NUREG/IA-0141

, International

Agreement Report

Result of BETHSY Test 9.1.b Using

RELAP5/MOD3

Prepared by

S. Petelin, B. Mavko, 0. Gortnar, I. Ravnikar, G. Cerne

University of Ljubljana

"Joief Stefan" Institute

Ljubljana, Slovenia

Office of Nuclear Regulatory Research

U.S. Nuclear Regulatory Commission

Washington, DC 20555-0001

August 1998

Prepared as part of

The Agreement on Research Participation and Technical Exchange

under the International Thermal-Hydraulic Code Assessment and Maintenance Program

(CAMP)

Published by

U.S. Nuclear Regulatory Commission
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NUREG/IA-0141

International

Agreement Report

Result of BETHSY Test 9.1.b Using

RELAP5/MOD3

Prepared by

S. Petelin, B. Mavko, 0. Gortnar, I. Ravnikar, G. Cerne

University of Ljubljana

"Jolef Stefan" Institute

Ljubljana, Slovenia

Office of Nuclear Regulatory Research

U.S. Nuclear Regulatory Commission

Washington, DC 20555-0001

August 1998

Prepared as part of

The Agreement on Research Participation and Technical Exchange under the International Thermal-Hydraulic Code Assessment and Maintenance Program (CAMP)

Published by

U.S. Nuclear Regulatory Commission

Abstract

RELAP5 computer code was used to simulate an experiment designated 9.1.b, (2" Cold Leg

Break without HPSI and with Delayed Ultimate Procedure) performed on BETHSY integral test

facility. This test is characterized as beyond design transients scenarios with unavailability of

some safety and protection systems. The calculations which have been completed using the

computer Sun Sparcstation 20 aim to evidence the difference between experimental and

computed data. Generally, an agreement of major transient treads is shown to be obtained in

the simulation.

Page I
University of Ljubljana

"Jolef Stefan" Institute, Ljubljana, Slovenia

Contents

List of Abbreviations III

Nomenclature III

Subscripts and Superscripts III

List of Figures IV

List of Tables IV

1 Introduction 1

2 BETHSY facility and corresponding RELAP5 input model 1

3 Results 6

3.1 Pre-test calculations of test 9.1.b (ISP-27) 6

3.2 Post-test calculations of test 9.1.b (ISP-27) 7

3.3 RELAP5/MOD3.1.2 simulation realized at Texas A&M University 14

4 Nodalization Study for BETHSY Experiment 18

4.1 Description 18

5 Run Statistics 21

6 Conclusion 21

7 References 23

Appendix A: Listing of middle BETHSY nodalization

Page II
University of LjubUana

"Joief Stefan" Institute, Ljubliana, Slovenia

List of Abbreviations

AFW auxiliary feedwater

DP ..... pressure difference

DT ..... temperature difference

uS ..... "Jolef Stefan" institute

ISP ..... international standard problem

MFW ..... main feedwater

NPP ..... nuclear power plant

PWR ..... pressurized water reactor

RCP ..... reactor coolant pump

RCS ..... reactor coolant system

SG ..... steam generator

Nomenclature

A .... flow area (m2)

g .... acceleration of gravity (m/s2)

h .... elevation change (m)

p .... pressure (Pa)

v .... velocity (m/s)

x .... length coordinate (m)

a .... vapour void fraction (m3/m3)

p .... density (kg/r 3)

Subscripts and Superscripts

cold .... in cold leg

hot .... in hot leg

Page III
University of Ljubljana

"Jolef Stefan" Institute, Ljubljana, Slovenia

List of Figures

Figure 2.1:

Figure 2.2:

Figure 2.3:

Figure 2.4:

Figure 2.5:

Figure 3.1:

Figure 3.2:

Figure 3.3:

Figure 3.4:

Figure 3.5:

Figure 3.6:

Figure 3.7:

Figure 3.8:

Figure 3.9:

Figure 3.10:

Figure 3.11:

Figure 3.12:

Figure 3.13:

Figure 3.14:

Figure 3.15:

Figure 3.16:

Figure 3.17:

Figure 3.18:

Figure 3.19:

Figure 3.20:

Figure 3.21:

Figure 4.1

Figure 4.2:

Figure 4.3:

Figure 4.4:

BETHSY facility

Base RELAP5 input model of BETHSY facility

Enlarged (detailed) RELAPS input model of BETHSY facility

RCS renodalization

RCS and RCP renodalization

The influence of guide tube renodalization

Test 9.1.b, Pressurizer pressure

Test 9.1.b, No.2 SG steam dome pressure

Test 9. 1.b, Core collapsed liquid level

Test 9.1 .b, Core outlet steam temperature

Test 9.1.b, Maximum cladding temperature

Test 9.1.b, No.1 CL spool piece void fraction, base case

Test 9.1.b, No.1 CL void fraction, renod. of guide tube

Test 9.1 .b, Break mass flow rate, base case

Test 9. 1.b, Break mass flow rate, renod. of guide tube

Test 9. 1.b, Secondary side mass inventory

Test 9.1.b, Break discharged mass

Test 9.1.b, Pressurizer pressure

Test 9.1.b, No.2 SG steam dome pressure

Test 9.1 .b, Core collapsed liquid level

Test 9.1 .b, Core outlet steam temperature

Test 9.1.b, Maximum cladding temperature

Test 9. 1.b, No. 1 CL spool piece void fraction

Test 9.1.b, Break-mass flow rate

Test 9. 1 .b, Secondary side mass inventory

Test 9.1.b, Break discharged mass

Steam generator nodalization for large input model

Maximal clad temperature calculated by RELAP5/MOD2 code.

Maximal clad temperature calculated by RELAP5/MOD3.1 code.

Maximal clad temperature calculated by RELAP5/MOD3.1.2 code.

2

3

4

5

5

9

10

10

10

11

11

11

12

12

12

13

13

14

14

15

15

15

16

16

16

17

19

20

20

20

List of Tables

Table 3.1:

Table 4.1.:

Table 5.1.:

Test 9.1 .b (ISP-27), initial condition

Three nodalizations.

Computational efficiency

8

18

21

Page IV
1 Introduction

The objective of Joief Stefan Institute (US) activities in area of RELAP5 analyses is to

extend the experiences in simulations of small break loss of coolant accidents and two-phase

natural circulation cooling. With an attempt to investigate all BETHSY experiments available

US has developed its own RELAP5 model of this facility. The on BETHSY experiences based

improved modelling methods will be used in simulations of real plant transients and

evaluation of plant accidents management procedures.

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 uncover and fuel heat-up, requiring the implementation of an

ultimate procedure.

The present analysis includes also assessment of three different versions of RELAP5 code

(MOD2, MOD3.1 and MOD3.1.2 without any modification of the codes and with guidelines

consideration) using experimental data of the BETHSY experiment 9.1.b (OECD-ISP-27).

The goal of the comparison among different versions of RELAP5 code was to optimize CPU

time and time for new model development.

The report describes the results of the calculation performed by the RELAP5/MOD3 codes

and shows the comparisons with the major variables obtained in the experiment, A brief

description of the BETHSY facility is provided in Section 2. Section 3 describes discusses

the pre-test and post-test results, sensitivity studies are in Section 4 and run statistic is

described in Section 5.

2 BETHSY facility and corresponding RELAP5 input model

BETHSY facility is located at Centre D'Etudes Nucleaires de Grenoble (France). It is a

scaled down model of the three loop 2775 MWt (900 MWe) Framatome PWR power plant,

which is designed to simulate most PWR accidents of interest and to study accident

management procedures (Fig. 2.1).

Six important choices have been made which characterize indeed the general design of the

Bethsy facility. They concern: the number of loops, the rated pressure of both the primary

and the secondary side, the maximum core power level, the maximum flow rate of primary

pumps, the general scaling factors and the connected circuits and systems. Volume, mass

flow and power are scaled to 1/100 full plant size [1,2,3]. The correct Froude number is

also maintained in the reactor coolant system (RCS) piping.

US RELAP5 base input model, which was developed according to the specified data, is

represented on Fig. 2.2. During post test analyses this model was upgraded to the middle and

large input model which is presented on figure 2.4 and 2.3 respectively. The models are

described in nodalization study in Section 4.

Page 1
pressure vessel

Figure 2.1: BETHSY facility

Page 2
0

tri

hladilna

zanka 3

hladilna hladilna C1d. 2 zanka I zanka 2 --

CD
La

ag0A

loop 3

Con, 3
STEAM GENERATOR DETAIL DISCRETIZATION OF

No.1 RCS LOOP

7440

REACTOR

VESSEL

SURGE

IINE

COLD LEG @

665 656

taLlummotall W-Mmu"al,

HOT LEG (9)

DOWNCOMER

BREAK

MODEL

000 U4

INTERMEDIATE LEG

Figure 2.4: RCS renodalization (from Fig. 2.3)

SiEAM GENEPRATR DETAIL DISGRETIZATION O

No. 1 AM LMP

J41

44'

REACTOR1

VESSEL

LMRE

LINE

WILD LEG @SI

WT LEG Q

BREAK

INTEWIATE LEG

Figure 2.5: RCS and RCP renodalization (RCP renodalization not shown on Fig. 2.3)

Page 5
3 Results

3.1 Pre-test calculations of test 9.1.b (ISP-27)

IJS has participated in the International Standard Problem No.27 (OECD ISP-27) based on

test 9.1.b. ISP-27 transient scenario involving a scaled 2" cold led break without high

pressure safety injection (HPSI) and with delayed operator action for secondary system

depressurization [4]. This transient leads to a large core uncover and fuel heat-up, requiring

the implementation of an ultimate procedure. The test was performed on December 19, 1989.

The scenario of the test starts at 10% nominal power (NP), the following actions are

achieved:

- t=O s: break opening (initiation of the transient)

- P+P (pressurizer pressure) = 13.1 MPa: Scram signal, the core power trip (from

10% NP) starts 17 s latter

- P+P=11.9MPa Safety injection signal, but no HPSI, turbine bypass and main

feedwater off

- 30 s after SI signal: Auxiliary feedwater on.

- 300 s after SI signal: Pump coastdown

- As the maximum core cladding temperature reaches 450°C: Implementation of the

ultimate procedure consisting in full opening of 3 steam dumps to atmosphere.

- P+P = 4.2 MPa: Accumulator injection starts, on the 2 intact loops only.

- P+P = 1.5 MPa: Accumulator isolation

- P+P = 0.91 MPa: LPIS injection starts, on the 2 intact loops only.

- When stable RHRS operating condition prevail: Core outlet fluid temperature <

177°C, P+P < 2.5 Mpa, saturation margin > 20°C, The transient is terminated.

US has performed blind pre-test and post-test analyses using computer codes

RELAP5/MOD2.36.05 and RELAP5/MOD3.1.

The pre-test simulations correspond quite well to the experimental data. The main

deficiency of pre-test analysis was the selection of the "cross" option for the break single

junction. Since the correct simulation of the break flow rate was shown to be extremely

important in order to determine the time evolution of a relatively long ISP-27 transient,

modelling of critical break discharge was studied in post-test analyses of ISP-27 [5]. It was

shown, that very good agreement between measured and RELAP5 predicted break flow can

be achieved when applying suitably adjusted discharge coefficients of single junction

component with abrupt area change and homogeneous junction options (junction flags). An

investigation of RELAP5 critical flow prediction for discharge of strongly subcooled liquid

was performed. The modification of MOD2 and MOD3 code versions was suggested to

correct the erroneous departure from subcooled choked flow condition, which occurs when

applying coupled abrupt area change and choking junction options [6].

Since the calculation of critical discharge through the break nozzle is strongly influenced

by the break boundary condition, in IJS post-test analyses an attempt was made to improve

the prediction of vapour void fraction in the broken No. 1 cold leg. Some other RELAP5

participants of ISP-27 also tried to improve their predictions of RCS void distribution during

post-test analyses [7,8].

Page 6
3.2 Post-test calculations of test 9.1.b (ISP-27)

A wide sensitivity study to improve the RCS void distribution, which was performed by

RELAP5/MOD3.1, dealt with following items:

- decrease of break discharge coefficients

- renodalization of downcomer to upper head bypass introducing the more precise description

of flow path

- introduction of homogeneous option for velocity calculation in reactor head junctions

- unrealistic reduction of bypass flow area and unrealistic increase of bypass hydraulic losses

- RCS renodalization increasing the number of nodes from 9 to 45 for RCS piping (Fig.

2.4), from 1 to 12 for core bypass, and from 1 to 14 for the reactor vessel downcomer

(Figs. 2.3 and 2.4)

- reduction of two-phase head and torque multipliers in RELAP5 reactor coolant pump

(RCP) model

- modifications of initial condition decreasing the average RCS temperature to the lower

margin of instrumentation uncertainty range (-0.5K) and increasing the RCS mass flow rate

to the upper margin of instrumentation accuracy (+ 3%)

- increase of RCS heat losses (+20%)

- increase of secondary heat sink changing the steam generator pressure control

- renodalization of reactor coolant pumps (Fig. 2.5).

1. No above parameter or model feature was found with significant influence on vapour

void fraction during the first transient phase up to the reactor coolant pumps trip. During

this phase the core generated steam bubbles (saturation condition) are driven with

(captured in) forced circulation flow - reactor coolant pumps remain running up to 300

seconds after the safety injection signal.

2. None of the above model modifications could essentially contribute to the reduction of

No.1 cold leg vapour void fraction during second transient phase following the reactor

coolant pumps trip.

In recent calculations the prediction of RCS coolant distribution was shown to be strongly

dependent on modelling of the connection from guide tube to upper head: due to the

misinterpretation, the annular orifice, J200 (located in guide tube), was connected to the

upper plenum instead of to the upper head. The correction of this model inadequacy has

improved the prediction of vapour void fraction in the broken No. 1 cold leg (comparison of

"base case" with "guid.renod." case on Fig. 3.1).

Furthermore, this guide tube renodalization resulted in the time shift of key transient

events, which can be observed by comparing the case "RCP+guide" with the base

"R5/MOD3.1" calculation on Figs. 3.2 to 3.12. Following the guide tube renodalization, the

core uncover and fuel temperature rise started earlier (Figs. 3.4 and 3.6), and therefore the

initiation of the "ultimate procedure" was also predicted to occur earlier (Fig. 3.11).

An additional MOD3.1 calculation is planned to be performed with vertical stratification

model turned off in guide tube volumes [7,9].

Page 7
In table 3.1 the measured data from experiment served as a initial conditions for BETHSY

model. Data uncertainties are also provided.

Table 3.1: Test 9.1 .b (ISP-27), initial condition

measured

([21; 10% nominal power)

± data uncertainties

BETHSY model

(RELAP5/MOD3.1

initialization)

core thermal power 2864 ± 30 kW 2864 kW

cold leg temperature 559.9 ± 0.5 K 560.3 K (core inlet)

downcomer mass flow rate 150.0 + 5.0 kg/s 154.3 kg/s

reactor coolant pump speed 2940 ± 30 rpm 2940 rpm

pressurizer pressure 155.1 ± 0.9 bar 155.1 bar

pressurizer level 4.08 ± 0.1 m 4.12 m

RCS coolant mass 1960 ± 40 kg 1948 kg

secondary side pressure 69.1 ± 0.4 bar 68.1 bar !

steam generator level (short range) 13.45 ± 0.05 m 13.45 m !

feedwater temperature 491.1 ± 2.0 K 491.0 K

secondary coolant mass (one SG) 820 ± 30 kg 821 kg !

RCS trace heating 53.5 kW no heat losses considering

the trace heating system on

! averaged for all the three steam generators

Page 8
junction 145-02 (J 200) connects

guide tubes and upper plenum

ISP-27: POST-TEST RELAP5/MOD3.1 CALCULATIONS

ALBFI: CLI spool piece void fraction ( )

1.2

reactor vessel

renodalization:

junction 145-02 redirected to upper head

ISP-27: POST-TEST, RELAP5/MOD3.1

ALBFI: CLI spool piece void fraction ( )

1.2

I ( i

Time (Iis)

Figure 3.1: The influence of guide tube renodalization

CD
CD

I1.

'00

W1

CD

C-9

co

N - -4 U)

t~I o6

(a U) 6

~~

--

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.. 0. t~

~, ~.

0.

-- S..

~'0 - C.)

CIO

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'0

CD,

-0 -

+ J

0*

a .- U 4 ~ -* 

* o Ca 0 Ca a Ca a

~1.

CDwH

CD

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p-a

'~0

-4

*0'

p-I

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'-I N

CD

p-I

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CD

U,

U,

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CD

-4

i.

pa

C'

-4

Ca 0

tCa

i.

CD

-a0
tSP-27: POST-TEST, RELAP5/MOD3.1

TF0S04G: core outlet steam temperature (K)

000.0

Time (win)

Figure 3.5: Test 9.1.b, Core outlet steam temperature

ISP-27: POST-TEST, RELAP5/MOD3.t

TKAX: mat. clad o. wall temperature (K)

1S00.0

Tiane (min)

Figure 3.6: Test 9.1.b, Maximum cladding temperature

ISP-27: POST-TEST. RELAP5/UOD3.1

ALOFI: CLI spool piece void fraction ( )

1.2

Time (min)

Figure 3.7: Test 9.1.b, No. 1 CL spool piece void fraction, base case

Page 11
ISP-27: POST-TEST, RELAP5/MOD3.1

ALBFI: CLI spool piece void fraction ( )

1.2

Time (min)

Figure 3.8: Test 9.1.b, No.1 CL void fraction, renod. of guide tube

ISP-27: POST-TEST, RELAP5/MOD3.1

QMB: break mass flow rate (kg/s)

3.0

Time (min)

Figure 3.9: Test 9.1.b, Break mass flow rate, base case

ISP-27: POST-TEST, RELAP5/MOD3.1

QMB: break mass flow rate (kg/s)

3.0

Time (min)

Figure 3.10: Test 9.1.b, Break mass flow rate, renod. of guide tube

Page 12
ISP-27: POST-TEST, RELAPS/MOD3.1

MGV2: SG2 secondary side mass inventory (kg)

1800.0

1600.0.

1400.0

1200.0

1000.0

600.0

600.0

0

NCP+S.id.

............. 20 40 s0 80

Time (min)

100 120 140

Figure 3.11: Test 9.1 .b, Secondary side mass inventory

ISP-27: POST-TEST, RELAP5/MOD3.1

INTQMB: break discharged mass (kg)

5400.0

4500.0.

3600.0

2700.0

1800.0

900.0

0.0

0

- -- --- -- ----------

20 40 60 60

Time (mrin)

100 120 140

Figure 3.12: Test 9.1.b, Break discharged mass

Page 13
3.3 RELAPS/MOD3.1.2 simulation realized at Texas A&M University

The time shift problem of RELAP5IMOD3.1 simulation did not appear in the last ISP-27

calculation, which has been performed at Texas A&M University by RELAP5/MOD3.1.2

code.

