3

10341504 034050000 10000 1 0 1.68168 4

10341505 034060000 10000 1 0 2.10210 5

10341506 034070000 10000 1 0 3.15315 9

10341507 034110000 10000 1 0 1.52402 11

10341508 034130000 10000 1 0 3.15315 15

10341509 034170000 10000 1 0 2.10210 16

175
10341510 034180000 10000 1 0 1.68168 17

10341511 034190000 10000 1 0 1.26126 18

10341512 034200000 10000 1 0 .84084 19

10341513 034210000 10000 1 0 .42042 20

10341601 060010000 10000 1 0 .47468 1 .-10341602- -- -.060020000 10000 1 0 .94936 2

10341603 060030000 10000 1 0 1.42405 3

10341604 060040000 10000 1 0 1.89873 4

10341605 060050000 10000 1 0 2.37341 5

10341606 060060000 10000 1 0 3.56012 9

10341607 060100000 10000 1 0 1.72072 10

10341608 060100000 -10000 1 0 1.72072 11

10341609 060090000 -10000 1 0 3.56012 15

10341610 060050000 -10000 1 0 2.37341 16

10341611 060040000 -10000 1 0 1.89873 17

10341612 060030000 -10000 1 0 1.42405 18

10341613 060020000 -10000 1 0 .94936 19

10341614 060010000 -10000 1 0 .47468 20

10341701 0 0.0 0.0 0.0 20

10341801 0.01968 10. 10. 0. 0. 0. 0. 1.0 20

10341901 .03503 10. 10. 0. 0. 0. 0. 1.0 20 * d=inter tube dist.

*steam generator tubes heat structures : loop b

10441000 20 4 2 1

10441100 0 1

10441101 3 0.01111

10441201 3 3

10441301 0.0 3

10441401 . 560. 4

10441501 044020000 10000

10441502 044030000 10000

10441503 044040000 10000

10441504 044050000 10000

10441505 044060000 10000

10441506 044070000 10000

10441507 044110000 10000

10441508 044130000 10000

10441509 044170000 10000

10441510 044180000 10000

10441511 044190000 10000

10441512 044200000 10000

10441513 044210000 10000

10441601 070010000 10000

0.00984

1

1

1

1

1

1

1

1

1

1

1

1

1

1

0 .42042 1

0 .84084 2

0 1.26126 3

0 1.68168 4

0 2.10210 5

0 3.15315 9

0 1.52402 11

0 3.15315 15

0 2.10210 16

0 1.68168 17

0 1.26126 18

0 .84084 19

0 .42042 20

0 .47468 1

176
10441602 070020000 10000 1 0 .94936 2

10441603 070030000 10000 1 0 1.42405 3

10441604 070040000 10000 1 0 1.89873 4

10441605 070050000 10000 1 0 2.37341 5

10441606 070060000 10000 1 0 3.56012 9

10441607 070100000 10000 1 0 .1,.72072-. 10-

10441608 070100000 -10000 1 0 1.72072 11

10441609 070090000 -10000 1 0 3.56012 15

10441610 070050000 -10000 1 0 2.37341 16

10441611 070040000 -10000 1 0 1.89873 17

10441612 070030000 -10000 1 0 1.42405 18

10441613 070020000 -10000 1 0 .94936 19

10441614 070010000 -10000 1 0 .47468 20

10441701 0 0.0 0.0 0.0 20

10441801 0.01968 10. 10. 0. 0. 0. 0. 1.0 20

10441901 .03503 10. 10. 0. 0. 0. 0. 1.0 20 * d=inter tube dist.

*steam generator tubes heat structures( loop c)

10410

105411000

10541100

10541101

10541201

10541301

10541401

10541501

10541502

10541503

10541504

10541505

10541506

10541507

10541508

105415109

10541510

10541511

10541512

105415013

10541601

10541602

10541603

10541604

10541605

20 4 2 1

0 1

3 0.01111

3 3

0.0 3

560. 4

054020000 10000

054030000 10000

054040000 10000

054050000 10000

054060000 10000

054070000 10000

054110000 10000

054130000 10000

054170000 10000

054180000 10000

054190000 10000

054200000 10000

054210000 10000

080010000 10000

080020000 10000

080030000 10000

080040000 10000

080050000 10000

080060000 10000

0.00984

1

1

1

1

1

1

1

1

1

1

1

1

1

1

1

1

1

1.

1

0 .42042 1

0 .84084 2

0 1.26126 3

0 1.68168 4

0 2.10210 5

0 3.15315 9

0 1.52402 11

0 3.15315 15

0 2.10210 16

0 1.68168 17

0 1.26126 18

0 .84084 19

0 .42042 20

0 .47468 1

0 .94936 2

0 1.42405 3

0 1.89873 4

0 2.37341 5

0 3.56012 9

177
10541607 080100000 10000 1 0 1.72072 10

10541608 080100000 -10000 1 0 1.72072 11

10541609 080090000 -10000 1 0 3.56012 15

10541610 080050000 -10000 1 0 2.37341 16

10541611 080040000 -10000 1 0 1.89873 17

10541612- 080030000 -10000 1 0--1.42405 18

10541613 080020000 -10000 1 0 .94936 19

10541614 080010000 -10000 1 0 .47468 20

10541701 0 0.0 0.0 0.0 20

10541801. 0.01968 10. 10. 0. 0. 0. 0. 1.0 20-

10541901 .03503 10. 10. 0. 0. 0. 0. 1.0 20 * d=inter tube dist.

• iht str no. 60, 70, 80

10601000 30 6 2 1 0.028775 0

10601100 0 1

10601101 5 0.03555

10601201 1 5

10601301 0.0 5

10601400 0

10601401 560.0 6

10601501 060010000 0 1 1 0.2 1

10601502 060020000 0 1 1 0.4 2

10601503 060030000 0 1 1 0.6 3

10601504 060040000 0 1 1 0.8 4

10601505 060050000 10000 1 1 10 5

10601506 060090000 0 1 1 1.5 9

10601507 060100000 0 1 1 1.8025 10

10601508 070010000 0 1 1 0.2 11

10601509 070020000 0 1 1 0.4 12

10601510 070030000 0 1 1 0.6 13

10601511 070040000 0 1 1 0.8 14

10601512 070050000 10000 1 1 1.0 15

10601513 070090000 0 1 1 1.5 19

10601514 070100000 0 1 1 1.8025 20

10601515 080010000 0 1 1 0.2 21

10601516 080020000 0 1 1 0.4 22

10601517 080030000 0 1 1 0.6 23

10601518 080040000 0 1 1 0.8 24

10601519 080050000 10000 1 1 1.0 25

10601520 080090000 0 1 1 1.5 29

10601521 080100000 0 1 1 1.8025 30

10601601 000000000 0 0 1 0.2 1

10601602 000000000 0 0 1 0.4 2

10601603 000000000 0 0 1 0.6 3

178
10601604

10601605

10601606

10601607

10601608

10601609

10601610

10601611

10601612

10601613

10601614

10601615

10601616

10601617

10601618

10601619

10601620

10601621

10601701

10601801

10601901

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

0

0.

0.

0

0

0

0

0

0

0'

0

0

0

0

0

0

0

0

0

0

0

0

10.0

10.0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

10.0

10.0

1

1

1

1

1

1

1

1

1

1

1

1

1

1

1

1

1

1

0

0.

0.

0.8

1.0

1.5

1.8025

0.2

0.4

0.6

0.8

1.0

1.5

1.8025

0.2

0.4

0.6

0.8

1.0

1.5

1.8025

0

0. 0.

0. 0.

4

5

9

10

11

12

13

14

15

19

20

21

22

23

24

25

29

30

30

30

30

0.

0.

1. 1.

*

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

* ht str no. 61-1, 71-1, 81-1

10611000

10611100

10611101

10611201

10611301

10611400

10611401

10611501

10611502

10611503

10611601

10611601

10611603

10611701

10611801

10611901

3 6

0

5

1

0.0

560.

061010000

071010000

081010000

000000000

000000000

000000000

0

0.

0.

2 1 0.03290 0 1

0.04038

5

5

0

6

0

10000

0

0

0

0

0

10.0

10.0

1

1

1

0

0

0

10.0

10.0

1

1

1

1

1.

1

0

0.

0.

0.158 1

0.158 2

0.158 3

0.158 1

0.158 2

0.158 3

0 3

0. 0. 1. 3

0. 0. 1. 3

0.

0. *

* ht str no. 61-2, 71-2, 81-2

10612000 6 6 2 1 0.02499 0

179
10612100

10612101

10612201

10612301

10612400

10612401

10612501

10612502

10612503

10612504

10612505

10612506

10612601

10612602

10612603

10612604

10612605

10613606

10612701

10612801

10612901

0

5

1 0.0

1

0.03211

5

5

0

560. .6

061020000

061030000

071020000

071030000

081020000

081030000

000000000

000000000

000000000

000000000

000000000

000000000

0

0.

0.

0

10000

0

10000

0

0

0

0

0

0

0

0

1

1

1

1

1

1

0

0

0

0

0

0

1

1

1

1

1

1

1

1

1

1

1

1

0

0.

0.

0.7952

0.900

0.7952

0.900

0.7952

0.900

0.7952

0.900

0.7952

0.900

0.7952

0.900

0

0. 0.

0. 0.

1

2

3

4

5

6

1

2

3

4

5

6

6

6

6

0

10.0 10.0

10.0 10.0

0.

0.

1. 1.

* ht str no. 62. 72. 82

10621000

10621100

10621101

10621201

10621301

10621400

10621401

10621501

10621502

10621503

10621601

10621602

10621603

10621701

10621801

10621901

3 6

0

5

1

0.0

560.

062010000

072010000

082010000

000000000

000000000

000000000

0

0.

0.

2 1 0.1245 0

1

0.137

5

5

0

6

10000

10000

0

0

0

0

0

10.0

10.0

1

1

1

0

0

0

1

1

1

1

1

0

0. 0.

2.16 1

2.16 2

2.16 3

2.16 1

2.16 2

2.16 3

0 3

0. 0. 1. 3

0. 0. 1. 3

10.0

10.0

0.

0. *

* ht str no. 63, 73, 83

10631000 3 6 2 1 0.2695 0

180
10631100

10631101

10631201

10631301

10631400

10631401

10631501

10631502

10631503

10631601

10631602

10631603

10631701

10631801

10631901

0

5

1 0.0

560.

063010000

073010000

083010000

-000000000

000000000

000000000

0

0.

0.

10000

10000

0

0

0

0

0

10.0

10.0

1

0.282

5

5

0

6

1 1 1 1

1 1

0 1 0 1

0 1

0

10.0 0.

10.0 0.

2.16

2.16

2.16

.2.16

2.16

2.16

0

0.

0.

1

2

3

1

2

3

3

3

3

0.

0.

0.

0.

1. 1.

* lht str no. 64, 65, 74, 75, 84, 85

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

10641000

10641100

10641101

10641201

.10641301

10641400

10641401

10641501

10641502

10641503

10641504

10641505

10641506

10641601

10641602

10641603

10641604

10641605

10641606

10641701

10641801

10641901

6 6

0

5

1

0.0

550.

064010000

065010000

074010000

075010000

084010000

085010000

000000000

000000000

000000000

000000000

000000000

000000000

0

0.

0.

2 1 0.088 0 1

0.0955

5

5

0

6

10000

10000

10000

10000

10000

0

0

0

0

0

0

0

0

10.0

10.0

1 1

1 1

1 1

1 1 1 1

1 1

0 1 0 1

0 1

0 1

0 1

0 1

0

10.0 0.

10.0 0.

0.3375

0.8275

0.3375

0.8Z75

0.3375

0.8275

0.3375

0.8275

0.3375

0.8275

0.3375

0.8275

0

0.

0.

1

2

3

4

5

6

1

2

3

4

5

6

6

6

6

0.

0.

0.

0.

1. 1.

* lht str no. 66, 76, 86

10661000

10661100

10661101

3 6 2 1 0.02991 0

0

5

1

0.03741

181
10661201

10661301

10661400

10661401

10661501

10661502--

10661503

10661601

10661602

10661603

10661701

10661801

10661901

1 0.0

550.

066010000

076010000

086010000

000000000

000000000

000000000

0

0.

0.

10000

10000

0

0

0

0

0

10.0

10.0

5

5

0

6

1 1 1 1

1 1

0 1 0 1

0 1

0

10.0 0.

10.0 0.

1.9815

1.9815

1.9815

1.9815

1.9815

1.9815

0

0. 0.

0. 0.

1

2"

3

1

2

3

3

3

3

0.

0.

1. 1.

* iht str no. 68, 78, 88

10681000 3 6 2 1 0.3265 0

10681100 0 1

10681101 5 0.3365

10681201 1 5

10681301 0.0 5

10681400 0

10681401 560. 6

10681501 068010000 10000 1 1 0.4 1

10681502 078010000 10000 1 1 0.4 2

10681503 088010000 0 1 1 0.4 3

10681601 000000000 0 0 1 0.4 1

10681602 000000000 0 0 1 0.4 2

10681603 000000000 0 0 1 0.4 3

10681701 0 0 0 0 3

10681801 0. 10.0 10.0 0. 0. 0. 0. 1. 3

10681901 0. 10.0 10.0 0. 0. 0. 0. 1. 3

* iht str no. 67-1/8, 77-1/8, 87-1/8

10671000

10671100

10671101

10671201

10671301

10671400

10671401

10671501

10671502

24 6 2 1 0.04309 0

0

5

1 0.0

1

0.05109

5

5

0

6 1

1

550.0

067010000

067040000

10000 1

0 1

1.481

1.5

1

4

182
10671503

10671504

10671505

10671506

10671507

10671508

10671509

10671510

10671511

10671512

10671513

10671514

10671515

10671516

10671517

10671518

10671601

10671602

10671603

10671604

10671605

10671606

10671607

10671608

10671609

10671610

10671611

10671612

10671613

10671614

10671615

10671616

10671617

10671618

10671701

10671801

10671901

067050000

067060000

067070000

067080000

077010000

077040000

077050000

077060000

077070000

077080000

087010000

087040000

087050000

087060000

087070000

087080000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000

000000000 0

0.