Base US input deck and restart input decks from the RELAP5/MOD3.1 simulation of ISP27 have been sent to A&M University for testing on a RELAP5/MOD3.1.2 simulation. The

results of the test have been returned to IJS and the conclusion was drawn that all the

transient differences observed on Figs. 3.13 to 3.21 comparing the cases "MOD3. 1" and

"MOD3.1.2" are caused only by code differences.

ISP-27: POST-TEST, RELAP5/MOD3

P+P: pressurizer top pressure (MPa)

18.0

UIAIU5EMMMT

15.0 1

12.0

* .0

0.0 .. ..

a 20 40 60 80 100 120 140

Time (min)

Figure 3.13: Test 9.1.b, Pressurizer pressure

ISP-27: POST-TEST. RELAP5/MOD3

P÷57: SG2 steam dome pressure (MPa)

9.0

Time (min)

Figure 3.14: Test 9.1.b, No.2 SG steam dome pressure

Page 14
ISP-27: POST-TEST. RELAPS/MOD3

ZT0200: core collapsed liquid level (m)

12.0

Time (min)

Figure 3.15: Test 9.1.b, Core collapsed liquid level

ISP-27: POST-TEST. RELAP5/MOD3

TF0304G: core outlet steam temperature (K)

900.0

Time (min)

Figure 3.16: Test 9.1.b, Core outlet steam temperature

ISP-27: POST-TEST, RELAP5/MOD3

TMAX: max. clad o. wall temperature (K)

1600.0

Time (min)

Figure 3.17: Test 9.1.b, Maximum cladding temperature

Page 15
ISP-27: POST-TEST. RELAP5/MOD3

ALBFI: CLI spool piece void fraction

1.2

1.0

0.8

0.6

0.4

0.2

0.0

Time (min)

Figure 3.18: Test 9.1.b, No.1 CL spool piece void fraction

ISP-27: POST-TEST, RELAP5/MOD3

QMB: break mass flow rate (kg/s)

3.0

2.5

2.0

1.0

0.8

0.0 ___________________________________________4

Time (min)

Figure 3.19: Test 9.1.b, Break mass flow rate

ISP-27: POST-TEST, RELAPS/MOD3

MGV2: SG2 secondary side mass inventory (kg)

1804.0

Time (min)

Figure 3.20: Test 9.1.b, Secondary side mass inventory

Page 16
ISP-27: POST-TEST, RELAP5/MOD3

INTQUB: break discharged mass (kg)

5400.0

u- II umZUlMNT

4600.0 1

.... .. O s.I.3

3600.0

2700.0

1300.0 1

100.0 1

0 .0 . . . . . . . . . . . . . .

0 20 40 60 80 100 120 140

Time (min)

Figure 3.21: Test 9.1.b, Break discharged mass

Page 17
4 Nodalization Study for BETHSY Experiment

4.1 Description

Some authors suggest that a more detailed nodalization should be utilized in order to

achieve better agreement between the calculated and experimental results. However, sometime

more detailed nodalization causes an oscillatory solution which requires a much smaller

currant and computing time step. In such situations CPU time can become excessive.

A comparison of existing experimental data of BETHSY experiment 9.1 .b with

simulation results of RELAP5/ MOD2, MOD3.1 and MOD3.1.2 is made.

The IJS RELAP5/MOD2 input model was developed and initialized according to the

specified data for each test. Each of the three coolant loops is represented explicitly without

taking into account the small asymmetry between the loops. This base input (Fig. 2.2)

consisted of 196 volumes, 207 junctions, 191 heat structures, 125 control variables and 13

trips. On this base RELAP5/MOD2 input model was further upgraded to RELAP5/MOD3.1

and RELAP5/MOD3.1.2. During post-test analyses, the base input model was renodalized,

increasing the number of nods in reactor coolant system pipping, reactor coolant pumps, core

bypass section and reactor vessel downcomer. The elevations of parallel volumes of the

reactor downcomer in bypass reactor core, hot leg and cold leg were preserved. Nodalization

of the reactor core, pressurizer, steam generators, reactor head, upper plenum and lower

plenum remained the same for middle input which is presented in figure 2.4. Further, middle

RELAP5 model was again upgraded, increasing the number of nods only in steam generator.

The detailed RELAP5 model of BETHSY facility contains 332 volumes, 343 junctions and

330 heat structures (Figs. 2.3, 2.4, 2.5). All three inputs based on different nodalization

should represent the same situation using different computer codes. These were assured with

strict consideration of RELAP5 code manuals. Table 4.1. presents number of volumes,

junctions, heat structures and mesh points for various inputs nodalization [10].

The comparison of experimental data with simulation results concentrated on only a few

important variables such as cold leg no#l spool piece void fraction, maximal clad

temperature, core collapsed liquid level and break mass flow rate [11,12,13].

Table 4.1.: Three nodalizations.

Nodalizations Volumes Junctions [_Heat Str./M.P.

Small Input 196 207 191/754

Middle Input 332 343 330/1290

Large Input 398 408 396/1554

Page 18
Con d. I

311

S I

L.C.

AFW

MF!

SG 1

Ia

11W m)y

Figure 4.1:" Steam generator nodaization for large input model

Page 19
ISP-27: POST-TEST, RELAP5/MOD2

TMAX: max. clad o. wall temperature (K)

1500.0

Time (rmin)

Figure 4.2: Maximal clad temperature calculated by RELAP5/MOD2 code.

ISP-27: POST-TEST, RELAP5/MOD31

TMAX: max. clad o. wall temperature (K)

1500.0

1300.0.- ...--- lol 11oo.o .... uo• la$-rndil

. MOD31-big

1100.0

000.0

700.0

500.0

5 0 0 .0 . . . . . . . . . . . . . f . . . . . . . . . I . . . . . . . .... . I . . . . . . . . . . . .

0 20 40 60 60 100 t20 140

Time (ruin)

Figure 4.3: Maximal clad temperature calculated by RELAP5/MOD3.1 code.

ISP-27: POST-TEST, RELAP5/MOD3.1.2

TMAX: max. clad o. wall temperature (K)

1500.0

-MIA3UUIXMBK

1t300.0 .... M3...2-o*l . .... i .t,-mtddle

--- -- M3,.I.-hbi

1100.0

900.0

700.0

500.0-

5300 .0 . .:. . . . . . . .I . . .. ................. . . . . . I. . . . s. . . . . , . .

0 20 40 60 80 100 120 140

Time (rain)

Figure 4.4: Maximal clad temperature calculated by RELAP5/MOD3.1.2 code.

Page 20
5 Run Statistics

The original RELAP5/MOD3.1 code with no modifications and with guidlines

consideration was used. Calculations were done on Sun Sparcstation 20 (4 processor

workstation) which uses multiuser and multitasking operating system SOLARIS 2.5.

The time step was limited at 1.OE-6 as a minimum time step and 2.OE-2 as a maximum

time step. During the calculation the thermodynamic property error (liquid phase property

error) at time 4119.642 sec. Therefore, restart calculation with the reduced maximum time

step of 1.OE-4 was applied for the next 50 seconds to overcome this.

The computational efficiency for middle nodalization (Table 4.1) is summarized in Table

5.1 14

Table 5.1.: Computational efficiency

Calculation Computer Time Number of time Number of volume Grind Time

(CPU), sec Step (DT) (N) CPU/(N*DT)

RELAP5/MOD3 72064 sec 491413 332 0.00044

Listing of the base input model and restart one are in Appendix A.

6 Conclusion

RELAP5/MOD3.1 computer code was used to simulate experiment performed on BETHSY

integral test facility (dealing with small break loss of coolant accidents). The main

discrepancies between the simulations presented and the measured data were found to be

connected with the predictions of critical discharge, collapsed core liquid level and loop seal

clearance phenomena. It should be noted that the reasons for all the problems encountered

are not yet well understood.

The wide RELAP5/MOD3.1 sensitivity study, which was performed to improve the

prediction of RCS void distribution for test 9.1.b (ISP-27), succeeded with the correction of

an input model inadequacy: the orifice J200 (located in guide tube) has been connected to the

upper plenum instead of to the upper head. Following this error correction, the prediction of

vapour void fraction in broken No. 1 cold leg was improved. Especially good agreement with

experimental data was achieved in the last ISP-27 simulation which was performed by

RELAP5/MOD3.1.2 code version at Texas A&M University.

In general, we found that a more detailed nodalization may lead to more accurate prediction

of void fraction but it also may lead to less accurate prediction of other variables, for example

maximal clad temperature (figures 2.2 through 2.4).

More detailed nodalization may also lead to an oscillatory solution which needs a very small

time step and therefore extensive CPU time. Such calculations can be very sensitive to certain

control volumes with regard to numerical stability resulting water property error.

Further, we found that for the most parameters and control variables there are no essential

differences between the results of the more detailed and less detailed nodalizations.

Comparison of the results of MOD2, MOD3.1 and MOD3.1.2 shows that in general the best

Page 21
results are obtained from MOD3.1.2. This version of RELAP5 code seams to be less

sensitive on users affects. What means that different manner of modelling the same flow path

are no more so sensitive.

The participation in BETHSY program provided additional knowledge which is needed for

good understanding of RCS phenomena during SB LOCA (e.g. RELAP5 simulation of DP

measurements observing the loop seal clearance phenomena). Further comparison of existing

experimental data with simulation results will lead to the modifications and improvements of

developed input models of experimental facilities and real plants. Experiences gained in

analyses of BETHSY experiments will also be used in simulations of real plant transients

which consider similar transient scenarios. Furthermore, US analyses also aim to answer

some basic questions concerning the effect on two-phase flows of scaling a commercial

nuclear plant down to the size of experimental facilities.

Page 22
7 References

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

2. BETHSY, Measurement System, Note SETh/LES/87-27, October 87

3. BETHSY, Data Base, Note SETH/LES/87-28, March 1988

4. T. Chataing, P. Clement: 2" Cold Leg Break without HPSI and with Delayed Ultimate

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

5. S. Petelin, B. Mavko, 0. Gortnar: RELAP5 Critical Flow Model Assessment,

Proceedings of the Conference Organized by British Nuclear Energy Society,

Manchester, May 1994.

6. S. Petelin, B. Mavko, 0. Gortnar: RELAP5 Critical Flow Model Assessment,

Proceedings of the Conference "Thermal Reactor Safety Assessment", Manchester,

May 1994.

7. G.R. Kimber, C.G. Richards: Assessment of RELAP5 via the Analysis of Selected

BETHSY Tests, 1993 RELAP5 International Users Seminar, Boston, Massachusetts,

July 1993.

8. F. De Pasquale, M. Sendar, N. Aksan: BETHSY 2" Cold Leg Break with Accident

Management Procedures, Blind- and Post Test Analysis Calculations Using the

RELAP5/MOD2.5 Code, PSI Report TM-42-92-01, December 1991.

9. G.Kimber, AEA Technology, Winfrith, UK, Private communication, 1994.

10. D.Dumont, G.Lavialle, B.Noel, R.Deruaz, Loos of Heat Remuval during Mid-loop

operation:BETHSY experiments, Nuclear Engineering and Design, Vol. 149, 365-374,

1994.

11. Charles P.Bott, Yassin A.Hassan, ISP 27Blind Test Analysis, OECD-CSNI ISP Final

Workshop-Grenoble, France, Jan. 14-15, 1992.

12. F.D'Auria, G.M.Galassi, OECD/CSNI ISP 27: Outline of the comparison between

blind prediction and experimental data, OECD-CSNI ISP Final Workshop-Grenoble,

France, Jan. 14-15, 1992.

13. S. Petelin, B. Mavko, I. Ravnikar, P. Cebull, Yassin Hassan, Nodalization study for

BETHSY experiment, Reactor Engineering Division, Institute "Joief Stefan",

University of Ljubljana, Ljubljana, SLovenia

14. S. Lee, B. D. Chung, H. J. Kim, Assessment of BETHSY Test 9.1.b Using

RELAP5/MOD3 - International Agreeement report, Korea Institute of Nuclear Safety,

June 1993

Page 23

APPENDIX A

Listing of the middle BETHSY nodalization

- base input

- restart input

Appendix A - Listing of the middle BETSY nodalization - base input

- bethsy - atandardni eksperiment; po 5.3.1991

* relap5/Sod3

* posttestni komentarji:

* podrobnejsa diskretizacija primarnih cevovodov

* tudi podrobnejsa diskretizacija toplotnih teles na RCS

cevovodih

* (trace-heating so nicer ugsanili 5610 po vbrizgu

akumulatorjev v 86.min)

a £ korekcijo: vueh ISP-27 DP tlacnih zeanaval po

renodalizaciji RCS (R.) * vseh 15P-27 VOImD senzorjev po renodalizaciji RCS (5*]

SRCP÷ dh renodalizacija RCr (i-.3 vol.)

* . : komenter najpomembnejsih dodatnih upremesh no 5X

gostejsi erezi S+*++* . is nbm .dat Je vzet realisticnl model bypasso v

glavo reaktorja * fff ; spremembe flsgov spojev v glavi resaktorja is 3-

centrally no 1-upward * bbb ; renod. obtoka 133 (1-'12 vol. in pipe(119,131,133)

fvcahs v:3-.0)

* d4d : renod. downcomerja 119 (S-.14 vol., elevacije

ustrerno uredici 131)

* ggg : spoj 145-03 (J200) pronesen no mesto 145-02 (J21)

* tokrat nobenih poizkusov a homogeno glavo!

10 t' znizanje Tcold reference a 560.35 K (+0.s K) na 559.35

R (-0.5 X)

* * 0 : povecanje mRCS no zgornjo tolerancno mejo 150 kg/s -.

155 kg/s

* ffll : potrebni izklop inicializacije toplotnega telesa

* rrXX, rrXXcc reaktorska posoda, rx ctv blok

* sagg. suggcc ; uparjolnik, ag ctv blok

* rrcc, rcp- * primarni cevovod, crpalka

• pprrzz, aline tlacnik, prelivnl vod

* ff, sill glavno napajanjoe, parovod

* 11p : lpsi in akumlatoli

* aaff. zzll pomozno napajanje in steam dump, cll zlom * hhes, hhll * blok toplotnib teles, model toplotnih izgub

• ccc, ccci : regulocijski siatem, reg. slates za

inicializacijo

* ccvv, ccvvLi blok kontrolnib spremenlJivk. b.k.s. zt

inicializacijo

* ttrr . blok tripov

• ddhh dh korekcija tlacnih zaznaval

* predtestni komentarji.

* : opozorilo ali pomanjkljivost

* * I uglasitev dp hidravlicnih isgub

* kkk a komentar

100 new tranont * 0 ... z izpisc.

* 100 new stdy-at

* 101 inp-chk

110 nitrogen

120 121010000 0.0 h2o prim

121 303010000 9.912 h2o sekl

122 403010000 9.912 h2o aek2

123 503010000 9.912 h20 sek3

201 200.0 1.0-6 0.1 3 100 1000 1000

••••. .•*.*•*•***. . •••• . .. * *•••••••.•.,* .. ...

s mee minor edit - initialization

'333 cntrlvar 305

*334 cntrlvar 303

'335 mflowJ 335000000

[kg/sl

'336 mflowj 334000000

-337 mflowj 332010000

' 38 mflowj 372000000

** ag 2

'341 p 410010000

*342 mflowj 411000000

'343 cntrlvar 405

*344 cntrivar 403

'345 mflowj 435000000

[kg/si

'346 mflowj 434000000

'347 mflowj 432010000

-348 mfloWj 472000000

** g 3

'351 p 510010000

*352 Mflowj 511000000

'353 catrivar 505

'354 cntrlvar 503

*355 emflowj 535000000

[kg/s]

*356 mflowj 534000000

'357 mflowj 532010000

*358 eflowi 572000000

'360 cntrlvor 235

• ap 1 sec. mass [kgi * ag 1 downcomer level (a)

* sg I recirculation faee flow

* mfw I mass flow - constant (kg/s)

* total feedl flow [kg/si

* steam dump I flow (kg/si

ug 2 pressure (pal

ug 2 steam flow (kg/mi

* sg 2 sec. Mass (kg)

•au 2 downcomer level (m]

* 9p 2 recirculation mass flow

mfw 2 mass flow - constant [kg/si

* total faed2 flow [kg/si

Ssteam dump 2 flow (kg/ul

* og 3 pressure [pal

* ag 3 steam flow (kg/si ag 3 sec. mass (kg)

* ag 3 downcomer level [mi

* up 3 recirculation mass flow

Smfw 3 mass flow - constant [kg/sa*

* total feed3 flow (kg/si

* steam dump 3 flow 1kg/si

h beat lossae

.. ZI

'301 cntrlvar 102

(kgi

'302 cntrlvar 120

*303 cntrlvar 110

'304 cntrlvar 111

'305 MflowJ 123010000

'306 mfiowJ 180000000

** prz

'307 p 203100000

'308 cntrlvar 203

'309 q 203010000

•" rca - loop 1 '310 tempf 602010000

'311 tempf 655010000

'312 mflowJ 611000000

'313 peyvel 701

** rca - loop 2

'314 tempf 802010000

*315 tompf 855010000

'316 flowj 811000000

'317 peovel 702

'318 mflowj 806000000

'319 mflowj 807000000

** rcs - loop 3

'320 tempf 902010000

'321 tempf 955010000

'322 mflowj 911000000

' 323 pepvel 703

'324 mflowj 906000000

'!325 mfIowj 907000000

'331 p 310010000

'332 mflowj 311000000

" reactor vessel inventory mass

* total core power Ckwi

* core level [m)

* reactor vessel level Cmi

" rx downcomer mass flow [kg/si

* cll break mass flow [kg/al

" prz pressure (pa)

prz level [a)

" heater power [wi

• loop 1 thot [k)

" loop 1 tcold [ki

• loop 1 loop mass flow [kg/sl

• loop 1 pump speed [red/si

* loop 2 thot 1k)

* loop 2 tcold (k]

* loop 2 loop mass flow 1kg/as

" loop 2 pump speed trad/si

a eccum. 2 mnss flow [kg/si

* lpai 2 mass flow [kg/si

* loop 3 thot (ki

" loop 3 tcold (k]

* loop 3 loop maas flow [kg/si

• loop 3 pump speed [rod/sI

•accum. 3 mass flow [kg/as

• lpai 3 mass flow [kg/s)

* sg 1 pressure (pai

• sg I steam flow [kg/s)

I

................ ..... ....