0.

0000

10000 00000

10000 00000000000000000000000

11111

....

11111111111111111111111111110

0.

0.

1.0 

5

0.8 6

0.6 

7

0.4 

8

1.481 9

1.5- 12

1.0 13

0.8 14

0.6 15

0.4 16

1.481 17

1.5 20

1.0 21

0.8 22

0.6 23

0.4 24

1.481 

1

1.5 

4

1.0 

5

0.8 

6

0.6 

7

0.4 

8

1.481 9

1.5 12

1.0 13

0.8 14

0.6 15

0.4 16

1.481 17

1.5 20

1.0 21

0.8 22

0.6 23

0.4 24

0 24

0. 0. 1. 24

0. 0. 1. 24

0

10.0 10.0

10.0 10.0

0.

0.

* ht str no. 67-9, 77-9, 87-9

10672*00

10672100

10672101

10672201

10672301

10672400

3 6 2 1 0.08034 0

051

0.0

1

0.08784 550

183
10672401

10672501

10672502

10672503

10672601

10672602

10672603

10672701

10672801

10672901

557.

067090000

077090000

087090000

000000000

000000000

000000000

0

0.

0.

0

10000

0

0

0

0

0

10.0

10.0

6

1 1 1 1

1 1

0 1 0 1

0 1

0

10.0 0.

10.0 0.

0.2

0.2

0.2

0.2

0.2

0.2

0

0.

0.

1

2

3

1

2

3

3

3

3

0.

0.

0.

0.

1. 1.

* pressurizer heat structures

* iht str no. 91-1

10911000

10911100

10911101

10911201

10911301

10911400

10911401

10911501

10911601

10911701

10911801

10911901

1 6

0

5 1

0.0

563.

091010000

000000000

0

0.

0.

2 1 0.08093 0

1

0.09593

5

5

0

6

0

0

0

10.0

10.0

1 1

0 1

0

10.0 0.

10.0 0.

0.105

0.105

0

0.

0.

1

1

1

1*

1

0.

0.

0.

0.

1. 1.

* iht str no. 91-2

10912000 1 6 2 1 0.09974 0

10912100 0 1

10912101 5 0.11474

10912201 1 5

10912301 0.0 5

10912400 0

10912401 563. 6

10912501 091020000 0 1 1 0.892 1

10912601 000000000 0 0 1 0.892 1

10912701 0 0 0 0 1

10912801 0. 10.0 10.0 0. 0. 0. 0. 1. 1

10912901 0. 10.0 10.0 0. 0. 0. 0. 1. 1

184
ht str no. 91-3

10913000

10913100

10913101

10913201

10913301

10913400

10913401

10913501

10913601

10913701

10913801 10913901

2 6 2 1 0.10499 0

0

5

1

0.0

563.

091030000

000000000

0

0.

0.

1

0.11999

5

5

0

6

1 1

0 1

0

10.0 0.

10.0 0.

0

0

0

10.0

10.0

5.4145

5.4145

0

0.

0.

2

2

2

2

2

0.

0.

0.

0.

1. 1.

* ht str no. 91-4

10914000 1 6 2 1 0.08573 0

10914100 0 1

10914101 5 0.10073

10914201 1 5

10914301 0.0 5

10914400 0

10914401 563. 6

10914501 091050000 0 1 1 0.105 1

10914601 000000000 0 0 1 0.105 1

10914701 0 0 0 0 1

10914801 0. 10.0 10.0 0. 0. 0. 0. 1. 1

10914901 0. 10.0 10.0 0. 0. 0. 0. 1. 1

* ht str no. 90

10901000

10901100

10901101

10901101

10901301

10901301

10901401

10901501

10901502

10901503

10901601

10901602

10901603

3 6

0

5

1

0.0

563.

090010000

090020000

090030000

000000000

000,00000

000000000

2 1 0.02046 0 1

0.02916

5

5

0

6

0

0

0

0

0

0

1

1

1

0

0

0

1

1

1

1

1

1

0.850

6.256

2.690

0.850

6.256

2.690

1

2

3

1

2

3

185
10901701

10901801

10901901

0

0.

0.

0

10.0

10.0

0

10.0 0.

10.0 0.

0.

0.

0

0.

0.

3

0.1. 3

0.1. 3

, ht str no. 91-5 prizer htrs ht struct

10915000 2 3 2 1 0.0 0

10915100 0 1

10915101 2 0.00525

10915201 1 2

10915301 1.0 2

10915400 0

10915401 563. 3

10915501 0 0 0 0 0.0 2

10915601 91010000 10000 1 1 0.535 2

10915701 789 0.5 0.0 0.0 2

10915801 0. 10. 10. 0. 0. 0. 0. 1. 2

10915901 0. 10.0 10.0 0. 0. 0. 0. 1. 2

* power table

20200100 power 0

20200101 0.0 2.857e+6

* rcp heat loss

20277700 htrnrate 407

20277701 0. 159155.

20277800 htrnrate

20277801 0. 30315.

* pzr heater

20278900

20278901 power 407

0. 1400.

calulte=iqid*ev=s=n=res=r=e=a=*=*=*=*=*=*=*=*=* *=*=*a*m ge

* calculate liquid levels in pressurizer and steam generators

20500100 preslev sum

20500101 0.0 0.105

1.0 4.08 1

voidf 091010000

186
20500102

20500103

20500104

20500105

20500400

20500401

20500402

20500403

20500404

20500405

20500406

20500407

20500408

20500409

20500410

20500411

20500412

20500413

20500200

20500201

20500202

20500203

20500204

20500205

20500206

20500207

20500208

20500209

20500210

20500211

20500210

20500213

20500214

20500215

20500300

20500301

20500302

20500303

20500304

20500305

20500306

20500307

20500308

20500309

20500310

0.892

5.4145

5.4145

0.105

veslev sum

0.0 1.0

1.054

0.11

0.788

0.78

0.52

0.78

0.788

0.35

1.0195

0.117

2.713

0.4015

sgalev sum

0.0 0.2

0.4

0.6

0.8

1.0

1.5

1.5

1.5

1.5

1.8025

0.158

0.7925

0.9

2.16

0.4

sgblev sum

0.0 0.2

0.4

0.6

0.8

1.0

1.5

1.5

1.5

1.5

1.8025

voidf

voidf

voidf

voidf

1.0

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

1.0

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

1.0

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

091020000

091030000

091040000

091050000

10.421 1

011010000

012010000

013010000

013020000

013030000

013040000

013050000

013060000

013070000

099010000

015010000

016010000

018010000

10.60282 1

060010000

060020000

060030000

060040000

060050000

060060000

060070000

060080000

060090000

060100000

061010000

061020000

061030000

062010000

068010000

10.61266 1

070010000

070020000

070030000

070040000

070050000

070060000

070070000

070080000

070090000

070100000

187
20500311

20500312

20500313

20500314

20500315

20500500

20500501

20500502

20500503

20500504

20500505

20500506

20500507

20500508

20500509

20500510

20500511

20500512

20500513

20500514

20500515

20502200

20502201

20502202

20502203

20502204

20502205

20502206

20502207

20502208

20502209

20502212

20502213

20502214

20502215

20502216

20502217

20503300

20503301

20503302

20503303

20503304

20503305

20503306

20503307

0.158

0.7925

0.9

2.16

0.4

sgclev sum

0.0 0.2

0.4

0.6

0.8

1.0

1.5

1.5

1.5

1.5

1.8025

0.158

0.7925

0.9

2.16

0.4

sgalevd sum

0.0 1.481

1.5

1.5

1.5

1.0

0.8

0.6

0.4

0.2

1.9815

0.8275

1.6055

0.3375

1.08

0.4

sgblevd sum

0.0 1.481

1.5

1.5

1.5

1.0

0.8

0.6

voidf

voidf

voidf

voidf

voidf

1.0

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

1.0

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

1.0

voidf

voidf

voidf

voidf

voidf

voidf

voidf

071010000

071020000

071030000

072010000

078010000

10.61266 1

080010000

080020000

080030000

080040000

080050000

080060000

080070000

080080000

080090000

080100000

081010000

081020000

081030000

082010000

088010000

12.00412 1

067010000

067020000

067030000

067040000

067050000

067060000

067070000

067080000

067090000

066010000

065010000

064010000

063010000

062010000

068010000

12.00995 1

077010000

077020000

077030000

077040000

077050000

077060000

077070000

188
20503308

20503309

20503312

20503313

20503314

20503315

20503316

20503317

20504400

20504401

20504402

20504403

20504404

20504405

20504406

20504407

20504408

20504409

20504412

20504413

20504414

20504415

20504416

20504417

0.4

0.2

1.9815

0.8275

1.6055

0.3375

1.08

0.4

sgclevd sum

0.0 1.481

1.5

1.5

1.5

1.0

0.8

0.6

0.4

0.2

1.9815

0.8275

1.6055

0.3375

1.08

0.4

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

1.0

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

077080000

077090000

076010000

075010000

074010000

073010000

072010000

078010000

12.00995 1

087010000

087020000

087030000

087040000

087050000

087060000

087070000

087080000

087090000

086010000

085010000

084010000

083010000

082010000

088010000

* primary system masses

20515100

20515101

20515102

20515103

20515104

20515105

20515106

20515107

20515108

20515109

20515110

20515111

20514100

20514112

20514113

20514114

20514115

sgamasl

0.0

sum 1.0

0.0350607

2.068400e-3

4.136800e-3

6. 205200e-3

8.273600e-3

1.034200e-2

1.551300e-2

1.551300e-2

1.551300e-2

1.551300e-2

7.497950e-3

99.3376 1

rho 034010000

rho 034020000

rho 034030000

rho 034040000

rho 034050000

rho 034060000

rho 034070000

rho 034080000

rho 034090000

rho 034100000

rho 034110000

102.5563 1

rho 034120000

rho 034130000

rho 034140000

rho 034150000

sgamas2 sum 1.0

0.0 7.497950e-3

1.551300e-2

1.551300c-2

1.551300e-2

189
20514116

20514117

20514118

20514119

20514120

20514121

20514122

20515200

20515201

20515202

20515203

20515204

20515205

20515206

20515207

20515208

20515209

20515210

20515211

20514200 20514212

20514213

20514M1 20514215

20514216

20514217

20514218

20514219

20514220

20514221

20514222

20516100

20516101

20516102

20516103

20516104

20516105

20516106

20516107

20516108

20516109

20516110

20516111

20516200

1.551300e-2

1.034200e-2

8.273600e-3

6.205200e-3

4.136800e-3

2.068400e-3

0.0350607

sgbmasl sum 1.0

0.0 0.0350607

2.068400e-3

4.136800e-3

6.205200e-3

8.273600e-3

1.034200e-2

1.551300e-2

1.551300e-2

1.551300e-2

1.551300e-2

7.497950e-3

sgbmas2 sum 1.0

0.0 7.497950e-3

1.551300e-2

1.551300e-2

1.551300e-2

1.551300e-2

1.034200e-2

8.273600e-3

6.205200e-3

4.136800e-3

2.068400e-3

0.0350607

sgcmasl sum 1.0

0.0 0.0350607

2.068400e-3

4.136800e-3

6.205200e-3

8.273600e-3

1.034200e-2

1.551300e-2

1.551300e-2

1.551300e-2

1.551300e-2

7.497950e-3

rho

rho

rho

rho

rho

rho

rho

034160000

034170000

034180000

034190000

034200000

034210000

034220000

99.3376 1

rho 044010000

rho 044020000

rho 044030000

rho 044040000

rho 044050000

rho 044060000

rho 044070000

rho 044080000

rho 044090000

rho 044100000

rho 044110000

102.5563 1

rho 044120000

rho 044130000

rho 044140000

rho 044150000

rho 044160000

rho 044170000

rho 044180000

rho 044190000

rho 044200000

rho 044210000

rho 044220000

99.3376 1

rho 054010000

rho 054020000

rho 054030000

rho 054040000

rho 054050000

rho 054060000

rho 054070000

rho 054080000

rho 054090000

rho 054100000

rho 054110000

sgamas2 sum 1.0 102.5563 1

190
20516212

20516213

20516214

20516215

20516216

20516217

20516218

20516219

20516220

20516221

20516222

20515300

20515301

20515302

20515303

20515304

20515305

20515306

20515307

20515308

20515309

20515310

20515312

20515313

20515314

20515315

20515316

20515317

20515318

20515319

20515400

20515401

20515402

20515403

20515404 20515405

20515406

20515407

20515408

20515410

20515411

20515412

20515413

20515414

20515415

20515416

0.0 7.497950e-3

1.551300e-2

1.551300e-2

1.551300e-2

1.551300e-2

1.034200e-2

8.273600e-3.

6.205200e-3

4.136800e-3

2.068400e-3

0.0350607

rho

rho

rho

rho

rho

rho

rho

rho

rho

rho

rho

054120000

054130000

054140000

054150000

054160000

054170000

054180000

054190000

054200000

054210000

054220000

cormas

0.0

vesmas

0.0

sum 1.0 407.052 1

0.15323 rho 011010000

6.20907e-2 rho 012010000

4.70800e-3 rho 013010000

3.37264e-2 rho 013020000

3.33840e-2 rho 013030000

2.22560e-2 rho 013040000

3.33840e-2 rho 013050000

3.37264e-2 rho 013060000

1.80660e-2 rho 013070000

1.56310e-3 rho 014010000

1.11975e-2 rho 014020000

1.10838e-2 rho 014030000

7.38920e-3 rho 014040000

1.10838e-2 rho 014050000

1.11975e-2 rho 014060000

4.97350e-3 rho 014070000

9.13340e-2 rho 099010000

1.02950e-2 rho 015010000

sum 1.0 361.04 1

.15418 rho 016010000

8.08300e-3 rho 017010000

4.89190e-2 rho 018010000

8.92590e-2 rho 019010000

4.33233e-2 rho 020010000

3.78310e-3 rho 021010000

2.44140e-3 rho 021020000

9.69700e-4 rho 021030000

2.39771e-2 rho 022010000

2.39771e-2 rho 022020000

2.39771e-2 rho 022030000

2.39771e-2 rho 022040000

7.51150e-3 rho 022050000

1.08295e-2 rho 022060000

2.79758e-2 rho 022070000

191
20515500

20515501

20515502

20515503

20515504

20515505

20515600

20515601

20515602

20515603

20515604

20515605

20516600

20516601

20516602

20516603

20516604

20516605

20515700

20515701

20515702

20515703

20515704

20515705

20515706

*20515708

20515709

20515710

20515711

20515712

20515713

20515800

20515801

20515802

20515803

20515804

20515805

20515806

*20515808

20515809

20515810

20515811

20515812

hlamas

0.0

hlibmas

0.0

hlcmas

0.0

clamas

0.0

sum 1.0

1.305868e-2

5.46800e-3

8.724194e-3

1.583533e-2

6.021362e-3

sum 1.0

1.305868e-2

5.46800e-3

8.724194e-3

1.583533e-2

6.021362e-3

sum 1.0

1.305868e-2

5.46800e-3

8.724194e-3

1.583533e-2

6.021362e-3

sum 1.0

4.581000e-3

2.123175e-2

2.430950e-2

8.967000e-3

2.263400e-2

2.062890e-2

8.921154e-3

1.14828e-2

9.394024e-3

5.46800e-3

8.57448e-3

5.860165e-3

sum 1.0

4.581000e-3

2.123175e-2

2.430950e-2

8.967000e-3

2.2634OOe-2

2.06277890e-2

8.921154e-3

1. 14828e-2

9.394024e-3

5.46800e-3

8.57448e-3

34.57254 1

rho 031010000

rho 032010000

rho 033010000

rho 033020000

rho 033030000

34.57254 1

rho 041010000

rho 042010000

rho 043010000

rho 043020000

rho 043030000

34.57254 1

rho 051010000

rho 052010000

rho 053010000

rho 053020000

rho 053030000

108.3605 1

rho 035010000

rho 035020000

rho 035030000

rho 035040000

rho 035050000

rho 036010000

rho 362010000

rho 037010000

rho 037020000

rho 038010000

rho 039010000

rho 039020000

108.3605 1

rho 045010000

rho 045020000

rho 045030000

rho 045040000

rho 045050000

rho 046010000

rho 462010000

rho 047010000

rho 047020000

rho 048010000

rho 049010000

clbmas

0.0

192
20515813

20516800

20516801

20516802

20516803

20516804

20516805

20516806

20516809

20516810

20516811

20516812

20516813

20515900

20515901

20515902

20515903

20515904

20515905

20515906

20515907

.20515908

20519900

20519901

20519902

20519903

20519904

20519905

20519906

20519907

20519908

20519909

20519910

20519911

20519912

20519913

20519914

20519915

20533000

20533001

20533002

90531700

20531701

5.860165e-3 rho 049020000

clcmas

0.0

prsrmas

0.0

totmas

0.0

tvesmas

0.0

sum 1.0

4.581000e-3

2.123175e-2 2.430950e-2

8.967000e-3

2.263400e-2

2.062290e-2

1.14828e-2

9.394024e-3

5.46800e-3

8.57448e-3

5.860165e-3

sum 1.0

1.118650e-3

9.040600e-3

3.863750e-3

2.161600e-3

2.789000e-2

0.187535

0.187535

2.424500e-3

108.3605 1

rho 055010000

rho 055020000

rho 055030000

rho 055040000

rho 055050000

ho 056010000

rho 057010000

rho 057020000

rho 058010000

rho 059010000

rho 059020000

114.4755 1

rho 090010000

rho 090020000

rho 090030000

rho 091010000

rho 091020000

rho 091030000

rho 091040000

rho 091050000

1802.557 1

151

141

152

142

153

154

155

156

157

158

159

161

166

168

162

768.092 1

153

154

sum

1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0

cntrlvar

cntrlvar

cntrlvar

cntrlvar

cntrlvar

cntrlvar

cntrlvar

cntrlvar

cntrlvar

cntrlvar

cntrlvar

cntrlvar

cntrlvar

cntrlvar

cntrlvar

sum 1.0

1.0 cntrlvar

1.0 cntrlvar

sgasml sum 1.0 605.622 1

0.0 1.151e-2 rho 060010000

193
20531702

20531703

20531704

20531705

20531706

20531707

20531708

20531709

20531710

20531711

20531712

20531713

20531714

20531800

20531815

20531816

20531817

20531818

20531819

20531820

20531821

20531822

20531823

20531824

20531825

20531826

20531827

20531828

20531829

20531830

20531900

20531923

20531924

20532000

20532001

20532002

20532003

20532004

20532005

20532006

20532007

20532008

20532009

20532010

20532011

2.303e-2 rho

3.454e-2 rho

4.605e-2 rho

5.756e-2 rho

8.635e-2 rho

8.635e-2 rho

8.635e-2 rho

8.635e-2 rho

0.10376 rho

1.0393e-2 rho

3.861e-2 rho

4.385e-2 rho

0.59549 rho

sgasm2 sum 1.0 187,

0.0 0.14922 rho

0.15856 rho

8.172e-2 rho

6.336e-2 rho

8.6429e-3 rho

8.7538e-3 rho

8.7538e-3 rho

8.7538e-3 rho

5.8359e-3 rho

4.6687e-3 rho

3.5015e-3 rho

2.3343e-3 rho

4.0563e-3 rho

0.13404 rho

3.425e-2 rho

3.425e-2 rho

060020000

060030000

060040000

060050000

060060000

060070000

060080000

060090000

060100000

061010000

061020000

061030000

062010000

.0125 1

063010000

064010000

065010000

066010000

067010000

067020000

067030000

067040000

067050000

067060000

067070000

067080000

067090000

068010000

069010000

069020000

sgasmt

0.0

sgasml 0.0

sum 1.0 792.635 1

1.0 cntrlvar 317

1.0 cntrlvar 318

sum 1.0 605.622 1

1.151e-2 rho 070010000

2.303e-2 rho 070020000

3.454e-2 rho 070030000

4.605e-2 rho 070040000

5.756e-2 rho 070050000

8.635e-2 rho 070060000

8.635e-2 rho 070070000

8.635e-2 rho 070080000

8.635e-2 rho 070090000

0.10376 rho 070100000

1.0393e-2 rho 071010000

194
20532012

20532013

20532014

20532100

20532101

20532102

20532103

20532104

20532105

20532106

20532107

20532108

20532109

20532110

20532111

20532112

20532113

20532114

20532115

20532116

20532200

20532201

20532202

2053Z300 20532301

20532302

2053Z303 2053*304

20532305

20532306

20532307

20532308

20532309

20532310

20532311

20532312

20532313

20532314

20532400

20532415

20532416

20532417

20532418

20532419

3.861e-•

4.385e-:

0.59549

sgasmZ sum

0.0 0.14922

0.15856

8.172e-,

6.336e-'

8.6429e8.7538e8.7538e8.7538e5.8359e4.6687e3.5015e2.3343e4.0563e0.13404

3.425e-,

3.425e-'

rho 071020000

2 rho 071030000

rho 072010000

1.0 187.0125 1

rho 073010000

rho 074010000

rho 075010000

rho 076010000

-3 rho 077010000

-3 rho 077020000

-3 rho 077030000

-3 rho 077040000

-3 rho 077050000

-3 rho 077060000

-3 rho 077070000

-3 rho 077080000

-3 rho 077090000

rho 078010000

2 rho 079010000

2 rho 079020000

sgasmt sum 1.0 792.635 1

0.0 1.0 cntrlvar 320

1.0 cntrlvar 321

sgasml sum 1.0

0.0 1.151e-2

2.303e-2

3.454e-2

4.605e-2

5.756e-2

8.635e-2

8.635e-2

8.635e-2

8.635e-2

0.10376

1.0393e-2

3.861e-2

4.385e-2

0.59549

605.622 1

rho 080010000

rho 080020000

rho 080030000

rho 080040000

rho 080050000

rho 080060000

rho 080070000

rho 080080000

rho 080090000

rho 080100000

rho 081010000

rho 081020000

rho 081030000

rho 082010000

sgasm2 sum 1.0 187

0.0 0.14922 rho

0.15856 rho

8.172e-2 rho

6.336e-2 rho

8.6429e-3 rho

.0125 1

083010000

084010000

085010000

086010000

087010000

195
20532420

20532421

20532422

20532423

20532424

20532425

20532426

20532427

20532428

20532429

20532430

20532500

20532501

20532502

8.7538e-3

8.7538e-3

8.7538e-3

5.8359e-3

4.6687e-3

3.5015e-3

2.3343e-3

4.0563e-3

0.13404

3.425e-2

3.425e-2

rho

rho

rho

rho

rho

rho

rho

rho

rho

rho

rho

087020000

087030000

087040000

087050000

087060000

087070000

087080000

087090000

088010000

089010000

089020000

sgasmt sum 1.0 792.635 1

0.0 1.0 cntrlvar 323

1.0 cntrlvar 324

* self initialization cards

20526200

20526201

20526300

20526301

20526302

20526303

20526304

20526305

20527200

20527201

20527300

20527301

20527302

20527303

20527304

20527305

20528200

20528201

20528300

20528301

20528302

20528303

20528304

20528305

sgllsp function 1.0 820. 0

time 0 4

fwlcntl feedctl 1.0

cntrlvar 262

50.0 * sk

mflowj 606000000 *

mflowj 601000000 *

2.5 10.0 4.0 *sm=maxdt

sg2lsp function

time 0 4

fw2cntl feedctl 1.0

cntrlvar 272

50.0 * sk

mflowj 706000000 *

mflowj 701000000 *

2.5 10.0 4.0 *sm=-maxdt

.52514

cntrlvar 319

sgl steam out

sgl fw in

t6=1/int.gain

1.0 820. 0

.52514

cntrlvar 322

sg2 steam out

sg2 fw in

t6=4/int.gain

) 3 0.0 10.0

t5=1/prop.gain

) 3 0.0 10.0

t5=1/prop.gain

sg3lsp function 1.0 820. 0

time 0 4

fw3cntl feedctl 1.0

cntrlvar 282

50.0 * sk

mflowj 806000000 *

mflowj 801000000 *

2.5 10.0 4.0 *sm=maxdt

.52514

cntrlvar 325

0 3 0.0 10.0

sg3 steam out

sg3 fw in

t6=1/int.gain t5=1/prop.gain

196
* pressure setpoint for single loop sg

20526500 sglpsp function 1.0 6.91+6 0

20526501 time 0 2

20526600

20526601

20526602

20526603

20527500

20527501

20527600

20527601

20527602

20527603

20528500

205Z8501

20528602

20528601

20528602

20528603

stmlcntl steamctl

cntrlvar 265

1.5

50.0 2.0

-1.34e-6 .0238706 0 3

p 068010000

*sj

*t4=1/int.gain

0.0 1.0

t3=1/prop.gain

sg2psp

time

stm2cntl

function

0 2

1.0 6.91+6 0

steamctl -1.34e-6 .0238706. 0 3 0.0 1.0

cntrlvar 275

1.5

50.0 2.0

sg3psp function

time 0 2

stmlcntl steamctl

cntrlvar 285

1.5

50.0 2.0

p 078010000

*S

*t4=Yint.gain t5=1/prop.gain

1.0 6.91+6 0

-1.34e-6 .0238706 0 3

p 088010000

*sj

*t4=1/int.gain

0.0 1.0

t3=1/prop.gain

*sgl pressure setpoint table

20200200 power 0

20200201 0.0 6.91e6

*sgl mass

202OO40

20200401

setpoint table

power 0

0.0 820.0

* thermal properties

*thermal properties for stainless steel

* thermal conductivity

20100100 tbl/fctn 1 1

20100101 293. 13.9

20100102 373. 15.1

20100103 473. 16.7

20100104 573. 18.3

197
20100105 673. 19.8

20100106 873. 23.0

20100107 1073. 26.1

* volumetric specific heat

20100151 293. 3.58e6

20100152 373. 3.89e6

20100153 473. 4.10e6

20100154 573. 4.21e6

20100155 673. 4.26e6

20100156 873. 4.41e6

20100157 1073. 4.66e6

*thermal properties for boron nitride

20100200 tbl/fctn 2 2

* function for thermal conductivity

20100201 293. 2000. 24.818 -0.00276 0.0 0.0 0.0 0.0 0.0

* function for volumetric specific heat

20100251 293. 423. 1.22e6 1.4e3 0.0 0.0 0.0 0.0 0.0

20100252 423. 1173. 1.46e6 1.62e3 0.0 0.0 0.0 0.0 0.0

*thermal properties for inconel 600

* thermal conductivity

20100300 tbl/fctn 1 1

20100301 323. 14.9

20100302 373. 15.6

20100303 473. 17.2

20100304 673. 20.4

20100305 873. 23.7

20100306 1073. 27.4

* volumetric specific heat

20100351 323. 3.76e6

20100352 373. 3.86e6

20100353 473. 4.03e6

20100354 673. 4.26e6

20100355 873. 4.68e6

20100356 1073. 4.98e6

198
* This contains a RELAP5 model of the French experimental facility

* BETHSY. The intended use of the model is for simulation of BETHSY

* test 9.1.b which studies the 2 inch cold leg break without hpsi

* ans with delayed ultimate procedure.