** prz:

'388 mflowj 232000000

'389 aflowj 712000000

" ag:

*390 cntrlvar 300

'391 cntrlvar 324

'392 mflowj 330000000

control

'393 cntriver 400

'394 cntrlvar 424

'395 mflowj 430000000

control

'396 cntrlver 500

'397 cntrlvar 524

'398 mflowj 530000000

control

* umprz flow

* umchar flow

* 11 delta tcold

* ag I recirculation control

* afw 1 mass flow - ag level

* 12 delta tcold

* ag 2 recirculstion control

* Afw 2 mass flow - ag level

* 13 delta tcold

* ag 3 recirculation control

* ofw 3 mass flow - ug level

" imne requested minor edit
'301 Voidg 603030000 * albcl: hit spool piece void

traction ( I R+

'302 vOidg 656070000 * albflt cli spool piece void

fraction ( I R÷

'303 voidg 803030000 * albc21 h12 Spool piece void

fraction I I at

*304 voidg 856070000 * albf21 12c spool piece void

fraction t I R+

'305 voidg 903040000 • albc3: hi3 spool piece void

fraction [ I Rt

'306 voidg 956070000 * albf3: c13 spool piece void

fraction I Rt

*'.. Op - p(low press. tap) - p(high press. tap)

'307 cntrlvar 240 * dp0200 t core heat. length diff.

press. [kpa!

'308 cntrlvar 241 * dpupl t upper plenum difft.

press. [kpae

'309 cntrlvar 242 * dp034 z guide tube dit. press. /kpe;

'310 cntrlvar 243 * Opuhead z upper head dif. press.

[kpe]

'311 catrivar 244 * dpOSO z downconmer to upp. head

dif. p. [kpa!

'312 catrivsr 245 * dporl pressure vessel dif.

press. [kpa]

*313 catrivar 246 - dpl : cli to hll diff. press.

(kpei

'314 cutrivar 247 * dplpg t pump I diff. press.

tkpal

'315 cntrlvAr 248 * dpl2vg & loop seal 1 doant, side

diff. p. Ckpal

'316 contrivar 249 * dpl2vp i loop seal I upflow, side

diff. p. ikpal

'317 cntrlvar 250 * dp2 c12 to h12 diff. press.

"'psi

"31B cntrivar 251 * dp22pg pump 2 diff. press.

(kpea

'319 cntrlvar 252 * dp22vg : loop seal 2 doGmt. side

diff. p. [kpal

*320 catrivar 253 * dp22vp : loop seal 2 upflow. side

diff. p. (kpal

'321 catrivar 254 * dp3 c i13 to h13 diff. press.

[kpeI

'322 cntrlvar 255 * dp32pg p mp 3 difft. press.

Okpae

*323 cntrlvar 256 * dpi2vg i loop seal 3 doanf. side

diff. p. [kpa]

'324 cntrivar 257 * dp32vp : loop seal 3 upflow, side

diff. p. (kpal

'325 cntrivar 258 * dp4 : egi u-tube in. to outlet

diff. p. Ikpae

'326 cntrivar 259 * dp4l sgl inlet plenum diff.

press. Ikpai

'327 cutrivar 260 - dp426 : sgl U-tube upflow side

diff. p. (kpa!

'328 cntrlvar 261 ' dp4r2 : egi boiler section diff.

press. (kpa]

'329 cntrlvar 262

dift. p. [kpe)

'330 cntrlvar 263

press. (kpai

'331 cntrlvar 264

diff. p. [kpa)

'332 catrlvar 265

press. [kIpa

'333 cntrlver 266

diff. p. (kpea

'334 cntrlvar 267

press. (kpa]

'335 cntrlvar 268

diff. p. [kpa!

'336 cntrlvar 269

press. (kpa]

'337 cntrlvar 270

[kpa) *÷.

'338 cntrlvar 271

mass flow (kg]

'339 cntrlvar 274

mass flow (kgS

'340 cntrlvar 305

invet. [kg]

*341 cntrlvar 405

invet. [kg]

'342 cntrlvar S0S

invet. (kg!

'343 cntrlvar 275

invetory (kg!

'344 catrivar 276

invetory (kg]

'345 cntrlvar 277

'346 cntrlvar 278

Impsl

'347 cotrivar 279

'348 cntrlvar 280

'349 cntrlvar 281

pressure [mpsa

'350 cntrlvar 282

pressure [opa!

'351 mflowj 123010000

[kg/si

'352 mtlowj 332010000

rate (kg/s]

'353 mflowJ 432010000

rate (kg/si

'3S4 mflowj 532010000

rate Ckg/s!

'355 mtlowj 180000000

[kg/s]

'356 mflowj 311000000

rate (kg/si

*357 tLflowj 411000000

rate [kg/s1

'358 mflowj 511000000

rate (kg/si

Sdps

• dpSl

• dp526

d dpSr2

• dp6

• dp61

" dp626

• dp6r2

:.0g2 u-tube in. to outlet

a sg2 inlet plenum Gift,

sg2 u-tube upflow side

sg2 boiler section diff.

eg3 u-tube in. to outlet

eg3 inlet plenum diff.

t sg3 u-tube upflow side

: sg3 boiler section diff.

* dppl a pressurizer diff. press.

" intqmb

' intqmsi

* mgvl

mm3

p.47

' p+57

p.67

• ptp

* ptsm2

' psm3

•qman3

' qman32

" qmgvll

* qmgvl2

"qegvl)

t time integrated break

time integrated lpsi

egl secondary side mass

s92 secondary side mass

sg3 secondary side mass

accumulator 2 mass

accumulator 3 mass

egi steam doam pressure

eg2 stem dome pressure

sg3 steam dome pressure

pressurizer top pressure

t accumulator 2 gas phase

i accumulator 3 gas phase

downcoer mass flow rate

sgl feedwater mass flow

sg2 feedwater meass flow

9g3 feedwater mass flow

t break mass flow rate

sl g steam line mass flow

: sg2 steam line mass flow

sg3 steam line mass flow

'359 mtlowj 807000000

rate (kg/si

*360 mflowj 907000000

rate (kg/si

'361 cntrivar 283

(kj/kg]

'362 tempt 123010000

Mk]

'363 tempf 141010000

[k!

'364 tempt 151010000

temperature (k]

*365 tempt 153010000

temperature [k) '366 tempt 602010000

(k)

'367 tempf 656050000

(k) RI '368 tempt 802010000

(k]

'369 tempt 856010000

(k] RI.

*370 tempf 902020000

(k) * 'a '371 tempt 956010000

(k] '*a

'372 tempt 309050000

temperature (k)

'373 tempt 409050000

temperature (k)

'374 tempt 509050000

temperature (k)

'375 httemp 131000701

*376 httemp 131000801

'377 httemp 131000901

middle to

'378 httesp 131001001

'379 httemp 131001101

tab.1 str.28/87)

'380 httemp 131001201

'381 cntrlvsr 146

(k)

'382 cntrlvar 286

[rpm)

'383 cntrlvar 287

*384 cntrlvar 288

(rpm,

'385 cntrlvar 289

-386 cntrlvar 290

'387 cntrlvar 110

'388 cntrlvar 291

*389 dt 0

transient (s)

*390 amass 0

' qmsbl2 : lpsi in c12 mass flow

" qmabl3 ipsi in c13 mass flow

" sebreak ibreak specific enthalpy

* tfo12&

' tf0304

" tf041

" tf042

* tfi12

" tf133

* tf212

* tf233

* tf312

" tf333

" tf4S4C

• tfS54c

" tfG54C

" tG02091 " tS02151

• ts02191

* ts02201

" ts02241

" ts02281

" tmax

core inlet temperature

a core outlet temperature

upper head (bottom)

upper head (top)

hot leg I temperature

cold leg I temperature

hot leg 2 temperature

cold leg 2 temperature

hot log 3 temperature

cold leg 3 temperature

bottom of sgI downcomer

bottom of sg2 dGoncomer

bottom of eg3 downcomer

rod temperature from

top core elevation 1k]

:++ to = 7 (e omemba v

max. clad temperature

" vp pump 1 rotation speed

Svp2 pump 2 rotation speed

" vp pump 3 rotation speed

• v+02

w V~trac

" ztO200

• zecore

core (electrical) power

trace heating (hke

core level (ma

swollen level (m)

G dtcalc : time step along

•eer : mass error (ksg

2
* comparison report variables request

301 cntrlvar 280 * p*p : PRESSURIZER TOP PRESSURE

[ePA)

302 cntrlvar 278 * p+57 : sg2 STEAM DOME PRESSURE

[mph]

303 antrlvar 163 * zt0200 CORE COLLAPSED LIQUID

LEVE (NI

* 304 tempg 131120000 * tf03046 : CORE OUTLET STEAM

TI4PM.ATURE 1k]

304 tempg 141010000 - tf03046

T3MRERATURR (k)

305 cntrlvar 146 * tsax

TEMPERATURE (k)

* 306 voidg 656010000 * albfl

FRACTION 1 1

306 voidg 656070000 * albfi

FRACTION I j R.

307 mflovj 180000000 * cMb

(EQ/SI

308 entrlvar 405 * mgV2

I•VRT. (KO0

309 cntrlvar 170 * mcp

310 cutrlvar 271 * intqub

(KG)

313 cntrlvar 110 * st02OO

LIQUID LE4VL IN[

CORE OUTLET STEMN

MAE. ClAD WALL I

cll SPOOL PIECE VOID

all SPOOL PIECE VOID

BREEK MASS FLOW RATE

sg2 SECONDARY SIDE MASS

PRIMARY MASS INVENTORY

BREAK DISCHARGED MASS

SInPL. CORE COLLAPSED

* 4 , p(low pressure tap) - p (high pressure tap)

* cv 240: dp0200: core heat. length diff. press. ft&p]

20524000 dp0200 sum 1.0e-03 0.0 1

20524001 0.0 1.0 p 123010000 -1.0 p 141010000 2.531 rho

131070000

- korakciJa: 0.25859.812.531

* cv 241: dpupl : upper plenum diff. press. [kpa]

20524100 dpupl sum 1.0-03 0.0 1

20524101 0.0 1.0 p 141010000 -1.0 p 147010000 13.400 rho

143010000

* korekCija: 1.366-9.81-13.400

* Cv 242:dp034 : guide tube dif. press. [kpa) *+. ni opisa v

bazi

20524200 dpupl sum 1.Oe-03 0.0 1

20524201 0.0 1.0 p 141010000 -1.0 p 153010000

• cv 243: dpuhead : upper head diff. press. [kpa)

20524300 dpupl sum l.Oe-03 0.0 1

20524301 0.0 1.0 p 151010000 -1.0 p 153010000 5.5B2 rho

151010000

• korekcijs: 0.569*9.81.5.582

* cv 244: dp050: downos•mer to upp. head dif. press. Ikpa)

20524400 dp050 sum 1.0e-03 0.0 1

20524401 0.0 1.0 p 111010000 -1.0 p 151010000 -3.267 rho

111010000

* korekcija: -0.333-9.81--3.267

* cv 245: dporl: pressure vessel dif. press. [kpa]

20524500 dpOrl sum 1.0e-03 0.0 1

20524501 0.0 1.0 p 123010000 -1.0 p 153010000 5.150 rho

212070000

* korekcija: 0.525*9.S15.150

* cv 252: dp22vg: loop seal 2 downflow side diff, press. [kpa)

20525200 dp22vg sum l.Oe-03 0.0 1

20525201 0.0 1.0 cntrlvar 823 -1.0 cntrivar 622

• cv 253: dp22vp: loop seal 2 upflowt side diff. press. (kpa)

20525300 dp22vp sum 1.Oe-03 0.0 1

20525301 0.0 1.0 cntrlvar 823 -1.0 cntrlvar 824

* cv 254:

20525400

20525401

* cv 255:

2052SS00

20525501

dp3: c13 to h13 diff. press. (cpa)

dp3 sum 1.0-03 0.0 1

0.0 1.0 p 956050000 -1.0 p 903010000 * R.

dp32pg: pump 3 diff. press. [kpa)

dp32pg um 1.Oe-03 0.0 1

0.0 1.0 cntrlvar 924 -1.0 p 955010000

* expanded minor edit requests

20800001 sathf 182010000 * liquid spec. enthalpy at sat. cond. (j/kgI

20800002 Sathg 182010000 * vapor spec. enthalpy at sat.

cond. (j/kcg

20800003 httemp 131000105 * cladding temperatures [k] (m.p.

t))

20800004 httemp 131000205 *

20800005 httemp 131000305 *

20800006 httemp 131000405 •

20800007 httemp 131000505 *

20800008 httemp 131000605 -

20800005 httemp 131000705 *

20800011 httemp 131000905 *

20800013 httemp 131001005 C

20600014 httemp 131001105 •

20800015 httemp 131001205 •

20800016 dt 0 * the current time step [s)

ccvV control variables for requested minor edit

- cv 246:

20524600

20524601

* cv 247:

20524700

20524701

• cv 248:

20524800

20524801

* cv 249:

20524900

20524901

* cv 250:

20525000

20525001

* cv 251:

20525100

20525101

dpl: cli to hil diff. press. (kpa]

41 sm 1.Oe-03 0.0 1

0.0 1.0 p 656090000 -1.0 p 603010000 * R+

dp12pg: pump I diff. press. [kpa)

dp12pg sum l.Oe-03 0.0 1

0.0 1.0 cntrlvar 624 -1.0 p 655010000

dp12vg: loop seal 1 downflow side diff. press. [kpa]

dpl2vg sum 1.Oe-03 0.0 1

0.0 1.0 cntrlvar 623 -1.0 cntrlvar 622

dp12vp: loop seal 1 upflowf side diff. press. kipa]

dpl2wp sum 1.Oe-03 0.0 1

0.0 1.0 cntrlvar 623 -1.0 cntrlvar 624

dp2: c12 to h12 diff, press. [kpa)

dp2 sum 1.0e-03 0.0 1

0.0 1.0 p 856050000 -1.0 p 803010000 - Rdp22pg: pump 2 diff. press. [kpa)

dp22pg sum 1.Oe-03 0.0 1

0.0 1.0 cntrlvar 824 -1.0 p 855010000

- cv 256: dp32vg: loop seal 3 downflot side diff. press. [kpa]

20525600 dp32vg sum l.Oe-03 0.0 1

20525601 0.0 1.0 cntrlvar 923 -1.0 cntrlvar 922

cv 257: dp32vp: loop seal 3 upflovf side diff. press. (kpa]

20525700 dp32vp sm l.0e-03 0.0 1

20525701 0.0 1.0 cntrlvar 923 -1.0 cntrlvar 924

cv 258: dp4: sgl u-tube in. to outlet diff. press. Jkpa]

20525900 dp4 sum l.0e-03 0.0 1

20525801 0.0 -1.0 p 301010000 1.0 p 313010000 * R.

• cv 259: dp4l: sgl inlet plenum diff. press. [kpa]

20525900 dp4l sum 1.0e-03 0.0 1

20525901 0.0 1.0 antrivar 620 -1.0 p 301010000

* cv 260: dp426: 591 u-tube upflow side diff. p. ['cpa)

20526000 dp426 sum 1.0e-03 0.0 1

20526001 0.0 1.0 p 301010000 -1.0 cntrlvar 621

c cv 261: dp4r2: g91 boiler section diff. press. (k'pa]

20526100 dp4r2 sum l.Oe-03 0.0 1

20526101 0.0 1.0 p 308010000 -1.0 p 310020000

* cv 262: dpS: sg2 u-tube in. to outlet diff. press. (kpa)

20526200 dp5 sum 1.Oe-03 0.0 1

20526201 0.0 -1.0 p 401010000 1.0 p 413010000 * R+

* cv 263: dp4l: sg2 inlet plenum diff. press. [kpa]

20526300 dpSl sum 1.0e-03 0.0 1

20526301 0.0 1.0 cntrlvar 820 -1.0 p 401010000

- cv 264: dp526: sg2 u-tube uptlow side diff. p. (kpa)

20526400 dp526 sum i.Oe-03 0.0 1

20526401 0.0 1.0 p 401010000 -1.0 cntrlvar 821

• cv 265: dpSr2: sg2 boiler section diff, press. (kpa)

20526500 dpSr2 sum 1.0-03 0.0 1

20526501 0.0 1.0 p 408010000 -1.0 p 410020000

• cv 266: dp6: s3 u-tube in. to outlet diff. press. [fta)

20526600 dp6 sum 1.Oe-03 0.0 1

20526601 0.0 -1.0 p 501010000 1.0 p 513010000 * Rf.

* cv 267: dp6l: sg3 inlet plenum diff. press. (kpa)

20526700 dp~l sm 1.00-03 0.0 1

3
20526701 0.0 1.0 cntrlvar 920 -1.0 p 501010000

: c, 266: dp6263 *g3 u-tube upflow side dift. p. [kpal

20526600 dp626 sum 1.0o-03 0.0 1

20526601 0.0 1.0 p 501010000 -1.0 cntrlvar 921

* cv 269: dp6r2: sgl boiler section dift. press. [kpal

20526900 dp6r2 sum 1.0e-03 0.0 1

20526901 0.0 1.0 p 506010000 -1.0 p 510020000

* cV 2701 dppl: pressurizer dift. press. [kpal

20527000 dppl sum 1.03-03 0.0 1

20527001 0.0 1.0 p 203010000 -1.0 p 203100000

* cv 271: intqwb: time integrated break mass flaw (kgl

20527100 intqmb integral 1.0 0.0 0 1 0.0

20527101 mflOwj 180000000

* cv 272: intsi2: time integrated lpsi 2 mass flow [kg]

20527200 intsi2 integral 1.0 0.0 0 1 0.0

20527201 aflowY 807000000

• cv 273: intui3: time integrated lpsi 2 mass flow [kgl

20527300 intei3 integral 1.0 0.0 0 1 0.0

20527301 utflowj 907000000

: ,V 274: intsi23: time integrated lpsi 2+3 mass flow [kg)

20527400 intsi23 sum 1.0 0.0 0 1 0.0

20527401 0.0 1.0 cntrlvar 272 1.0 cntrlvar 273

• CV 275: msm: accumulator 2 mass invetory [kg)

20527500 sm2 mult 1.0 0.0 1

20527501 acvliq 633 rhof 633010000

* cv 276: msm3: accumulator 3 mass invetory (kg)

20527600 m=m3 mult 1.0 0.0 1

20527601 acvliq 933 rhof 933010000

* cv 277: p+47: sgl steam dome pressure l[pa]

20527700 p-47 sum 1.Oe-06 0.0 1

20527701 0.0 1.0 p 310020000

* cV 278: p*57: Sg2 steam dams pressure impa

20527800 p+57 sum 1.0e-06 0.0 1

20527901 0.0 1.0 p 410020000

* cV 279: p#67: sg3 steam dome pressure [mpel

20527900 p.67 sum 1.Oe-06 0.0 1

20527901 0.0 1.0 p 510020000

: cv 280: p-p: pressurizer top pressure Impel

20528000 p*p sum 1.Oe-06 0.0 1

20528001 0.0 1.0 p 203100000

* cv 281: p*sm2: accumulator 2 gas phase pressure (opal

20528100 p+sm2 sum 1.Oe-06 0.0 1

20528101 0.0 1.0 p 633010000

• cv 282: p-sm3: accumulator 3 gas phase pressure (mpel

20526200 p.6m3 sum 1.Oe-06 0.0 1

20528201 0.0 1.0 p 933010000

* cv 283: sebreak: break specific enthalpy (kj/kgl ..