*=•*=**=**=**==*==*==*==*==* *= **=*= •€ *=*=*-'*=*=**•**•,

* transient input deck of bethsy test 9.1.b

= 2 inch cold leg break : bethsy test 9.1.b

100 restart transnt

101 run

102 si si

103 9283

105 2. 4.

201 2500. l.e-6 0.5 3 10 2000 1000

* minor edit variables

301 voidg 031010000

302 voidg 039010000

303 voidg 041010000

304 voidg 049010000

305 voidg 051010000

306 voidg 059010000

307 cntrlvar 111

308 cntrhvar 112

309 cntrlvar 113

310 cntrlvar 114

311 cntrlvar 311

312 cntrIvar 100

313 cntrlvar 51

314 cntrlvar 95

315 cntrlvar 63

316 cntrlvar 96

317 cntrlvar 52

318 cntrlvar 102

319 cntrlvar 103

320 cntrlvar 97

321 cntrlvar 53

322 cntrlvar 105

323 cntrlvar 106

324 cntrlvar 98

325 cntrlvar 316

326 cntrlvar 60

199
327 cntrlvar 314

328 cntrlvar 500

329 cntrlvar 326

330 cntrlvar 70

331 cntrlvar 399

332 cntrlvar 501

333 cntrlvar 336

334 cntrlvar 80

335 cntrlvar 334

336 cntrlvar 502

337 cntrlvar 73

338 cntrlvar 768 * time integrated break flow

339 cntrlvar 738

340 cntrlvar 319

341 cntrlvar 323

342 cntrlvar 326

343 cntrlvar 721

344 cntrlvar 722

345 p 068010000

346 p 078010000

347 p 088010000

348 p 091050000

349 p 721010000

350 p 722010000

351 mflowj 022030000

352 cntrlvar 34

353 cntrlvar 35

354 cntrlvar 36

355 mflowj 768000000

356 mflowj 608000000

357 mflowj 708000000

358 mflowj 808000000

359 mflowj 732000000

360 mflowj 735000000

361 sathf 037010000

362 sathg 037010000

363 tempf 020010000

364 tempf 015010000

365 tempf 019010000

366 tempf 018010000

367 tempf 033010000

368 tempf 038010000

369 tempf 043010000

370 tempf 048010000

371 tempf 053010000

372 tempf 058010000

373 tempf 060010000

374 tempf 070010000

200
375 tempf 080010000

376 httemp 013100708

377 httemp 013100808

378 httemp 013100908

379 httemp 013101008

380 httemp 013101108

381 httemp 013101208

382 cntrlvar 901

383 pmpvel 036

384 pmpvel 046

385 pmpvel 056

386 cntrlvar 888

387 cntrlvar 818

388 cntrlvar 821

389 cntrlvar 889

390 cntrlvar 1

391 cntrlvar 2

392 cntrlvar 22

393 cntrlvar 199

394 cntrlvar 12

395 mflowj 605000000

396 cntrlvar 13

397 cntrlvar 14

398 cntrlvar 15

399 cputime 0

* trips

407 discard

507 discard

501 time 0 ge null 0 0.0 1 cl break

502 p 91050000 it null 0 1.31e7 1 *scram signal

503 time 0 ge timeof 502 17.0 1 * core power trip

504 p 91050000 it null 0 1.19e7 1 * si signal

505 time 0 ge timeof 504 6.0 1 tbn bypass & main feed off

506 time 0 ge timeof 504 30.0 1 * aux feed on

507 time 0 ge timeof 504 300.0 1 * pump coastdown

508 cntrlvar 901 ge null 0 823.15 1 * opening of steam dump

509 p 91050000 gt null 0 1.46e6 n * accumulator isolation

510 tempf 013070000 It null 0 450.1 1 * transnt termination

511 p 91050000 It null 0 2.5e6 1 * transnt termination

512 cntrlvar 740 it null 0 20.0 1 * transnt termination

513 cntrlvar 22 It null 0 13.72 n * auxfeed on

514 cntrlvar 33 it null 0 13.72 n * auxfeed on

515 cntrlvar 44 it null 0 13.72 n * auxfeed on

201
516 p 91050000 It null 0 0.91e6 1 . ipsi

518

519

520

*600

time 0

p 91050000

time 0

it timeof

it null 0

ge timeof 504

505 0.0

4.16e6

1000. 1

n 0. * tbn bypass & aux off

n * accum on

*rcp heater reduced

666

603 506 and 513 n

604 506 and 514 n

605 506 and 515 n

608 509 and 519 n

*666 510 and 511

*

*

*

auxfeed-a on

auxfeed-b on

auxfeed-c on

* accum on

n * transient termination

* ********•* **   ** •******* ****** *****   ** •************ ************ **•**

* hydrodynamic components

* component 36 - inlet portion of single loop pump

0360000

0360101

0360108

0360109

0360200

0360201

0360202

0360110

0360111

0360301

0360302

pumpa pump 0.0 0.350 0.02062 0.0

035010000 1.0936e-2 0.0

037000000 1.0936e-2 0.0

0 15518260. 1253919.

0 6.23355 6.51145 0.

0 6.224798 6.504798 0.

.118 0. 1. 1.

.118 0. 1. 1.

0 0 0

311. 0.94578 6.3056e-2 78.

45.518 0.232 00000

0.0 01000

0.0 01000

2449436. 0.

* 3.39762

* 3.397625

-1 0 0

144.75 37.3 750.0

1 0. 0. 4.65e-2 0. 0

* bethsy pump single phase homologous curves

0361100 1

0361101

0361102

0361103

0361200 2

0361201

0361202

0361203

0361300 1

0361301

1 0.0 1.3257

0.5 1.2603

0.8 1.1279

0.925 1.0583

1 0.0 0.5139

0.5 0.7610

0.8 0.9093

0.925 0.9710

2 0.0 -0.5772

0.5 • 0.0733

0.1 1.3317 0.2 1.3273

0.6 1.2223 0.7 1.1780

0.825 1.1146 0.85 1.1009

0.95 1.0437 0.975 1.0287

0.1 0.5633 0.2 0.6128

0.6 0.8105 0.7 0.8599

0.825 0.9216 0.85 0.9340

0.95 0.9834 0.975 0.9957

0.1 -0.4471 0.2 -0.3169

0.6 0.2035 0.7 0.3572

0.3 1.3135

0.75 1.1536

0.875 1.0870

0.987 1.0215

0.3 0.6622

0.75 0.8846

0.875 0.9463

0.987 1.0017

0.3 -0.1868

0.75 0.4471

0.4 1.2909

0.775 1.1409

0.9 1.0728

1.0 1.0135

0.4 0.7116

0.775 0.8969

0.9 0.9587

1.0 1.0081

0.4 -0.0567

0.775 0.4951

202
0361302

0361303

0361400 2

0361401

0361402

0361403

0361500 1

0361600 2

0361700 1

0361701

0361702

0361703

0361800 2

0361900 1

0362000 2

0362100 1

0362101

0362102

0362103

0362200 2

036Z300 1

0362400 2

0362500 1

0362600 2

0363O00

0363001

0363002

0363100

0363101

0363102

0.8

0.92!

2 0.0

0.5

0.8

0. 92!

3 -1.

3 -1.

4 -1.0

-. 50( -. 221, -. 10(

4 -1.0

5 0.0

5 0.0

6 .0

.125

.250

.600

6 0.0

7 -1.C

7 -1.(C

8 -1.(

8 -1.C

0 o.a

0.4

1.0

0 0.0

0.4

1.0

0.5450

5 0.8238

-0.5772

0.2362

0.7243

5 0.8972

1.3257

0.5139

1.3257

) 1.0978

j 0.9725

) 0.9156

0.5139

1.3257

0.5139

0.8700

0.9269

0.9839

1.1434

0.5139

1 0.1

)-1.5

) 0.1

-1.5

0.0

1.0

0.0

0.0

1.0

0.0

0.825 0.5969 0.85

0.95 0.8852 0.975

0.1 -0.4145 0.2

0.6 0.3989 0.7

0.825 0.7579 0.85

0.95 0.9333 0.975

0.0 1.3257

0.0 0.5139 -. 900 1.2801 -. 800 -. 400 1.0522 -. 300 -. 200 0.9611 -. 175 -. 075 0.9042 -. 050

0.00 0.5139

1.00 1.3257

1.00 0.5139

.025 0.8814 .050 0.

.150 0.9383 .175 0.

.275 0.9953 .300 1.

.700 1.1889 .800 1.

1.000 0.5139

0.0 1.3257

0.0 .5139

0.0 -. 5772

0.0 -. 5772

0.6508

0.9485

-0.2518

0.5616

0.7915

0.9707

1.2346

1.0067

0.9497

0.89,8

0.875 0.7066

0.987 0.9795

0.3 -0.0891

0.75 0.6429

0.875 0.8263

0.987.0.9886

0

1

0

0.

0,

i.

-. 700

-. Z75 -. 150 -. 025

1.1889

0.9953

0.9383

0.8814

.9 0.7643

.0 1.0135

.4 0.0735

.775 0.6836

.9 0.8611

.0 1.0081

600 1.1434

.250 0.9839

125 0.9269

).00 0.8700

0.9156

0.9725

1.0978

1.3257

8928

9497

0067

2346

.075

.200

.400

.900

0.9042

0.9611

1.0522

1.2801

.100

.225

.500

1.00

0.1 0.0 0.2 0.0 0.3 0.5

0.6 1.0 0.8 1.0 0.9 1.0

0.1 0.0 0.2 0.0 0.3

0.6 1.0 0.8 1.0 0.9

0.5

1.0

*

two-phase difference tables from semiscale

0364100 1

0364101

0364102

0364200 1

0364201

0364300 1

0364301

0364302

0364400 1

0364401

0364402

0364500 1

0364501

0364502

1 0.0

0.5

0.9

2 0.0

0.4

3 -1.0

-0.7

-0.25

4 -1.0

-0.7

-0.35

5 0.0

0.4

0.8

0.00

1.02

0.94

0.00

0.21

-1.06

-2.36

-1.69

-1.16

-0.31

0.00

0.00

-0.65

-1.19

0.1

0.6

1.0

0.1

0.8

-0.9

-0.6

-0.1

-0.9

-0.6

-0.2

0.2

0.6

1.0

0.83

1.015

1.00

-0.04

0.67

-1.24

-2.79

-0.50

-0.78

-0.17

0.05

-0.34

-0.95

-1.47

0.2 1.09

0.7 1.01

0.2

0.9

-0.8

-0.5

0.0

-0.8

-0.5

0.0

0.00

0.80

-1.77

-2.91

0.00

-0.05

-0.17

0.11

0.3 0.11

1.0 1.0

-0.4. -2.67

203
0364600 1

0364601

0364602

0364700 1

0364800 1

0364900 2

0365000 2

0365100 2

0365200 2

0365300 2

0365400 2

0365500 2

0365600 2

6 0.0

0.4

0.8

7 0.0

8 0.0

1 0.0

2 0.0

3 0.0

4 0.0

5 0.0

6 0.0

7 0.0

8 0.0

0.11

0.13

-0.51

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.1

0.5

0.9

1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0

0.13

0.07

-0.91

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.25

0.6

1.0

0.15

-0.04

-1.47

0.7 -0.23

*pump speed controller for steady calculation

0366100

0366101

0366102

0366103

0366104

0366105

0366106

0366107

0366108

0366109

0366110

0366111

0366112

0366113

0366114

20542400

20542500

504

0.0

300.0

305.0

310.0

320.0

330.0

340.0

350.0

370.0

400.0

500.0

700.0

916.0

1000.0

294.1

294.1

201.0

141.3

113.0

87.9

75.3

62.8

47.1

37.6

21.9

15.7

10.4

0.0

mserr delete 0.

rcpspp delete 0.

0.

0.

0.

0.

0.

0.

0.

0.

0.

0.

* component 46 - inlet portion of single loop pump

0460000

0460101

0460108

0460109

0460200

04-60201

0460202

punipb pump

0.0 0.350 0.02062 0.0 45.518 0.232 00000

045010000 1.0936e-2 0.0 0.0 01000

047000000 1.0936e-2 0.0 0.0 01000

0 15518260. 1253919. 2449436. 0.

0 6.23355 6.51145 0. * 3.39762

0 6.224798 6.504798 0. * 3.397625

204
0460110

0460111

0460301

0460302

0466100

0466101

0466102

0466103

0466104

0466105

0466106

0466107

0466108

0466109

0466110

0466111

0466112

0466113

0466114

.118 0.

.118 0.

36 36

311. 0.94578

504

0.0

300.0

305.0

310.0

320.0

330.0

340.0

350.0

370.0

400.0

500.0

700.0

916.0

1000.0

36

6.3056e-2

-1 0 0

78. 144.75 37.3 750.0 0.

I

0. 4.65e-2 0. 0

294.1

294.1

201.0

141.3

113.0

87.9

75.3

62.8

47.1

37.6

21.9

15.7

10.4

0.0

* component 56 - inlet portion of broken loop pump

0560000

0560101

0560108

0560109

0560200

0560201

0560202

0560110

0560111

0560301

0560302

0566100

0566101

0566102

0566103

0566104

0566105

0566106

0566107

0566108

PUMPc PUMP

0.0 0.350 0.02062 0.0 45.518 0.232 00000

055010000 1.0936e-2 0.0 0.0 '01000

057000000 1.0936e-2 0.0 0.0 01000

0 15518260. 1253919. 2449436. 0.

0 6.23355

0 6.224798

.118 0.

.118 0.

36 36

311. 0.94578 6.

504

0.0

300.0

305.0

310.0

320.0

330.0

340.0

350.0

6.51145

6. 504798

1. 1

36

.3056-2

0.

0.

*

*

3.39762

3.397625

-1 0 0

78. 144.75 37.3 750.0

1

0. 0. 4.65e-2 0. 0.

294.1

294.1

201.0

141.3

113.0

87.9

75.3

62.8

205
0566109

0566110

0566111

0566112

0566113

0566114

370.0

400.0

500.0

700.0

916.0

1000.0

47.1

37.6

21.9

15.7

10.4

0.0

* break nodalization

*

*7000000

*7000101

*7000201

*7670000

*7670001

*7670101

*7670301

*7670601

*7670801

*7671001

*7671101

*7671201

*7671300

*7671301

7680000

7680101

7680102

7680201

7680300

7680301

9000000

9000101

9000102

9000200

9000201

breakjn

037010000

1 0.

breakpp

2

1.6619e-3

0.7953

0.0

4.0e-5

00 2

01000

003 15.

sngljun

767000000

0. 0.

2.083e-5 0. 100. 01100

pipe

2

2

2

0.0 2

565.0 0. 0. 0. 2

1

5e6

1

0. 0. 0. 1

breakvlv

037010000

0.85 1.

1 0.

trpvlv

501

containm

1.Oe+8 10.0

0.0 0.

002

0.0 0.11

valve

900000000 2.0830e-5 0. 0. 00100

0. 0.

tmdpvol

0. 0.

00

Ole6 1.0

0. 0.

* aux feedwater

******t***************d***pvo*l***********

7110000

7110101

7110200

7110201

auxfeeda

10.0 5.0

3

0. 5.9e6

tmdpvol

0. 0.

307.15

0. 0. 0. 0 00

206
7120000 auxfeeda tmdpjun

7120101 711000000 065000000 0.004

7120200 1 506 cntrlvar 13

7120201 -1.0 0. 0. 0.

7120202 0.0 0.30451 0. 0.

7120203 13.32 0.30451 0. 0.

7120204 13.42 0.22863 0. 0.

7120205 13.52 0.15275 0. 0.

7120206 13.62 0.07687 0. 0.

7120207 13.72 0.0 0. 0.

7120208 14.00 0.0 0. 0.

7120209 20.00 0.0 0. 0.

7130000 auxfeedb tmdpvol

7130101 10.0 5.0 0. 0. 0. 0. 0. 0 00

7130200 3

7130201 0. 5.9e6 307.15

7140000 auxfeedb tmdpjun

7140101 713000000 075000000 0.004

7140200 1 506 cntrlvar 14

7140201 -1.0 0. 0. 0.

7140202 0.0 0.30451 0. 0.

7140203 13.32 0.30451 0. 0.

7140204 13.42 0.22863 0. 0.

7140205 13.52 0.15275 0. 0.

7140206 13.62 0.07687 0. 0.

7140207 13.72 0.0 0. 0.

7140208 14.00 0.0 0. 0.

7140209 20.00 0.0 0. 0.

7150000 auxfeedc tmdpvol

7150101 10.0 5.0 0. 0. 0. 0. 0. 0 00

7150200 3

7150201 0. 5.9e6 307.15

7160000 auxfeedc tmdpjun

7160101 715000000 085000000 0.004

7160200 1 605 cntrlvar 15

7160201 -1.0 0. 0. 0.

7160202 0.0 0.30451 0. 0.

7160203 13.32 0.30451 0. 0.

7160204 13.42 0.22863 0. 0.

7160205 13.52 0.15275 0. 0.

7160206 13.62 0.07687 0. 0.

7160207 13.72 0.0 0. 0.

7160208 14.00 0.0 0. 0.

207
7160209 20.00 0.0 0. 0.

* accumulator injection

7210000

7210101

7210200

7211101

7212200

7220000

7220101

7220200

7221101

7222200

accub accum

0.0 8.376 0.423 0.0

4.18e6 290.15

048000000 1.14e-3 19.0

0.2562 0.0 21.0 9.780

accuc accum

0.0 8.376 0.423 0.0

4.18e6 290.15

058000000 1.14e-3 19.0

0.2562 0.0 21.75 9.780

90.0 8.376 3.3e-5 0. 00

19.0 0

0.00927 0 0 0 608

90.0 8.376 3.3e-5 0. 00

19.0 0

0.00927 0 0 0 608

* component 48 - single loop accumulator nozzle

0480000

0480001

0480101

0480200

0481101

0482101

0483101

0481201

0482201

0483201

0481110

0482110

0483110

accnoza branch

3 0

1.0936e-2 0.5 0.0 0.0 0.0

003 15737388. 561.3

047010000 048000000 1.0936e-2

048010000 049000000 1.0936e-2

733010000 048000000 1.0936e-2

6.2291 6.2291 0.0

6.2291 6.2291 0.0

0.0 0.0 0.0

0.118 0.0 1.0 1.0

0.118 0.0 1.0 1.0

0.118 0.0 1.0 1.0

0.0 4.57e-5 .118 00000

0.0

0.0

0.0

0.0

0.0

0.0

01000

01000

01000

* component 58 - single loop accumulator nozzle

0580000

0580001

0580101

0580200

0581101

0582101

0583101

accnozc branch

3 0

1.0936e-2 0.5 0.0 0.0 0.0

003 15737388. 561.3

057010000 058000000 1.0936e-2

058010000 059000000 1.0936e-2

736010000 058000000 1.0936e-2

0.0 4.57e-5 .118 00000

0.0 0.0 01000

0.0 0.0 01000

0.0 0.0 01000

208
0581201

0582201

0583201

0581110

0582110

0583110

6.2291

6.2291

0.0

0.118

0.118

0. 118

6.2291

6.2291

0.0

0.0 1.0

0.0 1.0

0.0 1.0

0.0

0.0

0.0

1.0

1.0

1.0

* low pressure safety injection

7310000

7310101

7310200

7310201

7320000

7320101

7320200

7320201

7320202

7320203

7320204

7320205

7320206

7320207

7320208

7320209

7320210

7320211

7320212

7330000

7330101

7330102

7330200

7340000

7340101

7340200

7340201

7350000

7350101

7350200

7350201

7350202

7350203

Ipsib

4.375

3

0.0

tmdpvol

10. 0. 0. 0. 0. 0. 0. 00

1. 013e5 307.15

lpsib tmdpjun

731000000 733000000 2.55e03

1 516

-1.0

0.

0. 1e6

0.2e6

0.3e6

0.4e6

0.5e6

0. 6e6

0.7e6

0.8e6

0. 9e6

0.91e6

0

p 0910500

0.

1.9749 0

1.8633 0

1.7445 0

1.6169 0

1.4785 0

1.3256 0

1.1527 0

0.9487 0

0.6866 0

0.2070 0

0.0 0

0

0.

0.

0.

0.

0.

0.

0.

0.

0.

0.

0.

0.

0. 0. 0. 3.33e-5 lpsijun snglvo.

2.55e-3 16.0 0

0.0 00

0 15738000.0 1253920. 2442260. 0.0

lpsic

4.375

3

0.0

tmdpvol 10. 0. 0. 0. 0. 0. 0. 00

1.013e5 307.15

lpsib tmdpjun

734000000 736000000 2.55e03

1 516 p 091050000

-1.0 0. 0. 0.

0. 1.9749 0. 0.

0.1e6 1.8633 0. 0.

209
7350204 0.2e6 1.7445 0. 0.

7350205 0.3e6 1.6169 0. 0.

7350206 0.4e6 1.4785 0. 0.

7350207 0.5e6 1.3256 0. 0.

7350208 0.6e6 1.1527 0. 0.

7350209 0.7e6 0.9487 0. 0.

7350210 0.8e6 0.6866 0. 0.

7350211 0.9e6 0.2070 0. 0.

7350212 0.91e6 0.0 0. 0.

7360000 lpsijun snglvol

7360101 2.55e-3 16.0 0. 0. 0. 0. 3.33e-5

7360102 0.0 00

7360200 0 15738000.0 1253920. 2442260. 0.0

* description of primary system components

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

* component 93 trip valve for pzr steady state

0930000 pzrvlv delete

* component 94 time dependent volume for pzr stp

0940000 pzr-tmdp delete

, steam generator secondary system components

20526200 sgllsp delete 0.0 0. 0. 0. 0. 0.0

20526300 fwlcntl delete 0. 0. 0. 0. 0. 0.

20527200 sg2lsp delete 0. 0. 0. 0. 0.0 0.0

20527300 fw2cntl delete 0. 0. 0. 0. 0. 0.

20528200 sg3lsp delete 0. 0. 0. 0. 0.0 0.0

20528300 fw3cntl delete 0. 0. 0. 0. 0. 0.

20526500 sglpsp delete 0. 0. 0. 0. 0.0 0.0

20526600 stmlcntl delete 0. 0. 0. 0. 0. 0.

20527500 sg2psp delete 0. 0. 0. 0. 0.0 0.0

20527600 stm2cntl delete 0. 0. 0. 0. 0. 0.

20528500 sg3psp delete 0. 0. 0. 0. 0.0 0.0

20528600 stm3cntl delete 0. 0. 0. 0. 0. 0.

210
* component 609 - feedwater source

*

6090000 feedwtr tmdpvol

6090101 1.0e6 1.0 0.0 0.0 0.0 0.0 0.0 0.0 11

6090200 103 0

6090201 0.0 6.910e6 491.1

* component 601 - feedwater junction

6010000

6010101

6010200

6010201

6010202

6010203

609000000

1

-1.0 (

0.0 0

100.0

"fedwtr'

065000000

518

tmdpjun

0.0

2.0

).52514 ].52514

0.0

0.0

0.0

0.0

0.0

0.0

* component 606 - steamline outlet

6060000

6060101

6060201

6060300

6060301

069010000

1

518

"trb st n"

607000000

0.

trpvlv

valve

4.94e-5

.52514

0.0 0.0 00000

0

* component 607 - steamline sink volume

6070000 stmsink tmdpvol

6070101 1.Oe6 1.0 0.0 0.0 0.0 0.0 0.0 0.0 10

6070200 102 0

6070201 0.0 0.10le6 1.0

* component 648 - steam bypass

6480000

6480101

6480200

6480201

stmbypas

069010000

1 505

-1.0

tmdpjun

607000000

p 68010000

0.0 0.0

1. 14e-3

0.0

211
6480202

6480203

6480204

7.03e+6

7.05e+6

7.06e+6

0.0 0.0

0.0 0.5

0.0 1.0

0.0

0.0

0.0

* component 610 - steam dump valve

6100000 stmdump tmdpjun

6100101 069010000 607000000 1.8506e-4

6100200 1 508 p 68010000

6100201 -1.0 0.0 0.0 0.0

6100202 0.1e6 0.0 0.0 0.0

6100203 7.03e6 0.0 0.55555 0.0

6100204 8.0e6 0.0 0.95238 0.0

* ***-* n** ******************w* s**o******************** *******a 

* component 709 - feedwater source

7090000

7090101

7090200

7090201

feedwtr tmdpvol

1.0e6 1.0 0.0 0.0 0.0 0.0

103 0

0.0 6.910e6 491.1

0.0 0.0 11

* component 701 - feedwater junction

7010000 "fedwtr" tmdpjun

7010101 709000000 075000000 0.0

7010200 1 518

7010201 -1.0 0.0 0.0 0.0

7010202 0.0 0.52514 0.0 0.0

7010203 100.0 0.52514 0.0 0.0

* component 706 - steamline outlet

7060000

7060101

7060201

7060300

7060301

079010000

1

518

"trb st n"

707000000

0.

trpvlv

valve

4.94e-5

.52514

0.0 0.0 00000

0

* component 707 - steamline sink volume

212
7070000

7070101

7070200

7070201

stmsink tmdpvol

l.Oe6 1.0 0.0 0.0 0.0 0.0 0.0 0.0 10

102 0

0.0 0.101e6 1.0

* component 748 - steam bypass

7480000

7480101

7480200

7480201

7480202

7480203

7480204

stmbypas

079010000

1 505

-1.0

7.03e÷6

7.05e+6

7.06e+6

tmdpjun

707000000

p 78010000

0.0 0.0

0.0 0.0

0.0 0.5

0.0 1.0

1. 14e-3

0.0

0.0

0.0

0.0

* component 710 - steam dump valve

7100000 stmdump tmdpjun

7100101 079010000 707000000 1.8506e-4

7100200 1 508 p 78010000

7100201 -1.0 0.0 0.0 0.0

7100202 0.1e6 0.0 0.0 0.0

7100203 7.03e6 0.0 0.55555 0.0

7100204 8.0e6 0.0 0.95238 0.0

* component 809 - feedwater source

8090000 feedwtr tmdpvol

8090101 1.Oe6 1.0 0.0 0.0 0.0 0.0 0.0 0.0 11

8090200 103 0

8090201 0.0 6.910e6 499.1

* component 801 - feedwater junction

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

8010000

8010101

8010200

8010201

"fedwtr"