• h - xseathg + (1-x)*sathf

20526300 sebreak sum 1.Oe-03 0.0 1

20528301 0.0 1.0 cntrlvar 264 1.0 sathf 182010000 -1.0

cntrlvar 265

: cv 264: x*sathg (J/kgl

20528400 bvaph mul 1.0 0.0 1

20528401 quals 162010000 sathg 182010000

: cv 265: xsathf rI/kgl

20S28500 bliqh mult 1.0 0.0 1

20528501 qualm 182010000 sathf 162010000

* cv 295: sebreak: break specific enthalpy Ckj/kgl ..

* u - x-ug . (l-x)-ul

S h - u + p/rho

20529500 sebreak sum 1.00-03 0.0 1

20529501 0.0 1.0 cntrlvar 296 1.0 cntrlvar 299

* cv 296: x-ug [E/kg)

20529600 bvapu mult 1.0 0.0 1

20529601 quals 182010000 ug 162010000

• cv 297: x-ul (j/kgl

20529700 bliqu mult 1.0 0.0 1

20529701 quals 182010000 uf 162010000

• cl 296: u - x-ug (Il-x)ul [l/kg)

20529600 u sum 1.0 0.0 1

20529801 0.0 1.0 cntrivar 296 1.0 uf 162010000 -1.0

cntrivar 297

• cv 299: p/rho (J/kg]

20529900 bliqu div 1.0 0.0 1

20529901 rho 162010000 p 182010000

20529100 sscore constant 0.0

t........... •................ ... 

*ttrr tripi

*...........4t..*.*... 

501 time 0 gt null

603 -S01 or -501

break

503 p 203090000 It null

signal

.505 p 203090000 It null

signal

515 time 0 gt timsi

teed on

520 p 203090000 It null

injection

loops only 2,3

521 p 203090000 It null

accum.iasolation

0 1000.0 n * break

n noM 

0 131.0e+05 n a scram

0 119.0e+05 n * Si

of SOS 30.0 n - aux.

0 41.60.05 n * accum.

intact

0 14.6e,05 n *

526 cntrlvar 146

ultimate procedure

527 time 0

actuation on 91

626 527 and -526

procedure

657 -521 or -521

659 520 and 657

670 659 or 659

gt null 0 723.0

gt timeof 505 30.0

1 .

n * afw

* cv 266:

20528600

20528601

Scv 207: 20526700

20S26701

SCv 268:

20S26600

20526601

SCV 269:

20526900

20525901

• Cl290:

20529000

20529001

20210200

20210201

20210202

20210203

* cv 291:

vpl pump I rotation speed [rpm)

vpl mult 9.5493 0.0 1

pmpvel 701

vp2 pump 2 rotation spe"d (rpml

vp2 mult 9.5493 0.0 1

pmpvel 702

vp3 pump 3 rotation speed [rpm!

vp3 mult 9.5493 0.0 1

pmpvel 703

w•02: core power [kw]

w.02 function l.Oe-03 0.0 1

time 0 100

w.trac: trace heating Jkw]

wvtrac function 1.00-03 0.0

time 0 102

power 670 * accum. injection

-1.0 107.Se,03

0.0 107.se+03

1.0 0.0e,03

zscore: swollen level (am *.+

4

n

n

0

1

• afw: on 1 and Wefore ultimate

• prz pressure St 14.6 bar

" accumulator open trip

* trace heating off - -•heat lossea

*rrxxccvv rx control variables

4.*.... ............................ 

* ctv 100: core bypass inventory mass (kg) bbb

20510000 coremasS sum 1.0-3 0. 1

20510001 0.0 7.5047 rho 133010000 3.695S rho 133020000

c.bypeas

2051I002 3.6955 rho 133030000 3.6955 rho 133040000

20510003 3.6955 rho 133050000 3.6955 rho 133060000

20510004 3.6955 rho 133070000 3.6955 rho 133060000

20510005 3.6955 rho 133090000 3.6955 rho 133100000

20510006 3.69SS rho 133110000 7.S047 rho 133120000

ctv 101: core inventory mass (kg)

20510100 coremess sum 1.0-3 0. 1
20510101 0.0 22.5984 rho 131010000 11.1280 rho 131020000 *

core

20510102 11.1280 rho 131030000 11.1200 rho 131040000

20510103 11.1280 rho 131050000 11.1280 rho 131060000

20510104 11.1260 rho 131070000 11.1280 rho 131060000

20510105 11.1280 rho 131090000 11.1260 rho 131100000

20510106 11.1280 rho 131110000 22.5984 rho 131120000

* ctv 1021 reactor vessel inventory mass (kg)

20510200 veesmasm Eum 1.0-3 0. 1

20510201 0.0 20.2492 rho 111010000

upp.downc.

20510202 14.4648 rho 113010000 14.4648 rho 115010000

core inlet

20510203 14.4646 rho 117010000 *

core Inlet

* ddd *+ art.

20510204 31.9369 rho 119010000 31.9369 rho 119050000

downcemr

20510205 31.9369 rho 119070000 *

downcommer

20510206 18.3410 rho 119100000 27.9758 rho 119140000 *

docown r

20510207 65.9122 rho 121010000 67.3224 rho 123010000 *

low.head-plen.

20510208 68.3616 rho 125010000 *

core inlet

20510209 1000.0000 cltrlvar 101

core

20510210 1000.0000 cntrlvar 100

c.bypass bbb 20510211 69.9396 rho 141010000 98.7564 rho 143010000 *

upp.plen.

20510212 9.2200 rho 145010000 4

guide tube

20510213 110.1513 rho 147010000 *

upp.plen.

20510214 75.1600 rho 151010000 49.9430 rho 153010000 *

upp.head

* ctv 110: core level CM)

20511000 corelevl sum 1.0 0. 1

20511001 0.0 .528 voidf 131010000 0.26 voidf 131020000 0.26

void! 131030000

20511002 0.26 void! 131040000 0.26 void! 131050000 0.26

void! 131060000

20511003 0.26 void! 131070000 0.26 void! 131000000 0.26

voidf 131090000

20511004 0.26 void! 131100000 0.26 void! 131110000 .528

void! 131120000

* ctv 2111 reactor vessel level (a)

20511100 vesslevi sum 1.0 0. 1

20511101 0.0 0.4 voidf 121010000 0.6 void! 123010000 1.164

void! 125010000

20511102 1.0 ontrivar 110

20511103 .6645 voLdf 141010000 1.127 voidf 143010000 2.155

voidf 147010000

20511104 .4545 voidf 153010000

* ctv 120: reactor power (Me)

20512000 rktpower sum 1.0-3 2864. 1

20512001 0.0 1.0 q 131010000 1.0 q 131020000 1.0 q 131030000

20512002 1.0 q 131040000 1.0 q 131050000 1.0 q 131060000

20512003 1.0 q 131070000 1.0 q 131080000 1.0 q 131090000

20512004

20512005

1.0 q 131100000 1.0 q 131110000 1.0 q 131120000

1.0 q 133010000

* CtV 1461 maXimum httemp rx core, left surface

20514600 msxrxt stdfnctn 1.0 600. 1

20514601 max httesp 131000105 httewp 131000205

20514602 httemp 131000305 httemp 131000405

20514603 httemp 131000505 httemp 131000605

20514604 httemp 131000705 httewp 131000805

20514605 httemp 131000805 httemp 131001005

20514606 htteup 131000905 httemp 131001205

............. 4* .**...l .......... . .**

rrxx reactor vessel

***........4 ....** **4**********....................

* region 110: vessel inlet part + downconmer (upper * lower)

*.......*..*.l* .......... ..... ...... *

* • cosponent 111: upper downcommer - upper head connection * 1110000 dc-uphea branch

* 1110001 0

* 1110101 0. 4.09465 41.9464-3 0. 90. 2.1049 5.-s 5.893-2 00

geom v25-33+(v34*v35.v3Edel)/2

.+.. nov model bypassa v glavo

* V34:

1100000 v34 branch

1100001 1 1

1100101 0.0 0.4635 21.70650-03 0.0 90.0 0.4635 5.-S

0.250 00

1100200 100 l.58649e,07 1.248440.06 2.43927e+06 0.O0000e*00 * 1101101 110010000 111000000 1.901e-03 0.1 1.0 130000

• +÷ UTU.INDEL

1101101 110010000 111000000 1.9010-03 0.1 1.0 110000 fff

1101201 2.13960e.00 2.13960s+00 0.00000*.00

* v33-v26 upper downco r - upper head connection

1110000 dc-uphea branch

1110001 0

1110101 1.901e-03 3.1314 0.0 0.0 18. 1.1414 5.-S 0.0492

00

1110200 100 1.585590+07 1.24844e#06 2.43946e.06 0.00000e+00

* v2S:

1120000 v25 branch

1120001 1 1

1120101 0.0 0.S 13.0550-03 0.0 90.0 0.5 S.-5 0.170 00

1120200 100 1.58487e.07 1.248440+06 2.439655e06 0.00000+e00

1121101 111010000 112000000 1.901e-03 1.0 0.1 130000

÷. ENTR.9MO08L

1121201 2.13960ei00 2.139604.00 0.O0000e.00

•comonent 152: bypass into vessel head

1520000 hecdbyps valve * sngljun

• 1520101 112010000 151000000 2.454-4 0. 0. 100000 * gSem j2S

1520101 112010000 151000000 2.454-4 0. 0. 100000 * peam j25 fff

1520110 0.017 0.0 1.0 1.0

1520300 srvvlv

1520301 152

1520401 0.01 0.1 0.1

1520402 1.0 33.0 33.0

•ccci : ctv 152: flow regulation into vessel head

20515200 valveIS2 sum 1. 0.2956 0 3 0.01 1.

20515201 0.0306 -0.01 MflOwj 152000000 1.0 cntrlvar 152

4

Scomponent 113: vessel inlet (1 of 3)

1130000 vess-inl branch

1130001 3

* peam

(v34.v35.v36del)/6

1130101 0. 0.4635 7.2324-3 0. -90. -0.4635 5.-s 123.47-3 00

* 1131101 113000000 111000000 1.5612-2 2.1 2.1 130000 * pem

j35/3

1131101 113000000 110000000 1.5612-2 2.1 2.1 110000 * geam

j35/3 * ÷*.+ fff

1132101 113010000 119000000 1.5812-2 0.3 0.3 130000 * gSem

j35/3

1133101 656010000 113000000 1.09358-2 1. 1. 130000 * gesa

J340

Scomponent 115: vessel inlet (2 of 3)

1150000 vess-in2 branch

1150001 3

(v34+v3S+v36del)/6

1150101 0. 0.4635 7.2324-3 0. -90. -0.4635 5.-S 123.47-3 00

* 1151101 115000000 111000000 1.5612-2 2.1 2.1 130000 * pem

j35/3

1151101 115000000 110000000 1.5612-2 2.1 2.1 110000 gema

j35/3 * *+... fff

1152101 115010000 119000000 1.5612-2 0.3 0.3 130000 * peam

J35/3

1153101 856010000 115000000 1.09358-2 1. 1. 130000 * geom

j340

• component 117: vessel inlet (3 of 3)

1170000 vess-in3 branch

1170001 3

(v34*v35.v36del)/6

1170101 0. 0.4635 7.2324-3 0. -90. -0.4635 S.-S 123.47-3 00

- 1171101 117000000 111000000 1.5612-2 2.1 2.1 130000 * peao

J35/3

1171101 117000000 110000000 1.5612-2 2.1 2.1 110000 * pem

j35/3 . .** fff

1172101 117010000 119000000 1.5612-2 0.3 0.3 130000 - peaf j35/3

1173101 956010000 117000000 1.09358-2 1. 1. 130000 * pea

J340

5
* component 119: doncomner

* 1190000 downcomo pipe

* 1190001 5

* 1190101 0. S * 1190301 1.346833 3 0,779367 4 1.054 5 * geom

v36del+v37.v38-39.v40

* 1190401 31.9457-3 3 18.341-3 4 27.9758-3 S geom

v36del~v37.v38-39.v40

* 1190601 -90. 3 -39.3 4 -90. 5

* 1190701 -1.348933 3 -0.49405 4 -0.95406 5

* 1190801 S.-S 0.18 1 S.-S 0.1731 4 5.-s 0.04S 5 g 9eom J37-

j40.j41

* 1190901 0. 0. 2 0.83 0.83 4 * 1191001 0 5 * 1191101 100000 4

* component 119: downcommsr ddd

1190000 downcomm pipe

1190001 14

1190101 2.36-2 13 2.6S-2 14

1190301 0.6746 1 0.528 2 0.26 12 0.528 13 1,1640 14

1190601 -90. 14 * ÷÷ appr.

1190801 5.-S 0.10 1 S.-S 0.1731 13 S.-S 0.045 14

1190901 0. 0. 12 0.83 0.83 13

1191001 0 14

1191101 100000 13

* region 120: vessel bottom + lower plenum + core inlet

* component 121: bottom of reactor

1210000 botmhead englvol

1210101 0. 0.4 65.9122-3 0. 90.0 0.4 5.-5 44,8493-3 00 * eaom -

vI

* component 123: lower plenum

1230000 lower-pl breach

1230001 3

1230101 0. 0.6 87.3224-3 0. 90.0 0.6 5.-S 36.44-3 00 * geom

v2*v3,v4

*1231101 119010000 123010000 2.6543-2 0. 0. 00000 * 9eom

J41

1231101 119010000 123010000 2.6543-2 2.8 2.8 130000 * 9eov

141 * dodaten k

1232101 123010000 125000000 5.8910-2 1.8 1.8 130000 * geom iS

1233101 121010000 123000000 16.2858-2 0. 0. 130000 * geome 12

1231110 0.045 0.0 1.0 1.0

* component 125: core inlet

1250000 coreinIt branch

1250001 1

1250101 0. 1.164 68.3618-3 0. 90. 1.164 5.-S 15.8743-3 00

9eon vS.v6+vSO (del)

1251101 125010000 131000000 4.28-2 0. 0. 130000 - geom 16

• component 126: core bypass inlet junction

1260000 intobyps valve * sngl1un

1260101 125010000 133000000 0.2143-2 0. 0. 100000 * geov JS0

1260110 0.0147 0.0 1.0 1.0

1260300 srvvlv

1260301 126

1260401 0.01 0.1 0.1

1260402 1.0 33.0 33.0

* ccci : Ctv 126: flow regulation into core bypase

20512600 velvel2E sue 1. 0.6481 0 3 0. 1.

20512601 0.045 -0.01 mflowj 126000000 1.0 cntrlver 126

............

* region 130: core + core bypass

* component 131: core

1310000 core pipe

1310001 12

1310101 4.28-2 12 * 9eon J16.*7.8

1310301 0.528 1 0.26 11 0.528 12 gect v7

1310601 90. 12

1310801 5.-S 11.3-3 12 * geom j6.17.J8

1310901 0.1 0.1 11

1311001 00100 12

1311101 100000 11

1311401 0.0113 0.0 1.0 1.0 11

* component 133: core bypass * bbb

* 1330000 corebypa englvol

1 1330101 0. 3.656 51.9532-3 0. 90. 3.656 5.-5 24.7-3 00 geom

v50(del)

1330000 corebyps pipe * bbb

1330001 12

1330101 0.01421 12

1330301 0.528 1 0.26 11 0.528 12

1330601 90. 12

1330801 S.-S 24.7-3 12

1330901 0.0 0.0 11

1331001 00000 12

1331101 100000 11

1331401 24.7-3 0.0 1.0 1.0 11

* region 140: core outlet + upper plenum

Scomponent 141: region above the core

1410000 abovcore branch

1410001 3

1410101 0. 0.8645 69.9396-3 0. 90. 0.8645 S.-S 0.156 00 geom

v8-vllvSO(del)

1411101 131010000 141000000 0. 2.1 2.1 130000 *(geom J8)

1412101 133010000 141000000 0.2143-2 0. 0. 130000 * geom 50

1413101 141010000 143000000 8.799-2 1.8 1.8 130000 - 9eon J12

1412110 0.0147 0.0 1.0 1.0

* component 143: upper plenum

1430000 veselout branch

1430001 3

1430101 0. 0.5635 49.5814-3 0. 90. 0.5635 S.-S 0.2081 00 * geom

vl2(del)

1431101 143010000 603000000 1.09358-2 1.6 1.6 130000 * geon

J140

6

1432101 143010000 803000000 1.09358-2 1.6 1.6 130000 * gem 1140

1433101 143010000 903000000 1.09318-2 1.6 1.6 130000 - geoe

1140

component C 145: rcc guide tube

1450000 guid-tub branch

1450001 2

*1450101 0. 3.335 9.22-3 0. 90. 3.335 5.-5 0. 00 * 9ego v2o

1450101 0. 3.335 9.22-3 0. 90. 3.282 5.-s 0. 00 * gea v2O

zaradi 147010000 • 1451101 141010000 145000000 2.094-2 S. S. 130000 - geam 120

1451101 141010000 145000000 2.094-2 S. 5. 110000 * g9om J20

* fff

* 1452101 145010000 147010000 7.063-4 50. 50. 130000 * 9vom

1200

; 9gg 1452101 145010000 147010000 7.063-4 50. 50. 110000 * geom

1200 * fff

1452101 145010000 153000000 7.063-4 50. 50. 110000 • goem 1200

- fff

• M99 * 1453101 145010000 153000000 2.743-3 10. 10. 130000

9gem J21 * 999 1453101 145010000 153000000 2.743-3 10. 10. 110000 * gem

121 * fff

• component 147: upper plenum

1470000 upper-pl branch

1470001 1

1470101 0. 2.7185 159.3263-3 0. 90. 2.7185 5.-S 1.-1 00 * 9eom

v12 (del) -v19 • 1471101 143010000 147000000 0. 0. 0. 130000 *(geom J14)

1471101 143010000 147000000 0. 0. 0. 110000 *(geom J14) *

ftf

* region IS0: vessel upper head

• component 151: upper head (lower part, around upper plenum)

1510000 aro-uppl branch

1510001 1

1510101 0. 0.9035 75.1799-3 0. 90. 0.9035 S.-5 0.17 00 * 9ego

v23 (del) +v24

* 1511101 151010000 153000000 7.878-2 0. 0. 130000 * geom J23

or J24

1511101 151010000 153000000 7.878-2 0. 0. 110000 - geom J23 or

124 - fff

1511110 0.017 0.0 1.0 1.0

component 152: bypass into vessel head

* 1520000 heedbype valve * engljun

* 1520101 111010000 151000000 2.4S4-4 0. 0. 100000 * geom 125 1520110 S 0.017 0.0 1.0 1.0

1520300 S rervlv 1520301 152

• 1520401 0.01 0.1 0.1 • 1520402 1.0 33.0 33.0

• *ccci : ctv 152: flow regulation into vessel head

20515200 valvelS2 sum 1. 0.2956 0 3 0.01 1.