809000000 085000000

1 518

-1.0 0.0 0.0

tmdpjun 0.0

0.0

213
8010202 0.0 0.52514 0.0 0.0

8010203 100.0 0.52514 0.0 0.0

* component 806 - steamline outlet

8060000

8060101

8060201

8060300

8060301

089010000

1

518

"trb st n"

807000000

0.

trpvlv

valve

4.94e-5

.52514

0.0 0.0 00000

0

* component 807 - steamline sink volume

8070000 stmsink tmdpvol

8070101 1.0e6 1.0 0.0 0.0 0.0 0.0 0.0 0.0 10

8070200 102 0

8070201 0.0 0.101e6 1.0

, component 848 - steam bypass

8480000 stmbypas tmdpjun

8480101 089010000 807000000 1.14e-3

8480200 1 505 p 88010000

8480201 -1.0 0.0 0.0 0.0

8480202 7.03e+6 0.0 0.0 0.0

8480203 7.05e+6 0.0 0.5 0.0

8480204 7.06e+6 0.0 1.0 0.0

* component 810 - steam dump valve

8100000

8100101

8100200

8100201

8100202

8100203

8100204

stmdump tmdpjun

089010000 807000000 1.8506e-4

1 508 p 88010000

-1.0 0.0 0.0 0.0

0.1e6 0.0 0.0 0.0

7.03e6 0.0 0.55555 0.0

8.0e6 0.0 0.95238 0.0

* power table

214
20200100 power 502

20200101 -1.0 2.857e6

20200102 0.0 2.857e6 17.0 2.857e6 17.6 2.720e6 19.0 2.57f

20200103 21.5 2.434e6 24.0 2.290e6 26.8 2.148e6 29.7 2.00

20200104 32.6 1.862e6 36.0 1.750e6 44.0 1.550e6 52.0 1.38•

20200105 63.0 1.265e6 74.0 1.170e6 84.0 1.110e6 94.0 1.05(

20200106 104.0 0.990e6 123.0 0.964e6 153.0 0.906e6 198.0 0.•

20200107 273.0 0.812e6 373.0 0.750e6 423.0 0.726e6 523.0 0.1

20200108 623.0 0.680e6 723.0 0.662e6 823.0 0.647e6 923.0 0.

20200109 1923.0 0.510e6 3123.0 0.439e6 5123.0 0.380e6

20200110 7123.0 0.340e6 9123.0 0.324e6 18123.0 0.271e6

3e6

5e6 5e6

)e6

54e6

706e6

629e6

* delete rcp and pzr heaters

20277700

20277701

20277702

htrnrate

-1.0

0.0

20277800 htrnrate

20277801 0.0

520

159155.

0.0

51556.1

501

0.

20278900

20278901 power

0.

++&4*

* control variables

*calculate time-integrated break mass flow

20576800 breakfl integral 1.0 0.0

20576801 mflowj 768000000

* calculate time-integrated lpsi flow

1

20573200 lpsib

20573201 mflowj

20573500 lpsic

20573501 mflowj

integral 1.0

732000000

integral 1.0

735000000

sum 1.0

0 cntrlvar

0 cntrlvar

0.0 1

0.0 1

20573800

20573801

20573802

lpsisum

0.0 1.

1.

0.0

732

735

1

20574000 smargin sum 1.0 0.0 1

215
20574001

20574002

20531700

20531701

20531702

20531703

20531704

20531705

20531706

20531707

20531708

20531709

20531710

20531711

20531712

20531713

20531714

20531800

20531801

20531802

20531803

20531804

20531805

20531806

20531807

20531808

20531809

20531810

20531811

20531812

20531813

20531814

20531815

20531816

20531900

20531901

20531902

20532000

20532001

20532002

20532003

20532004

20532005

20532006

0.0 1.0 sattemp

-1.0 tempf

sgasml

0.0

sum

1. 151e-2

2.303e-2

3.454e-2

4.605e-2

5.756e-2

8.635e-2

8.635e-Z

8.635e-2

8.635e-2

0.10376

1. 0393e3.861e-2

4.385e-2

0.59549

039010000

039010000

1.0 605.622 1

rho 060010000

rho 060020000

rho 060030000

rho 060040000

rho 060050000

rho 060060000

rho 060070000

rho 060080000

rho 060090000

rho 060100000

Z rho 061010000

rho 061020000

rho 061030000

rho 062010000

sgasm2 sum 1.0 187.

0.0 0.14922 rho

0.15856 rho

8.172e-2 rho

6.336e-2 rho

8.6429e-3 rho

8.7538e-3 rho

8.7538e-3 rho

8.7538e-3 rho

5.8359e-3 rho

4.6687e-3 rho

3.5015e-3 rho

2.3343e-3 rho

4.0563e-3 rho

0.13404 rho

3.425e-2 rho

3.425e-2 rho

.0125 1

063010000

064010000

065010000

066010000

067010000

067020000

067030000

067040000

067050000

067060000

067070000

067080000

067090000

068010000

069010000

069020000

sgasmt sum 1.0 792.635 1

0.0 1.0 cntrlvar 317

1.0 cntrlvar 318

sgbsml sum 1.0

0.0 1.151e-2

2.303e-2

3.454e-2

4.605e-2

5."756e-2

8.635e-2

605.622 1

rho 070010000

rho 070020000

rho 070030000

rho 070040000

rho 070050000

rho 070060000

216
20532007

20532008

20532009

20532010

20532011

20532012

20532013

20532014

20532100

20532101

20532102

20532103

20532104

20532105

20532106

20532107

20532108

20532109

20532110

20532110

20532112

20532113

20532114

20532115

20532116

20532116

20532201

20532202

20532300 20532301

20532302

2053Z303

20532304

20532305

20532306

20532307

20532308

205323095

20532310

20532311

20532312

20532313

20532314

20532400

8.635e-,

8.635e-'

8.635e-ý

0.10376

1.0393e3.861e4.385e-i

0.59549

sgbsm2 sum

0.0 0.14922

0.15856

8.172e-'

6.336e-e

8.6429e8.7538e8.7538e8.7538e5.8359e4.6687e3.5015e2.3343e4.0563e0.13404

3.425e-t

3.425e-,

rho

rho

rho

rho

rho

rho

rho

rho

070070000

070080000

070090000

070100000

071010000

071020000

071030000

072010000

1.0 187.0125 1

rho 073010000

rho 074010000

rho 075010000

J rho 076010000

-3 rho 077010000

-3 rho 077020000

-3 rho 077030000

-3 rho 077040000

-3 rho 077050000

-3 rho 077060000

-3 rho 077070000

-3 rho 077080000

-3 rho 077090000

rho 078010000

rho 079010000

2 rho 079020000

sgbsmt sum 1.0 792.635 1

0.0 1.0 cntrlvar 320

1.0 cntrlvar 321

sgcsml sum 1.0

0.0 1.151e-2

2.303e-2

3.454e-2

4.605e-2

5.756e-2

8.635e-2

8.635e-2

8.635e-2

8.635e-2

0.10376

1.0393e-2

3.861e-2

4.385e-2

0.59549

605.622 1

rho 080010000

rho 080020000

rho 080030000

rho 080040000

rho 080050000

rho 080060000

rho 080070000

rho 080080000

rho 080090000

rho 080100000

rho 081010000

rho 081020000

rho 081030000

rho 082010000

sgcsm2 sum 1.0 187.0125 1

217
20532401

20532402

20532403

20532404

20532405

20532406

20532407

20532408

20532409

20532410

20532411

20532412

20532413

20532414

20532415

20532416

20532500

20532501

20532502

0.0 0. 14922

0.15856

8.172e-2

6.336e-2

8.6429e-3

8.7538e-3

8.7538e-3

8.7538e-3

5.8359e-3

4.6687e-3

3.5015e-3

2.3343e-3

4.0563e-3

0.13404

3.425e-2

3.425e-2

rho

rho

rho

rho

rho

rho

rho

rho

rho

rho

rho

rho

rho

rho

rho

rho

083010000

084010000

085010000

086010000

087010000

087020000

087030000

087040000

087050000

087060000

087070000

087080000

087090000

088010000

089010000

089020000

sgcsmt

0.0

sum 1.0 792.635 1

1.0

1.0

cntrlvar 323

cntrlvar 324

*mass inventory of accumulator b

20572100 accmass mult 1.0 0.