• 20515201 0.0306 -0.01 aflowj 152000000 1.0 cntrlvar 152
* component 153: upper head (upper part)

1530000 upp-head branch

1530001 1

1530101 0. 0.4545 49.9431-3 0. 90. 0.4545 5.-S 0.380 0 - goom

v21,v22÷v23(del)

* 1531101 147010000 153000000 7.06858-6 100. 110. 130000 * geoM

J190

1531101 147010000 153000000 7.06858-6 100. 110. 110000 * geom

J190 * fff

: ..............................................................

•*t•Q••t•

t

reactor vessel initial conditions - volumes

........tt....t..............t....t......t.t...................

1110200 100

1130200 100

1150200 100

1170200 100

* ddd

1191201 100

0. O0000e00

1191202 100

0.O000000+00

1191203 100

0.00000e00

1191204 100

0.O0000eO00

1191205 100

0.0000O+00

1191206 100

0.00000s+00

1191207 100

0. 000008+00

1191208 100

0.00000000

1191209 100

0.O0000e+00

1191210 100

0.O0000e+00

1191211 100

0.O00000O00

1191212 100

0.00000+00

1191213 100

0.O0000e*00

1191214 100

0. O0000e÷00

1210200 100

1230200 100

1250200 100

1311201 100

0.00000..00

1311202 100

0.0000eo00

1311203 100

0.O0000eO00

1311204 100

0.O0000eO0

1311205 100

0.000006400

1311206 100

0.00000O+00

1.58559e.07

1.58612t+07

1.s5612e+07

1.55612..07

1.$8421e+07

1

1.54•51e+07

2

1.58471e+07

3

1.58404e+07

4

1.58497e+07

S

1.58510o.07

6

1.58523s.07

7

1.58536e.07

8

1.58549e.07

9

1.58562*.07

10

1.58575e+07

11

1.505080e07

12

1.58607e.07

13

1.58432.407

14

1.58080e.07

1.580430.07

1.57808e+07

1.57614e407

1

1.57495e07

2

1.57414e+07

3

1.57333*.07

4

1.57252e.07

5

1.57171e.07

6

1.24844e-06

1.24844e+06

1.24•84e406

1.24844e+06

1.24844e+06

1.24844e+06

1.24844e+06

1.24844e+06

1.24844*+06

1.24044e+06

1.24844e+06

1.24844e+06

1.24845+.06

1.24845*+06

1.24045e+06

1.24845e+06

1.24845e06

1.248466.06

1.24592.+06

1.24846e+06

1.24847e.06

1.24994•e06

1.25088e+06

1.2S2100406

1. 25305506

1.255846÷06

1.25800o.06

2.43948e+06

2.43935e.06

2.43935o.06

2.43935o.06

2.43960e+06

2.43973e+06

2.43968e+06

2.43965e+06

2.43962*.06

2.43959e+06

2.439S6e.06

2.43953e+06

2.439509e06

2.43947*.06

2.439440.06

2.439410e06

2.43936eo06

2.43977e+06

2.44060e+06

2.44068$e06

2.44124e+06

2.44169e*06

2.441979.06

2.442166+06

2.44235e*06

2.44254a.06

2.442738,06

0.00000eO00

0.00000e000

0.00000e+00

0.O000000+00

0.O00000e00

0.00000e00

0.00000e00

0.O00000e+00

0.00000e+00

0.00000e+00

0.0000e00

0.00000..00

0.000006+00

0.O0000Oe00

0.00000e+00

0.O0000eO00

0.O0000e+00

0.00000.+00

0.O0000.00

0.00000.+00

0.O0000e+00

0.O0000e+00

0.00000e.00

0.000000e+00

0.000006+00

0.O0000e+00

0.O0000eO00

1311207 100

0.00000..00

1311208 100

0.O00000e+00

1311209 100

0.O0000eO00

1311210 100

0.O0000.00

1311211 100

0.O0000e*00

1311212 100

0.O0000 +00 * bbb

1331201 100

0.O0000e*00

1331202 100

0.0000e*00

1331203 100

0.O00000e00

1331204 100

0.O0000+00

1331205 100

0. 00000e+00

1331206 100

0.O0000eO+00

1331207 100

0.O00004O00

1331208 100

0.00000+e00

1331209 100

0.O0000eO00

1331210 100

0.0000+e00

1331211 100

0.O000006400

1331212 100

0.O0000e00

1410200 100

1430200 100

1450200 100

1470200 100

1510200 100

1530200 100

1.57090e+07

7

1.57009e.07

1.56928e+07

9

1.56847o.07

10

1.$6765e+07

11

1.56646e.07

12

1.56734e+07

1

1.56705Se07

2

1.56685e+07

3

1.556666007

4

1.56646.*07

S

1.56627e+07

6

1.56608o.07

7

1.56568@÷07

8

1.56569.+07

9

1.56550e+07

10

1.56530o+07

11

1.565012+07

12

1.56427*+07

1.56338$e07

1.56296*.07

1.562386+07

1.56303e.07

1.56253..07

1.26015e÷06

1.262140+06

1.263780.06

1.26506o+06

1.26597e+06

1.26741a.06

1.24866e+06

1.24893*+06

1.24931e+06

1.24985e+06

1.25055e+06

1.25141e.06

1.25243*.06

1.25355e+06

1.25473..06

1.25592e.06

1.257080+06

1.25027e906

1.26681e.06

1.26677e+06

1.24918s+06

1.240704.06

1.240430e06

1.24836e+06

2.44292e+06

2.44311e+06

2.44330e÷06

2.443490+06

2.44369eo06

2.44397*+06

2.44376e806

2.443836+06

2.443870.06

2.44392e+06

2.44397e+06

2.44401e+06

2.44406e.06

2.44410e906

2.44415..06

2.44419s.06

2.44424e+06

2.44431e*06

2.44448e*06

2.44469e.06

2.44479e+06

2.44493e+06

2.444780.06

2.44490e+06

0.O00000e00

0.00000+.00

0.O0000O.00

0.00000..00

0.00000e+00

0.000000+00

0.O00000e00

0.O0000e00

0.000006+00

O.O00000e÷00

0.000006+00

0.00000+e00

0.O00000+00

0.00000000

0.00000.+00

0.O000000+00

0.O00000+00

0.O0000O+00

0.O00000e*O0

0.00000e600

0.00000000

0.00000e+00

0O.0000O+00

0.O00000..00

1191305

1191306

1191307

1191308

1191309

1191310

1191311

1191312

1191313

1231201

1232201

1233201

1251201

1260201

1311301

1311302

1311303

1311304

1311305

1311306

1311307

1311306

1311309

1311310

1311311

* 1b3

1331301

1331302

1331303

1331304

1331305

1331306

1331307

1331308

1331309

1331310

1331311

1411201

1412201

1413201

1431201

1432201

1433201

1451201

8.60020e.00 0.960600e00 O.OOOOOe+00 5

8.60020e+00 5.96060+00 O0.000006+00 6

8.60020o.00 8.96060*.00 0.000000+00 7

8.60020e+00 8.96050e+00 0.00000e+00 8

8.60020eo00 8.96050eo00 0.O0000e+00 9

8.52830e.00 8.52830e.00 0.O0000+o00 10

8.60020e+00 8.96050e900 0.00000e+00 11

8.60010e*00 8.96040e+00 0.O0000e+00 12

0.60010e+00 8.96040e+00 0.00000e*00 13

7.64680e+00 7.64680e+00 0.O0000e+0

3.44560e+00 3.69440*+00 0.O0000+00

9.170820-10 9.172100-10 0.000006+00

4.60290e+00 4.00210..00 0.00000..00

0 2.79150e+00 2.79150e+00 0.00000e000

4.60620e+00 4.60620*.00 0.000006400 1

4.60830e+00 4.60830e.00 0.00000e+00 2

4.61120e+00 4.61120*.00 0.O0000O00 3

4.61480e+00 4.61480e+00 0.O0000oe00 4

4.619306+00 4.61930*+00 0.O0000e+00 5

4.62410e+00 4.62410e+00 0.O0000e+00 6

4.62890e+00 4.628900*+00 0.O0000e+00 7

4.63340e+00 4.63340.+00 0.00000e+00 8

4.637100+00 4.637100+00 0.00000+00 9

4.SS090a00 4.55090e+00 0.O0000+00 10

4.642100+00 4.64210e+00 0.00000e*00 11

4.21080e-01 4.22080e-01 0.00000e+00 1

4.21130e-01 4.21130e-01 0.O0000+00 2

4.21210.-Ol 4.21210.-01 0.O0000k+00 3

4.21320e-01 4.213200-01 0.O0000eO00 4

4.21460e-01 4.21460-o01 0.O0000eO+00 5

4.216306-01 4.21630o-01 0.O0000e.00 6

4.21830.-01 4.218300-01 0.O0000e00 7

4.22060.O01 4.22060e-01 0.00000e0O0 8

4.22300e-01 4.223006-01 0.O0000eO00 9

2.79150e+00 2.79150.+00 0.00000e.00 10

4.22770e-01 4.22770.-Ol 0.00000e+00 11

4.64540e+00 4.64540e÷00 0.00000e00

2.805009+00 2.805006+00 0.000006+00

2.37040e+00 2.58520e+00 0.O0000e+00

6.36860o*00 6.645900.00 0.O0000e00

6.36740.*00 6.64470e*00 0.00000e600

6.36740e+00 6.64470e+00 0.00000e00

-1.781300-01 -2.171500-01 0.000000.00

* reactor vessel initial conditions - junctions

1131201

1132201

1133201

1151201

1152201

1153201

1171201

1172201

1173201

* ddd

1191301

1191302

1191303

1191304

8.73255e-02

4.33350e+00

6.311206,00

8.660340-02

4.33340.+00

6.31000e900

8.660340-02

4.33340eo00

6.31000e900

8.60030e+00

8.60030e+00

8.600200+00

8.60020e.00

1.034509-01

4.56840e.00

6.31120e+00

1.02550o-0l

4.58830e+00

6.31000e÷00

1.02SSCo-01

4.56830e.00

6.31000l+00

5.96080e.00

8.96070*,00

8.96070.+00

8.96060e+00

7

0.O0000e+0

0.000000.00

0.O00000+00

0.O00000e00

0.000006+00

0.000006400

0.O0000O+00

0.O000006400

0.00000e+00

0.O0000eo00

0.O0000e÷00

0.O0000O+00

0.O0000eO00

1452201 4.75840e-01 4.75840e-01 0.O0000+00

* 1453201 -1.481800+00 -1.481800+00 0.000Oe00 * ggg

1471201 -s.80170e-03 -6.072050-03 0.000006+00

1511201 S.164•1e-02 S.56476e-02 0.O0000e00

1520201 0 1.65750e.01 1.65750e+01 0.O0000e+0

1531201 -5.50540e-o01 -S.SSSOe-Ol 0.O0000*O+00

hhes reactor vessel heat structures - active

4 reactor core: 428 heater rods - active part

11310000 12 6 2 1 0.

11310100 0 1

11310101 1 0.575-3 2 3.575-3 1 4.15-3 1 4.7S-3

11310201 2 4 1 5

1

2

3
11310301 0. 1 1. 3 0. S

11310401 570. 6

11310501 0 0 0

11310601 131010000 0 1

11310602 131020000 10000 1

11310603 131120000 0 1

11310701 100 0.0764624 0

0 0.0 12

1 225.964 1 - -0.528'428

1 111.25 11 * -0.26 *428

1 225.954 12 • -0.528*428

0 1

11310702 100 0.0490314 0 0 2

11310703 100 0.0682176 0 0 3

11310704 100 0.0674038 0 0 4

11310705 100 0.1051660 0 0 5

11310706 100 0.1136960 0 0 6

11310707 100 0.1136960 0 0 7

11310706 100 0.1051686 0 0 8

11310709 100 0.0874036 0 0 9

11310710 100 0.0662176 0 0 10

11310711 100 0.0490314 0 0 11

11310712 100 0.0764824 0 0 12

11310901 0.011875 10. 10. 0. 0. 0. 0. 1. 12

* tab 100: scram table

20210000 power 503 * power versus time

20210001

2864.0.3

20210002

2434.0.3

20210003

2005.0+3

20210004

1550.0+3

20210005

1170.0.3

20210006

990.0+3

20210007

854.0+3

20210006

726.0.3

20210009

662.0.3

20210010

510.0+3

20210011

340.0+3

20210012

-1.0 2864.0+3 0.0 2864.0+3 17.0

17.6 2720.0+3 19.0 2578.0.3 21.5

24.0 2290.0+3 26.8 2148.0.3 29.7

32.6 1862.0+3 36.0 1750.0+3 44.0

52.0 1385.0+3 63.0 1265.0+3 74.0

64.0 1110.0+3 94.0 1050.0÷3 104.0

123.0 964.0+3 153.0 906.0.3 198.0

273.0 812.0+3 37Y.0 750.0.3 423.0

523.0 706.0+3 623.0 680.0+3 723.0

623.0 647.0+3 923.0 629.0+3 1923.0

3123.0 439.0+3 5123.0 380.0+3 7123.0

9122.0 324.0+3 18123.0 271.0+3

• vessel inlet (cold leg connection)

11130000 3 3 2 1 0.123786

11130100 0 1

11130101 2 0.163047

11130201 1 2

11130301 0 2

11130401 560. 3

11130501 113010000 2000000 1 1 0.309 3 * 0.927/3-0.309

11130601 0 0 0 1 0.309 3

11130701 0 0. 0. 0. 3

11130801 0. 10. 10. 0. 0. 0. 0. 1. 3

- trefoil shaped piece

11131000 3 3 1 1 0.

11131100 0 1

11131101 2 6.-3

11131201 1 2

11131301 0 2

11131401 560. 3

11131501 113010000 2000000 1 1 0.11 3

11131601 11501000 2000000 1 1 0.11 2

11131602 113010000 0 1 1 0.11 3

11131701 0 0. 0. 0. 3

11131801 0 10. 10. 0. 0. 0. 0. 1. 3

11131901 0 10. 10. 0. 0. 0. 0. 1. 3

Sdowncommer (upper part): hhll * dd

11190000 13 3 2 1 86.1805-3

11190100 0 1

11190101 2 110.6706-3

11190201 1 2

11190301 1.0 2

11190401 560. 3

11190501 119010000 0 1 1 0.6746 1

11190502 119020000 0 1 1 0.5280 2

11190503 119030000 10000 1 1 0.2600 12

11190504 119130000 0 1 1 0.5280 13

11190601 0 0 0 1 0.6746 1

11190602 0 0 0 1 0.5280 2

11190603 0 0 0 1 0.2600 12

11190604 0 0 0 1 0.5280 13

11190701 10223 0.0714 0. 0. 13

11190601 0. 10. 10. 0. 0. 0. 0. 1. 13

* docommw r (lower part): hull * ddd

11191000 1 3 2 1 0.198776

11191100 0 1

11191101 2 0.236226

11191201 1 2

11191301 1.0 2

11191401 563. 3

11191501 119140000 0 1 1 1.164 1

11191601 0 0 0 1 1.164 1

11191701 10223 0.0714 0. 0. 1

11191801 0 10. 10. 0. 0. 0. 0. 1. 1

* boltto head

11210000 1 3 2 1 0.249359

11210100 0 1

11210101 2 0.322124

11210201 1 2

11210301 0 2

11210401 560. 3

11210501 121010000 0 1 1 0.4 1

11210601 0 0 0 1 0.4 1

11210701 0 0. 0. 0. 1

11210801 0. 10. 10. 0. 0. 0. 0. 1. 1

* reactor core: 428 heater rods - inactive part

'11211000 4 3 2 1 0.

11211000 2 3 2 1 0.

11211100 0 1

11211101 2 4.75-3

11211201 1 2

11211301 0 2

11211401 560. 3

'11211501 0 0 0 0 0.0 4

11211501 0 0 0 0 0.0 2

'11211601 121010000 0 1 1 171.200 1 * -0.400'428

*11211602 123010000 0 1 1 256.600 2 * -0.600'428

'11211603 125010000 0 1 1 496.192 3 * -1.164'428 '11211604 141010000 0 1 1 75.756 4 * -0.177'426

* coupled

11211601 123010000 0 1 1 926.192 1 - -(0.4-0.6'1.164)'428

11211602 141010000 0 1 1 75.756 2 * -0.177*428

'11211701 0 0. 0. 0. 4

*11211901 0 0. 0. 0. 4

11211701 0 0. 0. 0. 2

11211901 0 10. 10. 0. 0. 0. 0. 1. 2

* tie rods (8 rods)

'11212000 3 3 2 1 0.

11212000 1 3 2 1 0.

11212100 0 1

11212101 2 7.-3

11212201 1 2

11212301 0 2

11212401 560. 3

'11212501 0 0 0 1 0.0 3

11212501 0 0 0 1 0.0 1

'11212601 121010000 0 1 1 3.2 1 - 6'0.4

'11212602 123010000 0 1 1 4.8 2 * 8*0.6

'11212603 125010000 0 1 1 8.432 3 * 8"1.054

* coupled

11212601 123010000 0 1 1 16.432 1 * 8*(0.4.0.6.1.054)

'11212701 0 0. 0. 0. 3

'11212901 0 0. 0. 0. 3

11212701 0 0. 0. 0. 1

11212901 0 10. 10. 0. 0. 0. 0. 1. 1

' water chamber

11213000 1 3 1 1 0.

11213100 0 1

11213101 2 0.976426 * 0.162 M3 . 0.1323M3 + 4/3*0.02234 R3 (for

Water)

11213201 1 2

11213301 0 2

11213401 560. 3

11213501 121010000 0 1 1 0.166 1

11213601 0 0 0 1 0.166 1 * this end has 1SS c (cooling)

- ignored III

11213701 0 0. 0. 0. 1

11213801 0 10. 10. 0. 0. 0. 0. 1. 1

lower plenum: hhll

11230000 1 3 2 1 0.242895

11230100 0 1

11230101 2 0.274279

11230201 1 2

11230301 1.0 2

* huhs reactor vessel heat structures - passive

* upper downcer

11110000 1 3 2 1 0.022659

11110100 0 1

11110101 2 0.0434

11110201 1 2

11110301 0 2

11110401 560. 3

11110501 111010000 0 1 1 3.6313S 1

11110601 0 0 0 1 3.63135 1

11110701 0 0. 0. 0. 1

11110801 0. 10. 10. 0. 0. 0. 0. 1. 1
11230401 560. 3

11230501 123010000 0 1 1 0.6 1

11230601 0 0 0 1 0.6 1

11230701 10220 1. 0. 0. 1

11230801 0. 10. 10. 0. 0. 0. 0. 1. 1

* separation between core inlet and downcommer

11250000 1 3 2 1 0.1715

11250100 0 1

11250101 2 0.1765

11250201 1 2

11250301 0 2

11250401 560. 3

11250501 125010000 0 1 1 1.054 1

11250601 119140000 0 1 1 1.054 1 • ddd

11250701 0 0. 0. 0. 1

11250801 0. 10. 10. 0. 0. 0. 0. 1. 1

11250901 0. 10. 10. 0. 0. 0. 0. 1. 1

* guide thimbles

*11251000 16 3 2 1 4.-3

11251000 3 3 2 1 4.-3

11251100 0 1

11251101 2 6.-3

11251201 1 2

11251301 0 2

11251401 560. 3

'11251501 123010000 0 1 1 10.2 1 * 17"0.600

'11251502 125010000 0 1 1 21.106 2 * 17*1.054 + 29"0.11

'11251503 131010000 0 1 1 15.312 3 - 29'0.528

'11251504 131020000 0 1 1 7.54 13 * 29*0.260

•11251505 131120000 0 1 1 15.312 14 * 29'0.528

'11251506 141010000 0 1 1 13.363 15 - 17'0.177 . 12'0.8645

*11251507 143010000 0 1 1 12.397 16 * 11'1.127

'11251508 145010000 0 1 1 3.335 17 - 1'3.335 - praY8 dolzinb

'11251509 147010000 0 1 1 24.288 18 * 11*2.208 - preva dolzina

* coupled

11251501 125010000 0 1 1 84.32 1

17*(0.6+1.054).29k(0.11+0.528+0.26"5)

11251502 143010000 0 1 1 103.08 2 *

29"(0.26'5.0.526)+17'0.177.12"0.S645+

112"(1.127+2.208)

11251503 145010000 0 1 1 3.335 3 * 1-3.335 prava dolzina

'11251601 123010000 0 1 1 10.2 1 * 17-0,600

'11251602 125010000 0 1 1 21.106 2 * 17'1.054 + 29'0.11

'11251603 131010000 0 1 1 15.312 3 * 29'0.528

'11251604 131020000 0 1 1 7.54 13 * 29*0.260

'11251605 131120000 0 1 1 15.312 14 ' 290.528

'11251606 141010000 0 1 1 23.383 15 * 17"0.177 + 12*0.8645

'11251607 143010000 0 1 1 12.397 16 * 11'1.127

'11251608 145010000 0 1 1 3.335 17 * 1*3.335 - prava dolzina

*11251609 147010000 0 1 1 24.288 18 ' 11-2.208 - pram dolzina

* coupled

11251601 125010000 0 1 1 84.32 1

17'(0.6*1.054)+29'(0.11.0.528+0.26"5)

11251602 143010000 0 1 1 103.06 2 *

29*(0.26'5.0.528)*17'0.177+12'0.6645÷

11'2(1.227.2.206)

11251603 145010000 0 1 1 3.335 3 ' 1'3.335 -prava dolzina

'11251701 0 0. 0. 0. 16

*11251601 0 0. o. o. 16

*11251901 0 0. 0. 0. 18

11251701 0 0. 0. 0. 3

11251801 0 10. 10. 0. 0. 0. 0. 1. 3

11251901 0 10. 10. 0. 0. 0. 0. 1. 3

• core baffle * cylinder approximation * bbb

11311000 12 4 2 1 429.1437-3

11311100 0 1

11311101 3 429.7707-3

11311201 1 3

11311301 0 3

11311401 560. 4

11311501 131010000 10000 1 1 0.343 12

11311601 133010000 10000 1 1 0.343 12

11311701 0 0. 0. 0. 12

11311601 0 10. 10. 0. 0. 0. 0. 1. 12

11311901 0 10. 10. 0. 0. 0. 0. 1. 12

- core barrel (middle part): hhll * bbb

11330000 12 3 2 1 0.1715

11330100 0 1

11330101 2 0.202397

11330201 1 2

11330301 1.0 2

11330401 562. 3

11330501 133010000 10000 1 1 0.3136 12

11330601 0 0 0 1 0.3138 12

11330701 10221 0.0833 0. 0. 12

11330801 0. 10. 10. 0. 0. 0. 0. 1. 12

* core barrel (core outlet + vessel outlet + upper plenum)

11410000 3 3 2 1 0.1715

11410100 0 1

11410101 2 0.1995

11410201 1 2

11410301 0 2

11410401 563. 3

11410501 141010000 0 1 1 0.8645 1

11410502 143010000 0 1 1 1.127 2 * outlet nozzle neglected

11410503 147010000 0 1 1 0.6465 3

11410601 0 0 0 1 0.8645 1

11410602 0 0 0 1 1.127 2

11410603 0 0 0 1 0.6465 3

11410701 0 0. 0. 0. 3

11410801 0. 10. 10. 0. 0. 0. 0. 1. 3

* upper core plate, upper tie plate

11411000 1 3 1 1 0.

11411100 0 1

11411101 2 4.232-3

11411201 1 2

11411301 0 2

11411401 563. 3

11411501 0 0 0 1 0.3562 1

11411601 141010000 0 1 1 0.3562 1

11411701 0 0. 0. 0. 1

11411901 0 10. 10. 0. 0. 0. 0. 1. 1

tube around rcc guide tube

11430000 2 3 2 1 36.05-3

11430100 0 1

11430101 2 38.05-3

11430201 1 2

11430301 0 2

11430401 563. 3

11430501 143010000 0 1 1 0.4485 1

11430502 147010000 0 1 1 1.2515 2

9

11430601 143010000 0 1 1 0.4485 1

11430602 147010000 0 1 1 1.2515 2

11430701 0 0. 0. 0. 2

11430801 0. 10. 10. 0. 0. 0. 0. 1. 2

11430901 0. 10. 10. 0. 0. 0. 0. 1. 2

* rcc guide tube

11450000 2 4 2 1 30.15-3

11450100 0 1

11450101 3 31.76-3

11450201 1 3

11450301 0 3

11450401 563. 4

11450501 145010000 0 1 1 1.127 1

11450502 145010000 0 1 1 2.155 2

11450601 143010000 0 1 1 1.127 1

11450602 147010000 0 1 1 2.155 2

11450701 0 0. 0. 0. 2

11450801 0. 10. 10. 0. 0. 0. 0. 1. 2

11450901 0. 10. 10. 0. 0. 0. 0. 1. 2

• core barrel (upper plenum - upper part)

11470000 1 3 2 1 0.370907

11470100 0 1

11470101 2 0.404192

11470201 1 2

11470301 0 2

11470401 563. 3

11470501 147010000 0 1 1 0.659 1

11470601 0 0 0 1 0.669 1

11470701 0 0. 0. 0. 1

11470801 0. 10. 10. 0. 0. 0. 0. 1. 1

separation between upper plenum and upper head

11471000 1 4 1 1 0.

11471100 0 1

11471101 3 31.42-3

11471201 1 3

11471301 0 3

11471401 560. 4

11471501 147010000 0 1 1 0.734 1

11471601 151010000 0 1 1 0.734 1

11471701 0 0. 0. 0. 1

11471601 0 10. 10. 0. 0. 0. 0. 1. 1

11471901 0 10. 10. 0. 0. 0. 0. 1. 1

* vessel upper bead: hhll

11530000 1 3 1 1 0.

11530100 0 1

11530101 2 49.67-3

11530201 1 2

11530301 1.0 2

11530401 560. 3

11530501 153010000 0 1 1 1.587 1

11530601 0 0 0 1 1.667 1

11530701 10222 1. 0. 0. 1

11530801 0. 10. 10. 0. 0. 0. 0. 1. 1

* rrxxccvv control variables for pressure losses calculation -

ip
'20500900 pdII9-04 mult 0.5 0. 1

'20500901 rho 119040000 velt 119040000 velt 119040000

-20501000 pt119-04 sum 1.0 0. 1

*20501001 0. 1. cntrivar 9 1. p 119040000

'20501300 pd123-01 mult 0.5 0. 1

'20501301 rho 123010000 velt 123010000 velt 123010000

'20501400 pt123-01 sum 1.0 0. 1

'20501401 0. 1. cntrlvar 13 1. p 123010000

'20501900 p•119-04 sum 9.80665 0. 1

'20501901 0. 0.10197 cntrlvar 10 -4.7570 rho 119020000

'20502100 pS123-01 sum 9.80665 0. 1

'20502101 0. 0.10197 cntrlvor 14 -6.2581 rho 119030000

'20502700 pd655-01 mult 0.5 0. 1

-20502701 rho 655010000 volt 655010000 volt 655010000

'20502800 ptESS-01 sum 1.0 0. 1

'20502801 0. 1. catrlvar 27 1. p 655010000

'20503500 dp119-04 sum 1.-5 0. 1

'20501501 0. 1. cutrlvar 19 -1. cutrivar 28

'20503700 0p123-01 sum 1.-5 0. 1

'20503701 0. 1. catrivar 21 -1. c-trivar 28

:20504500 pdl4l-01 sult 0.5 0. 1

'20504501 rho 141010000 velt 141010000 vnlt 141010000

'20504600 ptl4l-01 Sum 1.0 0. 1

*20504601 0. 1. cotrlvar 45 1. p 141010000

'20504700 pd143-01 sult 0.5 0. 1

'20504701 rho 143010000 velt 143010000 velt 143010000

'20504800 pt143-01 sum 1.0 0. 1

'20504801 0. 1. cntrlvar 47 1. p 143010000

:20504900 pd603-01 sult 0.5 0. 1

'20504901 rho 603010000 velt 603010000 velt 603010000

*20505000 pt603-01 sum 1.0 0. 1

'20505001 0. 1. cntrlvar 49 1. p 603010000

'20505300 pg141-01 sum 9.80665 0. 1

'20505301 0. 0.10197 Cntrlvar 46 -0.7059 rho 131050000

'20505400 p9143-01 sum 9.80665 0. 1

*20505401 0. 0.10197 cntrlvar 48 +0.0082 rho 131060000

'20505500 p9603-01 sum 9.80665 0. 1

'20505501 0. 0.10197 cntrlvar 50 *0.2899 rho 131060000

'20505800 dpl4l-0l sum 1.-s 0. 1

'20505801 0. 1. cutrivar 53 -1. catrivar 28

'20505900 dp143-01 sum 1.-s 0. 1

'20505901 0. 1. cntrlvar 54 -1. c.trlvar 28

':20506000 dp603-01 sam 1.-5 0. 1

*20506001 0. 1. cntrlvar 55 -1. cntrlvar 28

* 5gg uparjalnik 1 3131201 6.67810*.00 6.96410o.00 0.00000.00

* prim. sistem: 9g tastop

6610000 sg-cl snqljun

'1 6610101 313010000 652000000 1.0936o-02 0.46 0.57 00100

6610101 313010000 652000000 1.0936e-02 0.01 0.02 130100

6610201 0 6.31550se00 6.53410e+00 0.00000e00

prim. sistem: Ng vstop

6110000 hl-ag sangljun

*! 6110101 602010000 301000000 1.0936e-02 0.57 0.46 00100

6110101 602010000 3010000000 1.09360-02 0.616 0.46 130100

6110201 0 6.36910e+00 6.57060o.00 0.00000e*.00

* prim. sistem: 5g vstopni prekat in u-csvi

3010000 sg-tube pipe

3010001 11

'! 3010101 0.04394 1 0.010342 11

3010101 0.04394 1 0.0103423 11

3010201 0 10

3010301 0.798 1 2.0 5 1.725 7 2.0 11

3010401 0 11

3010501 0 11

3010601 53.0 1 90.0 5 45.0 6 -45.0 7 -90.0 11

3010701 0.728 1 2.0 5 1.685 6 -1.685 7 -2.0 11

*01 3010801 0.le-03 0.091 1 0.Ole-03 0.01968 11

3010801 0.lo-05 0.091 1 0.Olo-07 0.01968 11

'! 3010901 0.44 0.60 1 0.01 0.01 5 0.22 0.22 6 0.01

0.01 10

3010901 0.01 0.01 1 0.0 0.0 10

3011001 00 11

*' 3011101 00100 1 00000 10

3011101 100000 10

3011201 103 1.555560.07 S.637460+02

3011202 103 1.551870+07 5.63172o,02

3011203 103 1.54826o.07 5.62658e+02

3011204 103 1.54465a.07 5.62198e+02

3011205 103 1.54105e+07 5.61785e.02

3011206 103 l.53770o.07 5.61455a.02

3011207 103 1.53586e.07 5.61159e+02

3011208 103 1.53523o.07 5.608664e02

3011209 103 1.53456e.07 5.60605e+02

3011210 103 1.533908:07 S.60379:.02

3011211 103 1.53324o.07 S.60181e+02

3011300 0

;8ek. sistem: dvizni kanal

3030000 riser pipe

3030001 6

3030101 0.0 6

3030201 0.01291 1 0.0214 4 0.048695 5

3030301 2.0 4 2.9605 5 0.8295 6

• povecanje mass sekundarnega hladils

-.. 3030401 0.11513 4 0.17171 5 0.04041 6

3030401 0.12S13 4 0.18171 5 0.04041 6

3030501 0 6

3030601 90.0 6

3030701 2.0 4 2.9605 5 0.8295 6

3030901 0.10-03 0.03503 5 0.lo-03 0.249 6

3030901 5.46 5.46 1 3.32 3.32 4 0.1 0.1 5

3031001 00 6

3031101 100100 4 100000 5

3031201 100 6.88631e.06 1.24544e+06 2.582760+06

0.O0000O.0 1

3031202 100 6.87343e+06 1.25147e+06 2.56289e+06

0.00000e00 2

3031203 100 6.86221a.06 1.25111o.06 2.582988o06

0.00000e.00 3

3031204 100 6.652370.06 1.25062o.06 2.58305o.06

0.00000+00 4

3031205 100 6.841220+06 1.25006e.06 2.58314o.06

0.00000 00 5

3031206 100 6.832860.06 1.24938oe06 2.56318o.06

0.00000e+00 6

3031300 0

3031301 4.72642:-02 2.73680o-01 0.00000o00 1

3031302 5.13242o-02 3.89180o-01 0.000 0 2

3031303 5.53470o-02 4.40650o-01 0.00000e+00 3

3031304 6.06003:-02 4.894600-01 0.00000÷o00 4

3031305 7.43034o-02 7.34730o-01 0.0OOO0e.00 S

3031401 0.027 0.0 1.0 1.0 5 * 4,

0.0O0000.00

0.00000e+00

0.00000+e00

0.00000e+00

0.00000e+00

0.00000e+00

0.O0000e+00

0.000000+00

0.00000e+00

0.00000+00

0.O0000ei.0

0

0

0

0

0

0

0

0

0

0

0

0 1

0 2

0 3

0 4

0 5

0 6

0 7

0 8

0 9

0 10

0 11

6.52550o-02

1.89420e-01

2.99440o-01

3.94750o-0l

4.19980e-01

4.017600-01

3011301 6.73470:+00 6.734700+00 0.00000e+00 1

3011302 6.725408+00 6.725400+00 0.00000o00 2

3011303 6.71720o.00 6.71720o+00 0.00000e+00 3

3011304 6.71000:.00 6.71000e+00 0.00000e00 4

3011305 6.703600+00 6.70360:.00 0.0000e.00 5

3011306 6.69850e+00 6.69850o+00 0.O00000.00 6

3011307 6.69390:+00 6.69390:000 0.000000000 7

3011308 6.68910o.00 6.68910o+00 0.00000Os00 8

3011309 6.68490e+00 6.68490e+00 0.000OOe00 9

3011310 5.86580*.00 5.665800+00 0.000000+00 10

3011401 .01968 0.0 1.0 1.0 10

prim. sistem: 09 izstopni prekat

3130000 o-ch branch

3130001 1 0

'1 3130101 0.0 0.798 35.0610-03 0.0 -65,0 -0.728 0.le-03

0.091 G0

3130101 0.0 0.798 35.061*-03 0.0 -85.0 -0.728 0.1-04

0.091 00

3130200 103 1.53426e+07 5.60188o+02

'1 3131101 301010000 313000000 0.010342 0.60 0.44 00100

3131101 301010000 313000000 0.0103423 0.3 0.2 130000

10

s aek. sistem: separator pare

3070000 separ separatr

3070001 3 0

3070101 0.0 1.9430 0.09467 0 90.0 1.9430 0.10-04 0.249

00

3070200 100 6.62485e+06 1.249230+06 2.58329o+06 1.46060o-01

3071101 307010000 310000000 4.8695e-02 0.82 0.14 01000

0.0

3072101 307000000 308000000 44.9150e-02 0.26 0.23 01000

0.0

3073101 303010000 307000000 4.8695e-02 0.0 0.0 01000

3071201 -9.27782e-02 3.063900-01 0.00000e+00

3072201 4.68546e-03 -1.70169o-02 0.00000e.00

3073201 7.22482e-02 7.615609-01 0.00000s.00

• sek. sistem: zgornji parni prostor

3100000 trdoomae pipe
3100001 2

3100101 0.0 2

3100201 0.0 1

3100301 1.0800 1 0.4000 2

3100401 0.54287 1 0.134040 2

3100501 0.0 2

3100601 90.0 2

3100701 1.0800 1 0.4000 2

3100601 0.1.-03 0.8000 1 0.le-03 0.41905 2

3100901 0.0 0.0 1

3101001 00 2

3101101 100000 1

3101201 102 6.818628.06 1.O0000e00 0.O0000e+00

3101202 102 6.81836e*06 1.00000 00 0.O0000Oe00

3101300 0

3101301 -9.29103e-03 4.43804.-02 0.00000e0 0

0 0 1 0 0 2

* ask. vistes: cpoj uparjalnika in parovoda

3110000 ag-al ungljun

3110101 310010000 320000000 0.0011401 0.222 1.0 130200

3110201 0 6.65870e+00 6.87160*+00 0.O0000e00

* mek. smstem: povratni kanal (tgornji obrocasti del)

3190000 udownanm branch

3190001 1 0

3190101 0.0 1.9430 0.3078 0 90.0 1.9430 0.le-03 0.1930

00

3190200 102 6.82490e006 8.101OOe-03

'3191101 310000000 319010000 0.44915 0.0 0.0 130100

3191101 310000000 319010000 0.0 0.5 0.5 130100

3191110 0.1930 0.0 1.0 1.0

3191201 3.04510e-01 3.70859e-04 0.00000..00

: sek. mistem: povratni kanal (srednji obrocasti del)

3080000 mSownann branch

3080001 2 0

3080101 0.0 0.8275 0.081723 0 -90.0 -0.8275 0.18-03

0.176 00

3080200 102 6.83412e+06 0.O0000e+00

3081101 319000000 308000000 0.0 0.09 0.15 130000

'3082101 308010000 309000000 0.030415 0.0 0.0 00100

3082101 308010000 309000000 0.0 0.43 0.60 130100

3081110 0.1930 0.0 1.0 1.0

3082110 0.1760 0.0 1.0 1.0

3081201 1.78363e-04 -3.00110*O01 0.00000e400

3082201 1.16890e-01 1.38490e-l 0.O0000e.00

3091300 0

3091301 4.67180k-01 4.671600-01 0.00000e800 1

3091302 4.67090e-01 4.67090e-01 0.O0000e.00 2

3091303 4.67090*-01 4,67090e-01 0.000006+00 3

3091304 4.67080e-01 4.67080.-al 0.00000*.00 4

3091410 0.0431 0.0 1.0 1.0 4

" oak. cistam: 8poj povratnegas in dviznega kanala

* ni -abrupt area change- models - regulacija recirkwlacije

3350000 drs valve

3350101 309010000 303000000 0,025761 0.0 0.0 100000

3350201 0 1.05820e-01 1.44390e-01 0.O0000e.00

3350300 crvvlv

3350301 324

3350401 0.01 0.01 0.01 * zaprto

3350402 1.0 1000.0 1000.0 * odprto

*ccci ugl recirkulacija: 4x : 4 ' 0.525 kg/c 2.100 kg/c

20532400 reg335 am 1.0 0.02846 0 3 0.01 1.0

20532401 0.0002100 -0.0001 edlowi 335000000 1.0 entrlvar

324

*20532400 reg335 constant 1.0

* hhsc toplotna telex& 89 1

13013000 10 4 2 1 0.00984

13013100 0 1

13013101 3 0.01111

13013201 3 3

13013301 0.0 3

13013401 S70.330 1 566.810 2 563.420 3 560.15 4

- prim. -- ,

13013501 301020000 0 1 1 68.0 1

13013502 301030000 0 1 1 68.0 2

13013503 301040000 0 1 1 68.0 3

13013504 301050000 0 1 1 68.0 4

13013505 301060000 0 1 1 58.65 S

13013506 301070000 0 1 1 58.65 6

13013507 301080000 0 1 1 68.0 7

13013508 301090000 0 1 1 66.0 8

13013509 301100000 0 1 1 68.0 9

13013510 301110000 0 1 1 68.0 10

* -- s cek.