20572101 rhof 721010000 acvliq

20572200 accmasc mult 1.0 0.0

20572201 rhof 722010000 acvliq

* core collapsed level

1

721

1

722

20581800

20581801

20581802

20581803

20581804

20581805

20581806

20581807

20581808

20581809

corelvl sum

0.0 0.11

0.788

0.78

0.52

0.78

0.788

0.35

1.054

0.600

1.0

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

0.0 1

013010000

013020000

013030000

013040000

013050000

013060000

013070000

012010000

011010000

* run statistics

20581900

20581901

20582000

20582001

oldtime

0.0 1.0

newtime

0.0 1.0

sum 1.0 0.0 0

cntrlvar 820

sum 1.0 0.0 0

time 0

218
20582100 timstep sum 1.0 0.0 0.0

20582101 0 -1. cntrlvar 819

20582102 1. cntrlvar 820

* calculate liquid levels in pressurizer and steam generators

20500100 preslev sum 1.0 4.08 1

20500101 0.0 0.105 voidf 091010000

20500102 0.892 voidf 091020000

20500103 5.4145 voidf 091030000

20500104 5.4145 voidf 091040000

20500105 0.105 voidf 091050000

20500400 veslev sum 1.0 10.421 1

20500401 0.0 1.0 voidf 011010000

20500402 1.054 voidf 012010000

20500403 0.11 voidf 013010000

20500404 0.788 voidf 013020000

20500405 0.78 voidf 013030000

20500406 0.52 voidf 013040000

20500407 0.78 voidf 013050000

20500408 0.788 voidf 013060000

20500409 0.35 voidf 013070000

20500410 1.0195 voidf 099010000

20500411 0.117 voidf 015010000

20500412 2.713 voidf 016010000

20500413 0.4015 voidf 018010000

20500200 sgalev sum 1.0 10.60282 1

20500201 0.0 0.2 voidf 060010000

20500202 0.4 voidf 060020000

20500203 0.6 voidf 060030000

20500204 0.8 voidf 060040000

20500205 1.0 voidf 060050000

Z0500Z06 1.5 voidf 060060000

20500207 1.5 voidf 060070000

20500208 1.5 voidf 060080000

20500209 1.5 voidf 060090000

20500210 1.8025 voidf 060100000

20500211 0.158 voidf 061010000

20500212 0.7925 voidf 061020000

20500213 0.9 voidf 061030000

20500214 2.16 voidf 062010000

20500215 0.4 voidf 068010000

20500300 sgblev sum 1.0 10.61266 1

Z0500301 0.0 0.2 voidf 070010000

219
20500302

20500303

20500304

20500305

20500306

20500307

20500308

20500309

20500310

20500311

20500312

20500313

20500314

20500315

20500500

20500501

20500502

20500503

20500504

20500505

20500506

20500507

20500508

20500509

20500510

20500511

20500512

20500513

20500514

20500515

20502200

20502201

20502202

20502203

20502204

20502205

20502206

20502207

20502208

20502209

20502212

20502213

20502214

20502215

20502216

20502217

0.4

0.6

0.8

1.0

1.5

1.5

1.5

1.5

1.8025

0.158

0.7925

0.9

2.16

0.4

sgclev sum

0.0 0.2

0.4

0.6

0.8

1.0

1.5

1.5

1.5

1.5

1.8025

0.158

0.7925

0.9

2.16

0.4

sgalevd sum

0.0 1.481

1.5

1.5

1.5

1.0

0.8

0.6

0.4

0.2

1.9815

0.8275

1.6055

0.3375

2.16

0.4

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

1.0

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

1.0

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidtf

voidf

070020000

070030000

070040000

070050000

070060000

070070000

070080000

070090000

070100000

071010000

071020000

071030000

072010000

078010000

10.61266 1

080010000

080020000

080030000

080040000

080050000

080060000

080070000

080080000

080090000

080100000

081010000

081020000

081030000

082010000

088010000

12.00412 1

067010000

067020000

067030000

067040000

067050000

067060000

067070000

067080000

067090000

056010000

065010000

064010000

063010000

062010000

068010000

220
20503300

20503301

20503302

20503303

20503304

20503305

20503306

20503307

20503308

20503309

20503312

20503313

20503314

20503315

20503316

20503317

20504400

20504401

20504402

20504403

20504404

20504405

20504406 20504407

20504408

20504409

20504412

20504413

20504414

20504415

20504416

20504417

sgblevd sum

0.0 1.481

1.5

1.5

1.5

1.0

0.8

0.6

0.4

0.2

1.9815

0.8275

1.6055

0.3375

2.16

0.4

sgclevd sum

0.0 1.481

1.5

1.5

1.5

1.0

0.8

0.6

0.4

0.2

1.9815

0.8275

1.6055

0.3375

2.16

0.4

1.0

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

1.0

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

voidf

12.00995 1

077010000

077020000

077030000

077040000

077050000

077060000

077070000

077080000

077090000

076010000

075010000

074010000

073010000

072010000

078010000

12.00995 1

087010000

087020000

087030000

087040000

087050000

087060000

087070000

087080000

087090000

086010000

085010000

084010000

083010000

082010000

088010000

* calculate pressure differences

20500600

20500601

20500602

20504100

20504101

20504101

20504103

20504104

p02 sum

0.0 1.0

-0.441

dp46lf

0.0

sum

1.0

-1.0

+0.49

+5.635

1.0 15694560. 1

p 013070000

rho 013070000

1.e-3 260.256 1

p 060010000

p 060060000

rho 060010000

rho 060060000

221
20504200

20504201

20504202

20504203

20504204

20504300

20504301

20504302

20504303

20504304

20505100

20505101

20505102

20505200

20505201

20505Z20 20505202

20505301

20505300

20505301

20505900

20505901

20505902

20505903

20506000

20506001

20506002

20506003

20506004

20506100

20506101

20506102

20506200 20506201

20506202

20506203

20506204

20506300

20506301

dp561f

0.0

dp661f

0.0

dpl

0.0

sum

1.0

-1.0

+0.49

+5.635

sum

1.0

-1.0

+0.49

+5.635

sum

1.0

-1.0

1.e-3 260.3635 1

p 070010000

p 070060000

rho 070010000

rho 070060000

1.e-3 260.3635 1

p 080010000

p 080060000

rho 080010000

rho 080060000

dp2 sum

0.0 1.0

-1.0

dp3 sum

0.0 1.0

-1.0

1.e-3

p 039010000

p 031010000

1.e-3

p 049010000

p 041010000

L.e-3

p 059010000

p 051010000

1.e-3

p 033010000

p 033030000

rho 0330300(

1.e-3

p 033030000

p 034010000

rho 0330300(

rho 0340100(

13.9222 1

13.92278 1

13.92278 1

102.8206 1

O0

70.6971 1

dpllv

0.0

sum

1.0

-1.0

-1.9213

dp4l sum

0.0 1.0

-1.0

1.9213

2.189

dllv4l sum

0.0 1.0

+1.0

dp44 sum

0.0 1.0

-1.0

+2.8204

+2.189

dpl2vg sum

0.0 1.0

1. e-3

cntrlvar

cntrlvar

173.5176

59

60

1

1.e-3

p 035010000

p 034220000

rho 0350100(

rho 0342200(

1.e-3

p 035040000

77.5905 1

20 O0

287.572 1

222
20506302

20506303

20506304

20506400

20506401

20506402

20506800

20506801

20506802

20506803

20507100

20507101

20507102

20507104

-1.0 -. 579

-2.8204

d4412vg sum

0.0 1.0

+1.0

dpOr3 sum

0.0 1.0

-1.0

+.981

p 035010000

rho 035040000

rho 035010000

1.e-3 365.162

cntrlvar 62

cntrlvar 63

1.e-3 497.097

p 011010000

p 031010000

rho 011010000

1.e-3 218.743

p 031010000

p 018010000

1

1

dpOr2 1

0.0

sum

1.0

-1.0

+1.9545 rho 018010000

20533100 dpOr2a3

20533101

20533102

20507300

20507301

20507302

20507303

20507304

20507400

20507401

20507402

20507403

20507404

20507500

20507501

20507502

20507503

20509100 20509101

20509102

20509103

20509104

20509300

20509301

20509302

0.0

sum l.e-3 7.1584

1.0 cntrlvar 68

1.0 cntrlvar 71

1

dppl

0.0

dpp2

0.0

dpp3

0.0

dp4rl

0.0

dp5rl

0.0

sum11

1.0

-1.0

-. 491

.716

sum ]

1.0

-1.0

+25.182

+19.384

sum

1.0

-1.0

+.491

sum

1.0

-1.0

+0.981

+9.614

sum

1.0

-1.0

l.e-3 269.995 1

p 091020000

p 091050000

rho 091020000

rho 091050000

l.e-3 231.885

p 091030000

p 091040000

rho 091030000

rho 091040000

I

L.e-3 264.0964 1

p 032010000

p 091020000

rho 091020000

1.e-3 761.492

p 067080000

p 062010000

rho 067080000

rho 062010000

1.e-3 762.19

p 077080000

p 072010000

1

1

223
20509303

20509304

20509500

20509501

20509502

20509503

20510000

20510001

20510002

20510003

20510004

+0.981 rho 077080000

+9.614 rho 072010000

dpl2p

0.0

dpOrl

0.0

sum

1.0

-1.0

-7.794

sum

1.0

-1.0

0.981

2.148

1.e-3 46.7045

p 035050000

p 037010000

rho 035050000

1.e-3 717.201

p 011010000

p 018010000

rho 011010000

rho 018010000

1

1

*

20511100

20511101

20511102

20511103

20511104

20511200

20511201

20511202

20511203

20511204

20511300

20511301

20511302

20511303

20511304

20511400

20511401

20511402

20511403

20511404

20509602

20509601

20509602

20509603

20509700

20509701

20509702

dpOZOO sum

0.0 1.0

-1.0

1.715

4.9

dpupl sum

0.0 1.0

-1.0

4.993

5.370

p

p

p

p

dpO34 sum

0.0 1.0 p

-1.0 p

-4.9955

13.867

dpuhead sum

0.0 -1.0 p

1.0 p

0.7203

2.19275

1.e-3 0.

011010000

013070000

rho 013070000

rho 011010000

1.e-3 0.

099010000

016010000

rho 099010000

rho 016010000

1.e-3 0.

099010000

017010000

rho 099010000

rho 017010000

1.e-3 0.

018010000

019010000

rho 019010000

rho 018010000

1.e-3 0.

035040000

035050000

rho 035050000

dpl2vp sum

0.0 1.0

-1.0

5.07

dp22vp sum

0.0 1.0

-1.0

P

p

p

p

1.e-3

045040000

045050000

0. 1

224
20509703

20509800

20509801

.20509802

20509803

20510200

20510201

20510202

20510203

20510300

20510301

20510302

20510303

20510304

20510500

20510501

20510502

20510503

20510600

20510601

20510602

20510603

20510604

20507000

20507001

20507002

20507003

20507004

20508000

20508001

20508002

20508003

20508004

20550000

20550001

20550002

20550003

20550004

20550100

5.07

dp

0.

dp22p

0.0

dp2 0.0

32vp sum

0 1.0

-1.0

5.07

sum

1.0

-1.0

-7.794

2vg sum

1.0

-1.0

-. 579

-2.8204

sum

1.0

-1.0

-7.794

rho 045050000

1.e-3 0.

055040000

055050000

rho 055050000

1

p

p

1.e-3 46.7045

p 045050000

p 047010000

rho 045050000

1

1.e-3

p 045040000

p 045010000

rho 0450400(

rho 0450100(

287.572 1

dp32p

0.0

1.e-3 46.7045

p 055050000

p 057010000

rho 055050000

1

dp32vg sum

0.0 1.0

-1.0 -. 579

-2.8204

dp5l sum

0.0 1.0

-1.0

1.9213

2.189

dp6l sum

0.0 1.0

-1.0

1.9213

2.189

dp4r2 sum

0.0 1.0

-1.0

1.96

4.41

1.e-3

p 055040000

p 055010000

rho 0550400(

rho 0550100(

l.e-3

p 043030000

p 044010000

rho 0430300(

rho 0440100(

1.e-3

p 053030000

p 054010000

rho 0530300(

rho 0540100(

287.572 1

OO

70

70.6971 1

O0

O0

70.6971 1

1.e-3 0.

p 061030000

p 068010000

rho 068010000

rho 061030000

1

dp5r2 sum 1.e-3 0. 1

225
20550101

20550102

20550103

20550104

20550200

20550201

20550202

20550203

20550204

0.0 1.0

-1.0

1.96

4.41

dp6r2 sum

0.0 1.0

-1.0

1.96

4.41

p 071030000

p 078010000

rho 078010000

rho 071030000

1.e-3 0.