13013601 303010000 0 1 1 68.0 1

13013602 303020000 0 1 1 68.0 2

13013603 303030000 0 1 1 68.0 3

13013604 303040000 0 1 1 68.0 4

13013605 303050000 0 1 1 56.65 5

13013606 303050000 0 1 1 58.65 6

13013607 303040000 0 1 1 68.0 7

13013608 303030000 0 1 1 66.0 8

13013609 303020000 0 1 1 68.0 9

13013610 303010000 0 1 1 68.0 10

13013701 0 0 0 0 10

13013801 0 10. 10. 0. 0. 0. 0. 1. 10

13013901 0 10. 10. 0. 0. 0. 0. 1. 10

II

* dividing plate in channel head

13011000 1 4 1 1 0.0

13011100 0 1

13011101 3 0.012

13011201 1 3

13011301 0.0 3

13011401 597.0 1 588.0 2 570.0 3

13011501 301010000 0 1 0 0.26643 1

13011601 313010000 0 1 0 0,26643 1

13011701 0 0 0 0 1

13011801 0 10. 10. 0. 0. 0. 0. 1. 1

13011901 0 10. 10. 0. 0. 0. 0. 1. 1

* cnannel head : zunanja stena --. plosca

13012000 2 4 1 1 0.0

13012100 0 1

13012101 3 0.0598

13012201 1 3

13012301 0.0 3

13012401 597.0 1 508.0 2 570.0 3 561.0 4

13012501 301010000 0 1 0 0.40167 1

13012502 313010000 0 1 0 0.40167 2

13012601 0 0 0 0 0.40167 1

13012602 0 0 0 0 0.40167 2

13012701 0 0 0 0 2

13012601 0 10. 10. 0. 0. 0. 0. 1. 2

13012901 0 10. 10. 0. 0. 0. 0. 1. 2

* tubeshnt

13014000 2 4 1 1 0.0

13014100 0 1

13014101 3 0.1645

13014201 1 3

13014301 0.0 3

13014401 597.0 1 588.0 2 S70.0 3 561.0 4

13014501 301010000 0 1 0 0.1139 1

13014502 313010000 0 1 0 0.1139 2

13014601 309050000 0 1 0 0.1139 1

13014602 303010000 0 1 0 0.1139 2

13014701 0 0 0 0 2

13014601 0 10. 10. 0. 0. 0. 0. 1. 2

13014901 0 10. 10. 0. 0. 0. 0. 1. 2

* riser (broz upper cylindrical *hell) --. plosca: hhll

13031000 S 4 1 1 0.0

13031100 0 1

13031101 3 0.0159

13031201 1 3

13031301 1.0 3

13031401 597.0 1 588.0 2 570.0 3 561.0 4

13031501 303010000 0 1 0 2.895 1

13031502 303020000 0 1 0 2.895 2

13031503 303030000 0 1 0 2.895 3

13031504 303040000 0 1 0 2.695 4

13031505 303050000 0 1 0 4.286 5

13031601 0 0 0 0 2.895 1

13031602 0 0 0 0 2.895 2

13031603 0 0 0 0 2.895 3

13031604 0 0 0 0 2.895 4

13031605 0 0 0 0 4.266 5

13031701 10225 0.2 0 0 5

13031801 0 10. 10. 0. 0. 0. 0. 1. 5

13031901 0 10. 10. 0. 0. 0. 0. 1. S

* upper-inner cylindrical chell --. plosca

13032000 2 4 1 1 0.0

561.0 4

* cek. sistem: povratni kanal (spodnji cevni del)

3090000 pipedown pipe

3090001 5

3090101 0.0 5

3090201 0.0 1 0.005836 4

3090301 2.9625 1 2.0 S

3090401 0.06909 1 0.01167 4 0.01456 5

3090501 0 5

3090601 -90.0 5

3090701 -2.9625 1 -2.0 S

3090601 0.1e-03 0.05963 1 0.le-03 0.0431 5

3090901 0.47 0.57 1 0.05 O.OS 4

3091001 00 S

3091101 100100 1 100000 4

3091201 103 6.84843e÷06 5.42776&+02 0.O0000ei00

3091202 103 6.06697e0.6 5.427886002 0.0000.00

3091203 103 6.86197e÷06 5.42799e.02 0.00000..00

3091204 103 6.89696e.06 S.42811e.02 0.O0000e.00

3091205 103 6.91201e.06 5.42849e*02 0.O0000e+00

0 0 1 0 0 2

0 0 3

0 0 4

0 0 5
13032100

13032101

13032201

13032301

13032401

13032501

13032502

13032601

13032602

13032701

13032801

13032901

0 1

3 0.006

1 3

0.0 3

597.0 1 588.0 2 570.0 3 561.0 4

308010000 0 1 0 0.6633 1

319010000 0 1 0 1.$537 2

303060000 0 1 0 0.6633 1

307010000 0 1 0 1.5537 2

0 0 0 0 2

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

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

* upper sleve and upper heed ---- plosce 13101.. .13104

13101000 1 4 1 1 0.0

13101100 0 1

13101101 3 0.0210

13101201 1 3

123101301 0.0 3

13101401 597.0 1 588.0 2 570.0 3 561.0 4

13101501 0 0 0 0 1.005 1

13101601 310020000 0 1 0 1.005 1

13101701 0 0 0 0 1

13101801 0 10. 10. 0. 0. 0. 0. 1. 1

13101901 .0 10. 10. 0. 0, 0. 0. 1. 1

13102000 1 4 1 1 0.0

13102100 0 1

13102101 3 0.0258

13102201 1 3

13102301 0.0 3

13102401 597.0 1 588.0 2 570.0 3 561.0 4

13102501 0 0 0 0 3.3870 1

13102601 310010000 0 1 0 3.3870 1

13102701 0 0 0 0 1

13102801 0 10. 10. 0. 0. 0. 0. 1. 1

13102901 0 10. 10. 0. 0. 0. 0. 1. 1

13103000 1 4 1 1 0.0

13103100 0 1

13103101 3 0.0947

13103201 1 3

13103301 0.0 3

13103401 597.0 1 588.0 2 570.0 3 561.0 4

13103501 0 0 0 0 0.4463 1

13103601 319010000 0 1 0 0.4463 1

13103701 0 0 0 0 1

13103801 0 10. 10. 0. 0. 0. 0. 1. 1

13103901 0 10. 10. 0. 0. 0. 0. 1. 1

13104000 1 4 1 1 0.0

13104100 0 1

13104101 3 0.0245

13104201 1 3

13104301 0.0 3

13104401 597.0 1 588.0 2 570.0 3 561.0 4

13104501 0 0 0 0 3.2448 1

13104601 308010000 0 1 0 3.2448 1

13104701 0 0 0 0 1

13104001 0 10. 10. 0. 0. 0. 0. 1. 1

13104901 0 10. 10. 0. 0. 0. 0. 1. 1

* downcomsr --. ploace 3091-01, 3092-01-02-03-04

13091000 1 4 1 1 0.0

13091100 0 1

13091101 3 0.00394

13091201

13091301

13091401

13091501

13091601

13091701

13091801

13091901

13092000

13092100

13092101

13092201

13092301

13092401

13092501

13092502

13092503

13092504

13092601

13092602

13092603

13092604

13092701

13092801

13092901

1 3

0.0 3

597.0 1 588.0 2 570.0 3

0 0 0 0 4.0116 1

309010000 0 1 0 4.0116 1

0 0 0 0 1

0 10. 10. 0. 0. 0. 0. 1. 1

0 10. 10. 0. 0. 0. 0. 1. 1

4 4 1 1 0.0

0 1

3 0.00276

1 3

0.0 3

597.0 1 588.0 2 570.0 3 561.0 4

0 0 0 0 1.2028 1

0 0 0 0 1.2028 2

0 0 0 0 1.2028 3

0 0 0 0 1.2028 4

309020000 0 1 0 1.2028 1

309030000 0 1 0 1.2028 2

309040000 0 1 0 1.2028 3

309050000 0 1 0 1.2029 4

0 0 0 0 4

0 10. 10. 0. 0. 0. 0. 1. 4

0 10. 10. 0. 0. 0. 0. 1. 4

561.0 4

............. ..... ...... 

* snggccvV• 1 kontrolne sprmenljivke

* cv 303: sgl: nivo v povratnem kanalu (m)

20530300 lsvdc sum 1.0 13.45 1

20530301 0.0 2.0 void! 309050000 2.0 void! 309040000

20530302 2.0 void! 309030000 2.0 void! 309020000

20530303 2.9625 void! 309010000 0.8275 voidf 308010000

20530304 1.9430 void! 319010000

* cv 305: sgl: masa sekundarnega hladila (Ikg

20530500 ssgmass sum 1.0 790.0 1

'++ 20530501 0.0 0.11513 rho 303010000 0.11513 rho

303020000

*÷t 20530502 0.11513 rho 303030000 0.11513 rho

303040000

-*i 20530503 0.17171 rho 303050000 0.04041 rho

303060000

20530501 0.0 0.12513 rho 303010000 0.12513 rho 303020000

20530502 0.12513 rho 303030000 0.12513 rho 303040000

20530503 0.18171 rho 303050000 0.04041 rho 303060000

20530504 0.09466 rho 307010000 0.54287 rho 310010000

20530505 0.13404 rho 310020000 0.30780 rho 319010000

20530506 0.08172 rho 308010000 0.06909 rho 309010000

20530507 0.01167 rho 309020000 0.01167 rho 309030000

20530508 0.01167 rho 309040000 0.01456 rho 309050000

• ma!! main feedwater 1

* konstantoni mw tok

3340000 wfv tmdpjun

3340101 331000000 332000000 0.0266

3340200 1 505 * si

3340201 -1.0 0.52517 0. 0.

3340202 0.0 0.52517 0. 0.

3340203 6.0 0.0 0. 0.

* volumaki mE w tok

'20530200 vufv div 1.0 0.0 1

'20530201 rhof 332010000 mflowj 332010000

* Eaedwater line

3320000 fwline branch

3320001 1 0

3320101 5.557e-04 10.0 0 0 60.0 7.0 0.01-03 0.0266 00

3320200 103 6.862718+06 4.90974e+02

'3321101 332010000 308000000 0.0006786 0. 0. 00100

3321101 332010000 308000000 0.0 1.0 0. 130100

3321201 1.11560e+00 1.11560e+00 0.00000e+00

- vir napajalne vode

3310000 !wsource tmdpvol

3310101 1.0 0.0 10.0 0 0 0 0.Ole-03 0.0 00

3310200 103

3310201 0 70.0+5 491.0

" ccci "regulacija" sgl nivoja

Sob konstantni mew 334 reguliramo nivo v povratnem kanalu

3290000 v329 tedpvol

3290101 1.0 0.0 10.0 0.0 0.0 0.0 0.20-03 0.0 0

3290200 103

3290201 0 70.0*S 491.0

3300000 J330 tedpjun

3300101 329000000 319010000 0.0

3300200 1 0 cntrlvar 303 * eg level

3300201 -1.0 0.0 0.0 0.0

3300202 13.35 1.5 0.0 0.0

3300203 13.45 0.0 0.0 0.0

3300204 13.55 -1.5 0.0 0.0

'3300000 J330 tmdpjun

'3300101 329000000 319010000 0.0

'3300200 1 0 cntrivar 305 * ag mass

'3300201 -1.0 0.0 0.0 0.0

'3300202 790.0 1.5 0.0 0.0

'3300203 800.0 0.0 0.0 0.0

'3300204 810.0 -0.50 0.0 0.0

* sell parovod 1

* steam line Erom porvlsv+miv

3200000 stmline snglvol

12
3200101 0.0 31.65 68.5-03 0 -45.0 -18.670 0.01-3 0.0525

00

3200200 102 6.612500.06 1.00000e.00

* bhas

* 13201000 1 4 2 1 0.0525

13201000 1 4 2 0 0.0525 * ffll

13201100 0 1

13201101 3 0.0603

13201201 1 3

13201301 0.0 3

13201401 570.330 1 566.810 2 563.420 3 560.15 4

13201501 320010000 0 1 1 31.65 1

13201601 0 0 0 1 31.65 1

13201701 0 0 0 0 1

13201801 0 10. 10. 0. 0. 0. 0. 1. 1

13201901 0 10. 10. 0. 0. 0. 0. 1. 1

* ccci regulacija tcold 1 preko tlaka sekundarne strani

* delta tcold : bethsy reference : 559.65 k

20530000 dtcold sum 1.0 0.0 0

20530001 560.35 -1.0 tempf 655010000

* 20530001 559.35 -1.0 tempf 655010000 * 10

20534400 p344 sum 1.0 68.12e.05 0

20534401 0.0 1.0 p 344010000 300. cntrlvar 300

3150000 venturi angljun

3150101 320010000 344000000 0.0 0.0 0.0 130000

3150201 0 6.89710e+00 6.89710e+00 0.O0000e.00

3440000 turbine tmdpvol

3440101 10.0 0.0 1000.0 0 0.0 0 0.2e-03 0 0

3440200 2 0 cntrlvar 344

3440201 -1.0 68.12e*05 1.0

3440202 1.Oe+05 1.0e.05 1.0

3440203 100.Oe05 100.0e+05 1.0

rrccss cevovodi primarnega kroga 1

* prim. sistem: hot leg do surge line

* 6030000 hleg englvol

6030101 0.010936 1.4441 0.0 0.0 0.0 0.0 0.le-03 0.1180

00

• 6030200 103 1.55957e.07 5.63790e+02

6030000 hleg pipe

6030001 5

6030101 0.010936 5

6030201 0.010936 4

6030301 0.28882 5

6030401 0.0 S

6030501 0.0 5

6030601 0.0 5

6030701 0.0 5

6030801 0.le-03 0.1180 5

6030901 0.0 0.0 4

6031001 00 5

6031101 100000 4 *fvcahg:v.O

* should be input as not used

6031201 103 1.559416+07 5.637626+02 0.O0000e00

6031202 103 1.55934e+07 5.63762e+02 0.O0000e+00

6031203 103 1.55927e+07 5.63762e+02 0.00000e.00

6031204 103 1.55920e+07 5.63762e+02 0.O0000e.00

6031205 103 1.55913e.07 5.637626+02 0.O00000.00

6031300 0

6031301 6.36880e,00 6.36880e600 0.O00000.00 1

6031302 6.36880a.00 6.36880e+00 0.O0000e.00 2

6031303 6.36880e.00 6.36880e+00 0.O000Oe.00 3

6031304 6.36880e.00 6.36880e.00 0.O0000e+00 4

0 0 1 0 0 2

0 0 3

0 0 4

0 0 5

* prim. sistem: hot leg spoj pri al

6130000 h1613 engljun

*1 6130101 603010000 602000000 0.0 0.0 0.0 00000

6130101 603010000 602000000 0.0 0.265 0.265 130000

6130201 0 6.36880e+00 6.36880e.00 0.O0000e+00

* • prim. Sistem: hot leg od sl do sg

* 6020000 hleg pipe

* 6020001 2

* 6020101 0.010936 2

6020201 0.010936 1

6020301 1.1891 1 1.8558 2

* 6020401 0.0 2

* 6020501 0.0 2

* 6020601 9.0 1 70.0 2

* 6020701 0.1800 1 1.7317 2

* 6020801 O.e-O03 0.1180 2

•! 6020901 0.32 0.31 2

6 6020901 0.24 0.24 1

6021001 00 2

6021101 100000 1

• 6021201 103 1.55880e,07 5.637906+02 0.O0000e+00 0 0 1

* 6021202 103 1.557380.07 5.63790e.02 0.00000e+00 0 0 2

* 6021300 0

6021301 6.29880e,00 6.29880e+00 0.O0000e00 1

6020000 hleg pipe

6020001 10

6020101 0.010936 10

6020201 0.010936 9

6020301 0.23782 5 0.37116 10

6020401 0.0 10

6020501 0.0 10

6020601 9.0 5 70.0 10

6020701 0.036 5 0.34634 10

6020801 0.10-03 0.1190 10

6020901 0.0267 0.0267 9

6021001 00 10

6021101 100000 5 100000 9 * v.0

6021201 103 1.55866e.07 5.63760e,02 0.O0000e+00 0 0 1

6021202 103 1.55853ei07 5.63760e.02 0.O0000O.00 0 0 2

6021203 103 1.558416.07 5.63760e+02 0.O0000O00 0 0 3

6021204 103 1.55828e.07 5.63759e.02 0.O0000e.00 0 0 4

6021205 103 1.55816e+07 5.637590+02 0.O00000.00 0 0 5

6021206 103 1.55791e+07 5.637580.02 0.000006+00 0 0 6

6021207 103 1.55752e+07 5.63757e.02 0.O0000e+00 0 0 7

6021208 103 1.55714e,07 5.637566+02 0.O0000e.00 0 0 8

6021210 103 1.55637e.07 5.637540.02 0.O0000e+00 0 0 10

6021300 0

6021301 6.36890e.00 6.36890e+00 0.00000e.0 1

6021302 6.36890*.00 6.3680e600 O0.00000e+00 2

6021303 6.36890e+00 6.36890e+00 0.O0000e.00 3

6021304 6.36890e+00 6.368900.00 0.O0000e00 4

6021305 6.36890e*00 6.36890e+00 0.O0000e+00 5

6021306 6.36890e.00 6.646806.00 0.000006+00 6

6021307 6.36900e.00 6.64680e+00 O0.00000e.00 7

6021308 6.36900e+00 6.646906+00 0.O00000.00 8

6021309 6.36900e+00 6.64700e+00 0.000006.00 9

sag

* 0

prim. uistem: intermediate leg down

* 6520000 ileg~a pipe

S 6520001 2

6520101 0.010936 2

* 6520201 0.010936 1

* 6520301 2.5122 1 2.0697 2

* 6520401 0.0 2

* 6520501 0.0 2

6520601 -76.0 1 -72.0 2

6520701 6 -2.4337 1 -1.9670 2

*! 6520801 0.le-03 0.1180 2

6520801 0.le-04 0.1180 2

* * 6520901 0.11 0.11 1

6520901 0.1 0.1 1

6521001 6 00 2

6521101 100000 1

* 6521201 103 1.53406e,07 5.60220e.02 0.O0000oe00 0 0 1

* 6521202 103 1.53517e.07 5.60220e+02 0.O0000e,00 0 0 2

* 6521300 0

• 6521301 6.246006.00 6.24600e+00 0.00000e+0 1

6520000 ilega pipe

6520001 10

6520101 0.010936 10

6520201 0.010936 9

6520301 0.50244 5 0.41394 10

6520401 0.0 10

6520501 0.0 10

6520601 -76.0 5 -72.0 10

6520701 -0.48674 5 -0.39340 10 *..