p 081010000

p 088010000

rho 088010000

rho 081030000

1

* primary system masses

20515100

20515101

20515102

20515103

20515104

20515105

20515106

20515107

20515108

20515109

20515110

20515111

20514100 20514112

20514113

20514114 20514115

20514116

20514117

20514118

20514119

20514120

20514121

20514122

20515200

20515201

20515202

20515203

20515204

20515205

20515206

sgamasl sum 1.0

0.0 0.0350607

2.068400e-3

4.136800e-3

6.205200e-3

8.273600e-3

1.034200e-2

1.551300e-2

1.551300e-2

1.551300e-2

1.551300e-2

7.497950e-3

sgamas2 sum 1.0

0.0 7.497950e-3

1.551300e-2

1.551300e-2

1.551300e-2

1.551300e-2

1.034200e-2

8.273600e-3

6.205200e-3

4.136800e-3

2.068400e-3

0.0350607

sgbmasl sum 1.0

0.0 0.0350607

2.068400e-3

4.136800e-3

6.205200e-3

8.273600e-3

1.034200e-2

99.3376 1

rho 034010000

rho 034020000

rho 034030000

rho 034040000

rho 034050000

rho 034060000

rho 034070000

rho 034080000

rho 034090000

rho 034100000

rho 034110000

102.5563 1

rho 03O120000

rho 034130000

rho 034140000

rho 034150000

rho 034160000

rho 034170000

rho 034180000

rho 034190000

rho 034200000

rho 034210000

rho 034220000

99.3376 1

rho 044010000

rho 044020000

rho 044030000

rho 044040000

rho 044050000

rho 044060000

226
20515207

20515208

20515209

20515210

20515211

20514200

20514212

20514213

20514214

20514215

20514216

20514217

20514218

20514219

20514220

20514221

20514222

20516100

20516101

20516102

20516103

20516104

20516105

20516106

20516107

20516108

20516109

20516110

20516111

20516200

20516212

20516213

20516214

20516215

20516216

20516217

20516218

20516219

20516220

20516221

20516222

20515300

20515301

20515302

sgbmas2 0.0

1.551300e-2

1.551300e-2

1.551300e-2

1.551300e-2

7.497950e-3

sum 1.0

7.497950e-3

1.551300e-2

1.551300e-2

1.551300e-2

1.551300e-2

1.034200e-2

8.273600e-3

6.205200e-3

4.136800e-3

2.068400e-3

0.0350607

rho

rho

rho

rho

rho

044070000

044080000

044090000

044100000

044110000

sgcmasl sum 1.0

0.0 0.0350607

2.068400e-3

4.136800e-3

6.205200e-3

8.273600e-3

1.034200e-2

1.551300e-2

1.551300e-2

1.551300e-2

1.551300e-2

7.497950e-3

sgamas2 sum 1.0

0.0 7.497950e-3

1.551300e-2

1.551300e-2

1.551300e-2

1.551300e-2

1.034200e-2

8.273600e-3

6.205200e-3

4.136800e-3

2.068400e-3

0.0350607

cormas sum 1.0

0.0 0.15323

6.20907e-2

102.5563 1

rho 044120000

rho 044130000

rho 044140000

rho 044150000

rho 044160000

rho 044170000

rho 044180000

rho 044190000

rho 044200000

rho 044210000

rho 044220000

99.3376 1

rho 054010000

rho 054020000

rho 054030000

rho 054040000

rho 054050000

rho 054060000

rho 054070000

rho 054080000

rho 054090000

rho 054100000

rho 054110000

102.5563 1

rho 054120000

rho 054130000

rho 054140000

rho 054150000

rho 054160000

rho 054170000

rho 054180000

rho 054190000

rho 054200000

rho 054210000

rho 054220000

407

rho

rho

.052 1

011010000

012010000

227
20515303

20515304

20515305

20515306

20515307

20515308

20515309

20515310

20515312

20515313

20515314

20515315

20515316

20515317

20515318

20515319

20515400

20515401

20515402

20515403

20515404

20515405

20515406

20515407

20515408

20515410

20515411

20515412

20515413

20515414

20515415

20515416

20515500

20515501

20515502

20515503

20515504

20515505

20515600

20515601

20515602

20515603

20515604

20515605

vesmas

0.0

hlamas

0.0

hlbmas

0.0

4.70800e-3

3.37264e-2

3.33840e-2

2.22560e-2

3.33840e-2

3.37264e-2

1.80660e-2

1. 56310e-3

1. 11975e-2

1. 10838e-2

7.38920e-3

1.10838e-2

1. 11975e-2

4.97350e-3

5.03000e-2

9.15640e-2

sum 1.0

.11263

9.06700e-3

4.90700e-2

8.92590e-2

4.33233e-2

3.78310e-3

2.44140e-3

9.69700e-4

2.39771e-2

2.39771e-2

2.39771e-2

2.39771e-2

7.51150e-3

1.08295e-2

2.79758e-2

sum 1.0

1.305868e-2

5.46800e-3

8.724194e-3

1.583533e-2

6.021362e-3

sum 1.0

1.305868e-2

5.46800e-3

8.724194e-3

1.583533c-2

6.021362e-3

rho

rho

rho

rho

rho

rho

rho

rho

rho

rho

rho

rho

rho

rho

rho

rho

361.04 

1

rho 016010000

rho 017010000

rho 018010000

rho 019010000

rho 020010000

rho 021010000

rho 021020000

rho 021030000

rho 022010000

rho 022020000

rho 022030000

rho 022040000

rho 022050000

rho 022060000

rho 022070000

34.57254 

1

rho 031010000

rho 032010000

rho 033010000

rho 033020000

rho 033030000

34.57254 

1

rho 041010000

rho 042010000

rho 043010000

rho 043020000

rho 043030000

013010000

013020000

013030000

013040000

013050000

013060000

013070000

014010000

014020000

014030000

014040000

014050000

014060000

014070000

099010000

015010000

228
20516600

20516601

20516602

20516603

20516604

20516605

20515700

20515701

20515702

20515703

20515704

20515705

20515706

*20515708

20515709

20515710

20515711

20515712

20515713

20515800

20515801

20515802

20515803

20515804

20515805

20515806

*20515808

20515809

20515810

20515811

20515812

20515813

20516800

20516801

20516802

20516803

20516804

20516805

20516806

*20516808

20516809

20516810

20516811

hlcmas

0.0

clamas

0.0

clbmas

0.0

sum 1.0

1.305868e-2

5.46800e-3

8.724194e-3

1.583533e-2

6.021362e-3

sum 1.0

4.581000e-3

2.123175e-2

2.430950e-2

8.967000e-3

2.263400e-2

2.062890e-2

8.921154e-3

1.14828e-2

9.394024e-3

5.46800e-3

8.57448e-3

5.860165e-3

sum 1.0

4.581000e-3

2.123175e-2

2.430950e-2

8.967000e-3

2.263400e-2

2.062890e-2

8.921154e-3

1.14828e-2

9.394024e-3

5.46800e-3

8.57448e-3

5.860165e-3

sum 1.0

4.581000e-3

2.123175e-2

2.430950e-2

8.967000e-3

2.263400e-2

2.06277890e-2

8.921154e-3

1.14828e-2

9.394024e--3

5.46800e-3

34.57254 1

rho 051010000

rho 052010000

rho 053010000

rho 053020000

rho 053030000

108.3605 1

rho 035010000

rho 035020000

rho 035030000

rho 035040000

rho 035050000

rho 036010000

rho 362010000

rho 037010000

rho 037020000

rho 038010000

rho 039010000

rho 039020000

108.3605 1

rho 045010000

rho 045020000

rho 045030000

rho 045040000

rho 045050000

rho 046010000

rho 462010000

rho 047010000

rho 047020000

rho 048010000

rho 049010000

rho 049020000

108.3605 1

rho 055010000

rho 055020000

rho 055030000

rho 055040000

rho 055050000

rho 056010000

rho 562010000

rho 057010000

rho 057020000

rho 058010000

clcmas

0.0

229
20516812

20516813

20515900

20515901

20515902

20515903

20515904

20515905

20515906

20515907

20515908

20519900

20519901

20519902

20519903

20519904

20519905

20519906

20519907

20519908

20519909

20519910

20519911

20519912

20519913

20519914

20519915

20533000

20533001

20533002

20530400

20530401

20530402

20530403

20530404

20530500

20530501

20530502

20530503

20530504

20530600

20530601

prsrmas

0.0

totmas

0.0

tvesmas

0.0

dp461c

0.0

8.57448e-3

5.860165e-3

sum 1.0

1.118650e-3

9.040600e-3

3.863750e-3

2.161600e-3

2.7890e-2

0.187535

0.187535

2.424500e-3

rho 059010000

rho 059020000

114.4755 1

rho 090010000

rho 090020000

rho 090030000

rho 091010000

rho 091020000

rho 091030000

rho 091040000

rho 091050000

sum

1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0 1802.557 1

cntrlvar 151

cntrlvar 141

cntrlvar 152

cntrlvar 142

cntrlvar 153

cntrlvar 154

cntrlvar 155

cntrlvar 156

cntrlvar 157

cntrlvar 158

cntrlvar 159

cntrlvar 161

cntrlvar 162

cntrlvar 166

cntrlvar 169

sum 1.0

1.0 cntrlvar

1.0 cntrlvar

768.092 1

153

154

L.0(

-1.(

+0.49

-4.12

sum 1.e-3 130.9371 1

p 060010000

p 060050000

rho 060010000

302 rho 060050000

dp462c sum

0.0 1.0

-1.0

+4.1202

+5.6408

dp463c sum

0.0 1.0

1.e-3 129.352

p 060050000

p 060060000

rho 060050000

rho 060060000

1

l.e-3 123.3542 1

p 060060000

230
20530602

20530603

20530604

20530700

20530701

20530702

20530703

20530704

20530800

20530801

20530802

20530803

20530804

20530900

20530901

20531000

20531001

20531002

20531003

.20531004

20531100

20531101

20531102

20531103

20531104

20531200

20531201

20531202

20531204

20531300

20531301

20531302

20531303

20531400

20531401

20531402

20531403

20531404

20531500

-1.0 p 060080000

-5.6408 rho 060060000

-1.7756 rho 060080000

dp464c sum 1.e-3 102.3876 1

0.0 1.0 p 060080000

-1.0 p 060090000

+1.7756 rho 060080000

+2.3642 rho 060090000

dp465c sum 1.e-3 54.6744 1

0.0 1.0 p 060090000

-1.0 p 060100000

-2.3642 rho 060090000

-3.5537 rho 060100000

dp466c sum 1.e-3 57.5067 1

0.0 11.124 rho 060100000

dp47 sum

0.0 1.0

-1.0

-7.571

+9.614

dpO50 sum

0.0 1.0

-1.0

0.1092

-1.369

dpO5l sum

0.0 1.0

-1.0

-1.369

1.e-3 185.7087 1

p 060100000

p 062010000

rho 060100000

rho 062010000

1.e-3 84.0194 1

p 021020000

p 019010000

rho 021020000

rho 019010000

1.e-3 146.4596 1

p 039020000

p 019010000

rho 019010000

dp052 sum 1.e-3 364.221 1

0.0 1.0 p 022060000

-1.0 p 039020000

+0.0896 rho 022060000

dp423t6 sum 1.e-3 724.238 1

0.0 1.0 p 034010000

-1.0 p 034110000

-2.189 rho 034010000

3.360 rho 034110000

dp433t6 sum 1.e-3 722.064 1

231
20531501

20531502

20531503

20531504

20531600

20531601

20531602

20531603

20531604

20539900

20539901

20539902

20539903

20539904

20533700

20533701

20533702

20533703

20533704

20532600

20532601

20532602

20532603

20532604

20533400

20533401

20533402

20533403

20533404

20533500

20533501

20533502

20533503

20533504

20533600

20533601

20533602

20533603

20533604

0.0 1.0

-1.0

-2.189

+3.360

dp4 sum

0.0 1.0

-1.0

-2.189

-2.189

dp523t6 st

0.0 1.0

-1.0

-2.189,

3.360 1

p

p

rho

rho

1. ep

p

rho

rho

034220000

034120000

034220000

034120000

-3 -33.6086 1

034220000

034010000

034220000

034010000

1.e-3 724.238 1

044010000

044110000

044010000

044110000

l.e-3 722.064 1

044220000

044120000

044220000

044120000

m

p

ptho

110

dp533t6 sum

0.0 1.0 1

-1.0 1

-2.189 ri

+3.360 rI

dp5 sum 1.

0.0 1.0 1

-1.0 1

-2.189 rA

-2.189 rA

dp623t6 sum

0.0 1.0 p

-1.0 p

-2.189 rh(

3.360 rh(

dp633t6 sum

0.0 1.0 1

0

0

.e-3 -33.6086

S044220000

044010000

o 044220000

ho 044010000

1

D

0

1.e-3 724.238 1

054010000

054110000

054010000

054110000

1.e-3 722.064 1

054220000

054120000

054220000

054120000

P

dp6

0.0

-1.0

-2.189

+3.360

sum

1.0

-1.0

-2.189

-2.189

P

rho

rho

1.e-3 -33.6086 1

p 054220000

p 054010000

rho 054220000

rho 054010000

232
20588800

20588801

20588900

20588901

20588902

20588903

20588904

20500700

20500701

20500702

20500703

20500704

20500705

20500706

20500707

20500708

20500709

20500800

20500801

20500802

20500803

20500804

20500805

20500806

20500807

20500808

20500809

20501000

20501001

20501002

20501003

20501004

20501100

20501101

20501102

20501200

20501201

20501300

20501301

20501302

20501303

corepow function 1.e-3 0.0 1

time 0 1

masserr sum 1.0 0.0 1

-2510.23 1.0 cntrlvar 199

1.0 cntrlvar 721

1.0 cntrlvar 722

1.0 cntrlvar 768

coredenf

0.0 1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0

coredeng

0.0 1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0

1.0

sum 0.111111 746.84 1

rhof 011010000

rhof 012010000

rhof 013010000

rhof 013020000

rhof 013030000

rhof 013040000

rhof 013050000

rhof 013060000

rhof 013070000

sum 0.111111 104.0 1

rhog 011010000

rhog 012010000

rhog 013010000

rhog 013020000

rhog 013030000

rhog 013040000

rhog 013050000

rhog 013060000

rhog 013070000

coredp sum 0.10204 0.0

0.0 1.0 p 011010000

-1.0 p 013070000

1.715 rho 013070000

-52.038 cntrlvar 8

1

dendiff sum 1.0 0.0 1

0.0 1.0 cntrlvar 7

-1.0 cntrlvar 8

corelvi div 1.0 0.0 1

cntrlvar 11 cntrlvar 10

auxlvla sum 1.0 13.45 1

11.255 0.158 voidf 061010000

0.7925 voidf 061020000

0.9 voidf 061030000

233
20501304 2.16 voidf 062010000

20501400 auxlvlb sum 1.0 13.45 1

20501401 11.255 0.158 voidf 071010000

20501402 0.7925 voidf 071020000

20501403 0.9 voidf 071030000

20501404 2.16 voidf 072010000

20501500 auxlvlc sum 1.0 13.45 1

20501501 11.255 0.158 voidf 081010000

20501502 0.7925 voidf 081020000

20501503 0.9 voidf 081030000

20501504 2.16 voidf 082010000

20590100 maxtempc stdfnctn 1.0 0.0

20590101 max httemp 13100108

20590102 httemp 13100208

20590103 httemp 13100308

20590104 httemp 13100408

20590105 httemp 13100508

20590106 httemp 13100608

20590107 httemp 13100708

20590108 httemp 13100808

20590109 httemp 13100908

20590110 httemp 13101008

20590111 httemp 13101108

20590112 httemp 13101208

20503400 feedi sum 1.0 0.0 1

20503401 0.0 1.0 mflowj 601000000

20503402 1.0 mflowj 712000000

20503500 feed2 sum 1.0 0.0 1

20503501 0.0 1.0 mflowj 701000000

20503502 1.0 mflowj 714000000

20503600 feed3 sum 1.0 0.0 1

20503601 0.0 1.0 mflowj 801000000

20503602 1.0 mflowj 716000000

* end of input

234
NRC FORM 335 U.S. NUCLEAR REGULATORY COMMISSION 1. REPORT NUMBER

(2.bi (Assigned by NRC. Add Vol_. Supo.. Rev..

NRCMl 1102. B Lnd GddeRdAPn Cy.) NHImber, if 32o1.32o2 BIBLIOGRAPHIC DATA SHEET

fSee instruc:ions on the reversel

2. TITLE AND SUBTITLE NUREG/IA-0103

Assessment of BETHSY Test 9.l.b using RELAPS/MOD3 3. DATE REPORT PUBLISHED

MONTH V YEAR

June 1993

4. FIN OR GRANT NUMBER L2245

5. AUTHOR (S) 6. TYPE OF REPORT

Sukho Lee, Bub-Dong Chung and Hho-Jung Kim

Technical 7. PERIOD COVERED finciusvec Dares)

8. PER FORMING ORG~ANIZ~ATION - NAME AND ADDRSS W~(iNRC. Provide Division. 0/fi/cta'Rgi~on. U.I. Nurlar Reguiaoev ComMissOn, and ma//Mg addrvuwif contraxrof, Pros/dc

mnnie and me/Ung add,,uLi

Korea Institute of Nuclear Safety P.O. Box 16, Daeduk-Danji, Daejon, Korea

9. SPONSORING ORGANIZATION - NAME AND ADDRESS (If NRC. type '&n ,es above"; if eontracor. Provide NRC Division. Office or Revion. U.S. Nuclear Regulatory Commiason.

-s mailin addrMU

Office of Nuclear Regulatory Research

U.S. Nuclear Regulatory Commission

Washington, DIC. 20555

10. SUPPLEMENTARY NOTES

11. ABSTRACT 1200 Wward olea)

2" cold leg break test 9.1.b, conducted at the BETHSY facility was analyzed using the RELAP5/MOD3 Version

5m5 code.

The test 9.1.b was conducted with the main objective being the investigation of the thermal-hydraulic mechanisms

responsible for the large core uncovery and fuel heat-up, requiring the implementation of an ultimate procedure.

The present analysis demonstrates the code's capability to predict, with sufficient accuracy, the main phenomena

occurring in the depressurization transient, both from a qualitative and quantitative point of view. Nevertheless,

several differences regarding the evolution of phenomena and affecting the timing order have to be pointed out in

the base calculation.

Three calculations were carried out to study the sensitivity to change of the nodalization in the components of the

loop seal cross-over legs, and of the auxiliary feedwater control logics, and of the break discharge coefficient.

12. KEY WORDS/DESCR;PTORS (Listwoeds orpnserns that willatist reseen in localing the revOtt.) 13. AVAILABILITY STATEMENT

ICAP Program Unlimited

RELAP5/MOD3 14. SECUAITY CLASSIFICATION

BETHSY 9.1.b rol, Pae)

Unclassified

I rnik Re, orn

Unclassified

15. NUMBER OF PAGES

16. PRICE

NRC FORM 33S (24191


Federal Recycling Program

UNITED STATES

NUCLEAR REGULATORY COMMISSION

WASHINGTON, D.C. 20555-0001 (4, copies)

SPECIAL FOURTH-CLASS RATE

POSTAGE AND FEES PAID

USNRC

PERMIT NO. G-67

OFFICIAL BUSINESS

PENALTY FOR PRIVATE USE, $300

lalfg-3

5

3