*t 6520801 0.le-03 0.1180 10

6520801 0.1-04 0.1180 10

*t 6520901 0.11 0.11 9

6520901 0.011 0.011 9

6521001 00 10

6521101 100000 9

6521201 103 1.53270e+07

6521202 103 1.53296e+07

6521203 103 1.533226.07

6521204 103 1.53348e+07

6521205 103 1.533746+07

6521206 103 1.53397e.07

6521207 103 1.53417e÷07

6521208 103 1.534386+07

6521209 103 1.53458e+07

6521210 103 1.53479e.07

6521300 0

5.60162e+02

5.60163e+02

S.60185e602

S.60186e.02

5.60187e+02

5.60188e÷02

S.60189e.02

S.60190e*02

5.60190e+02

5.60191e+02

0.O0000e00

0.O00000e00

0.O00000e00

0.O0000e+00

0.O0000e,00

0.O0000e.00

0.O00000e00

0.O0000e00

0.O0000e+00

0.O0000.00

0

0

0

0

0

0

0

0

0

0

0 1

0 2

0 3

0 4

0 5

0 6

0 7

0 8

0 9

0 10

6021209 103 1.556766.07 5.63755e602 0.00000e00

13

0 0 9 6521301 6.31560e+00 6.$9530e÷00 0.O00000e00 1
6521302 6.31560e.00 6.59520e+00 O.00000e.O0 2

6521303 6.31560e.00 6.S9520e+0O O.00000e.00 3

6521304 6.31560e.00 6.59510e.00 O.00000e+00 4

6521305 6.31560e.00 6.59510e.0O O.00000e0O S

6521306 6.31560e÷00 6.59510e.00 O.00000e.O0 6

6521307 6.31550e.00 6.59500e.00 0.00000eo.00 7

6521308 6.31550e+00 6.595000+00 O.00000oOO0 S

6521309 6.31550e.00 6.59500e.00 o.OOOOOei00 9

6630000 jun663 sngljun

*1 6630101 652010000 653000000 0.0 0.20 0.20 130000

6630101 652010000 653000000 0.0 0.0 0.0 130000

6630201 0 6.315500+00 6.59490e+00 0.O0000e÷00

* * prim. sistem: intermediate leg

* 6530000 ileg.b snglvol

* 6530101 0.010936 1.1027 0.0 0.0 9.0 0.180 0.1e-03

0.1180 00

- 6530200 103 1.53553e.07 5.60220es02

6530000 Llegb pipe

6530001 S

6530101 0.010936 5

6530201 0.010936 4

6530301 0.22054 5

6530401 0.0 5

6530501 0.0 5

6530601 9.0 S

6530701 0.036 5

6530801 O.le-03 0.1180 S

6530901 0.0 0.0 4

6531001 00 S

6531101 100000 4 *fvcahs:v-O

should be input as not used

6531201 103 1.534868+07 S.60192e÷02 0.O0O0Oe+00 0 0 1

6531202 103 1.53478e+07 S.60192e+02 0.O0000a.00 0 0 2

6531203 103 1.534700+07 S.6019104:02 0.O0000e0O0 0 0 3

6531204 103 1.534626+07 5.60191e+02 0.O0000e+00 0 0 4

6531205 103 1.534540+07 5.60191e.02 O.OOOOOe÷00 0 0 5

6531300 0

6531301 6.31550e+00 6.31550e+00 O.OOOOOe+O0 1

6631302 6.31550e+00 6.31550s.00 0.O0000.00 2

6531303 6.31550o.00 6.31550e.00 0.O0000e÷00 3

6531304 6.31550e÷00 6.31550se00 0.O0000e00 4

6640000 jun664 angljun

' 6640101 653010000 654000000 0.0 0.20 0.20 130000

6640101 653010000 654000000 0.0 0.0 0.0 130000

6640201 0 6.31550e+00 6.31550e.00 0.O00000.00

* * prim. sistes: intermediate leg up

* 6540000 ilegc snglvol

* *6$40101 0.010936 1.7870 0.0 0.0 90.0 1.7870 0.le-03

0.1180 00

* 6540101 0.010936 1.7871 0.0 0.0 90.0 1.7671 0.le-03

0.1180 00

* -*. podaljsek 0.1 -m zaradi sklenitve rcs elevacij v rx

(napalm base pod.)

6 6540200 103 1.53447e+07 5.60220e.02

6540000 liege pipe

6540001 5

6540101 0.010936 5

6540201 0.010936 4

6540301 0.35742 5

6540401 0.0 S

6540501

6540601

6540701

6540801

6540901

6541001

6541101

6541201

6S42202

6541203

6541204

6541205

6541300

6541301

6541302

6541303

6541304

0.0 5

90.0 5

0.35742 5

0.le-03 0.1180 5

0.0 0.0 4

00 5

100000 4 -fvca•h:v-O

should be input as not used

103 1.53433:007 5.60191e+02 0,O00000+O0 0 0 1

103 1.53398e.07 5.60190e,02 0.O0000e+O0 0 0 2

103 1.53363e.07 5.60189e+02 0.O0000e*00 0 0 3

103 1.53328e+07 5.601886.02 0.00000e.00 0 0 4

103 1.53293e÷07 5.60187e.02 0.O0000e+00 0 0 5

0

6.31560e+00 6.59500e.00 0.OOOOe+O0 1

6.31560ea00 6.59510e+00 0.O0000e+00 2

6.31560e.00 6.59520e.00 0.O0000O00 3

6.31560e+00 6.59520e+00 0.O000Oe.00 4

7016105 370.0 47.1 400.0 37.7

7016106 500.0 22.0 700.0 15.7

7016107 916.0 10.5 917.0 0.0

6010000 outl branch

6010001 1 0

6010101 0.0 0.064 5.460e-03 0.0 -90.0 -0.084 0.01g-04

0.0 00

6010200 100 1.56151e+07 1.24842ei06 2.44514e+06 0.00000+e00

6011101 601010000 655000000 0.0 0.0 0.0 130000

6011201 6.31570e÷00 6.59530e.00 0.oo000e+00

* hhll-hhes rcpl

17010000 1 3 1 1 0.0

17010100 0 1

17010101 2 0.1

17010201 1 2

17010301 1.0 2

17010401 560.0 3

17010501 701010000 0 1 1 1.0 1

17010601 0 0 0 1 1.0 1

17010701 10701 1.0 0.0 0.0 1

17010601 0. 10. 10. 0. 0. 0. 0. 1. 1

.......... ..... ....- *....

RCP. •

6000000 inl branch

6000001 1 0

6000101 0.010936 0.232 0.0 0.0 90.0 0.232 O.Ole-04 0.118

00

6000200 100 1.56151e.07 1.24842e.06 2.44514e+06 0.O00000.00

6001101 654010000 600000000 0.0 0.0 0.0 130000

6001201 6.31570e.00 6.S9530e+00 0.00000e*00

* pump loop 1

7010000 pump1 pump

7010101 0.0 0.097 14.0628e-03 0.0 60.0 0.084 00

7010108 600010000 0. 0.47 0.49 100000 *++ upor ustavlane

crpalke ?

7010109 601000000 0. 0.49 0.47 100000

7010200 0 1.56151e+07 1.24842e+06 2.44514e÷06 0.00000e+00

7010201 0 6.315700+00 6.59530e.00 0.O0000e+00

7010202 0 1.06000e.00 1.06000*+00 O.OOOOOe0

* pup index and option card

7010301 -2 0 -2 -1 0 505 0 * trip 505: si - pump 1

stop

* pump description card

-1 7010302 311.0 1.0 0.063056 78.0 0.0

7010302 311.0 1.0 0.067939 78.0 0.0

* 7010302 311.0 1.0 0.068797 78.0 0.0 * i5

7010303 5.0 751.0 0.0 0.0 74.39 71.39 0.0 *.. rated

density

* mh two phase pump bead multiplier tables

7013000 0 0.0 0.0. 0.2 0.0, 0.4 1.0, 0.9 1.0, 1.0

0.0

* •t two phase pump torque aultiplier tables

7013100 0 0.0 0.0. 0.2 0.0. 0.4 1.0, 0.9 1.0, 1.0

0.0

* pump velocity table (red/s)

7016100 SOS

7016101 300.0 311.0

7016102 305.0 201.0 310.0 141.1

7016103 320.0 113.1 330.0 88.0

7016104 340.0 75.4 350.0 62.8

14

* cv 701:

20570100

20570101

20270100

20270101

20270102

20270103

toplotne irgube - rcp 1,2,3

rcplhl function 1.0 0.0 1 3 -25000.0 0.0

time 0 701

reac-t 505 * si :rcp trip

-1.0 -25000.0

0.0 -25000.0

300.0 -4000.0

prim. sistem: cold leg a

6SS0000 cleoa branch

6550001 1 0

I 6550101 0.010936 1.8656 0.0 0.0 0.0 0.0 0.1e-03

0.1180 00

- 6550101 0.010936 1.8656 0.0 0.0 0.0 0.0 0.le-04 0.1180

00

• 6550101 0.010936 0.332 0.0 0.0 0.0 0.0 0.le-04 0.1160

00 * R+

6550101 0.010936 0.20763 0.0 0.0 0.0 0.0 O.le-04 0.1180

00 • RCP+

6550200 103 l.58753e.07 5.60350e+02

*1 6551101 655010000 656000000 0.0 0.07 0.07 00000

6551101 655010000 656000000 0.0 0.002 0.002 130000

6551201 6.31100e+00 6.31100e+00 0.O0000e+00

* * prim. sistem: cold leg b

* 6560000 cleg-b englvol * S, 6560101 0.010936 1.8656 0.0 0.0 0.0 0.0 0.1e-03

0.1160 00

- 6560201 0.010936 1.8656 0.0 0.0 0.0 0.0 0.1e-04 0.1180

00

- 6560200 103 1.58875e+07 5.60350e.02
6560000 cleg.h pipe R -. 6560001 9

6560101 0.010936 9

6560201 0.010936 8

6560301 0.3777 9

6560401 0.0 9

6560501 0.0 9

6560601 0.0 9

6560701 0.0 9

6560801 0.1e-03 0.1100 9

6560901 0.0 0.0 8

6561001 00 9

6561101 100000 6 *fvceahsjv.0

should be input as not used

6561201 103 1.567450.07 5.60350e.02 0.00000e00 0 0 1

6561202 103 1.587360e07 5.603490.02 0.00000*.00 0 0 2

6561203 103 1.58727e+07 5.60349e+02 0.O0000e.00 0 0 3

6561204 103 l.58718e+07 5.60349e÷02 0.00000e00 0 0 4

6561205 103 1.59709e÷07 5.60349*+02 0.00000e+00 0 0 5

6561206 103 1.507008.07 5.60349e.02 0.00000e+00 0 0 6

6561207 103 l.58691e.07 5.60349e.02 0.00000e+00 0 0 7

6561206 103 1.58662e.07 5.60349e802 0.00000e+00 0 0 £

6561209 103 1.58673e+07 5.60349e.02 0.00000e.00 0 0 9

6561300 0

6561301 6.31100@+00 6.31100e+00 0.00000e+00 1

6561302 6.31100e-00 6.31100e.00 0.O0000etO0 2

6561303 6.31100e*00 6.31100e+00 0.00000e+00 3

6561304 6.31100et00 6.31100e*00 0.00000e+00 4

6561305 6.31100e+00 6.31100e+00 0.00000e.00 S

6561306 6.31100e+00 6.31100@+00 0.00000@00 6

6561307 6.31100e.00 6.31100s00 0.00000+e00 7

6561308 6.31100e+00 6.31100e+00 0.00000.e00 6

* Miss toplotna telema - primarni cevovod 1

Svse toplotna telesa primarnih cevovodov so poenostavljena v

plosce

* * hot leg - cov a prirobnicami: hhll

* 16021000 3 4 1 1 0.0

* 16021100 0 1

* 16021101 3 0.0286

* 16021201 1 3

* 16021301 1.0 3

* 16021401 597.0 1 596.0 2 570.0 3 561.0 4

* 16021501 603010000 0 1 0 0.5353 1

* 16021502 602010000 0 1 0 0.4405 2

* 16021503 602020000 0 1 0 0.6879 3

* 16021601 0 0 0 0 0.5353 1

* 16021602 0 0 0 0 0.4400 2

* 16021603 0 0 0 0 0.6679 3

* 16021701 10226 0.333 0 0 3

* 16021601 0 10. 10. 0. 0. 0. 0. 1. 3

* 16021901 0 10. 10. 0. 0. 0. 0. 1. 3

* hot leg - cv s prirohnicami: hill

16021000 15 4 1 1 0.0

16021100 0 1

16021101 3 0.0286

16021201 1 3

16021301 1.0 3

16021401 597.0 1 568.0 2 570.0 3 561.0 4

16021501 603010000 10000 1 0 0.1070 S

16021502 602010000 10000 1 0 0.0661 10

16021503 602060000 10000 1 0 0.1376 15

16021601 0 0 0 0 0.1070 5

16021602 0 0 0 0 0.0881 10

16021603 0 0 0 0 0.1376 15

16021701 10226 0.0667 0 0 15

16021601 0 10. 10. 0. 0. 0. 0. 1. 15

16021901 0 10. 10. 0. 0. 0. 0. 1. 15

* * intermediate leg - cev a prirobnicami: hhll

* 16521000 4 4 1 1 0.0

* 16521100 0 1

* 16521101 3 0.0226

* 16521201 1 3

* 16521301 1.0 3

* 16521401 597.0 1 588.0 2 570.0 3 561.0 4 * 16521501 652010000 0 1 0 0.9313 1

* 16521502 652020000 0 1 0 0.7673 2

* 16521503 653010000 0 1 0 0.4068 3

* 16521504 654010000 0 1 0 0.6625 4

* 16521601 0 0 0 0 0.9313 1

* 16521602 0 0 0 0 0.7673 2

2 16521603 0 0 0 0 0.4088 3

* 16521604 0 0 0 0 0.6625 4

16521701 S 10224 0.166 0 0 4

* 16521001 0 10. 10. 0. 0. 0. 0. 1. 4

* 16521901 0 10. 10. 0. 0. 0. 0. 1. 4

* intermediate leg - cvy * prirobnicami: hhll

16521000 20 4 1 1 0.0

16521100 0 1

16521101 3 0.0226

16521201 1 3

16521301 1.0 3

16521401 597.0 1 568.0 2 570.0 3 561.0 4

16521501 652010000 10000 1 0 0.1663 5

16521502 652060000 10000 1 0 0.1535 10

16521503 653010000 10000 1 0 0.0618 15

16521504 654010000 10000 1 0 0.1325 20

16521601 0 0 0 0 0.1863 S

16521602 0 0 0 0 0.1535 10

16521603 0 0 0 0 0.0818 15

16521604 0 0 0 0 0.1325 20

16521701 10224 0.0332 0 0 20

16521801 0 10. 10. 0. 0. 0. 0. 1. 20

16521901 0 10. 10. 0. 0. 0. 0. 1. 20

*cold c leg - cov a prirobnicami: hhll

* 16551000 2 4 1 1 0.0

2 16551100 0 1

* 16551101 3 0.0279

* 16551201 1 3

* 16551301 1.0 3

* 16551401 597.0 1 568.0 2 570.0 3 561.0 4

* 16551501 655010000 0 1 0 0.6915 1

* 16551502 656010000 0 1 0 0.6915 2

* 16551601 0 0 0 0 0.6915 1

* 16551602 0 0 0 0 0.6915 2

* 16551701 10224 0.166 0 0 2

* 16551601 0 10. 10. 0. 0. 0. 0. 1. 2

* 16551901 0 10. 10. 0. 0. 0. 0. 1. 2

* cold leg - cev s prirobticami: hhll

16551000 10 4 1 1 0.0

15

16551100

16551101

16551201

16551301

16551401

16551501

16551502

16551601

16551602

16551701

16551601

16551901

0 1

3 0.0279

1 3

1.0 3

597.0 1 588.0 2 570.0 3 561.0 4

655010000 0 1 0 0.1383 1

656010000 10000 1 0 0.1383 10 * R.

0 0 0 0 0.1383 1

0 0 0 0 0.1383 10

10224 0.0332 0 0 10

0 10. 10. 0. 0. 0. 0. 1. 10

0 10. 10. 0. 0. 0. 0. 1. 10

* ddhhl : dh korekcija nekaterih rcil tlacnih zagnaval

* cv 620 a dh korigirano tlacno zaznavalo 602-10 (pal

20562000 pk60202 sum 9.8067 0.0 1

20562001 0.0 0.10197 p 602100000 -0.15 rho 602100000 * Rf

* cv 621 : dh korigirano tlacno zaznavalo 301-06 (pal

20562100 pk30106 sum 9.8067 0.0 1

20562101 0.0 0.10197 p 301060000 -0.8425 rho 301060000

* cv 622 dh korigirano tlacno zasnavalo 652-01 (pal

20562200 pk65201 sm 9.6067 0.0 1

20562201 0.0 0.10197 p 652010000 -0.15 rho 652010000 * R.

* cv 623 a dh korigirano tlacno zatnavalo 652-10 (pal

20562300 pk65202 mau 9.8067 0.0 1

20562301 0.0 0.10197 p 652100000 0.15 rho 652100000 * R.

cv 624 dh korigirano tlacno zaznavalo 654-05 [pal

20562400 pk65401 sum 9.8067 0.0 1

20562401 0.0 0.10197 p 654050000 -0.15 rho 654050000 - R.

ccvvii dpmeasured - gravity term - zanka I

** ta blok cv Je uporabIjan med rcsl Op inicializacijo

upostevane so vne dh korekcije tlacnih zaznaval

** cv 630 a Opillh Car)

"20563000 dpllh mm l.Os-OS -0.0763 0

*20563001 0.0 1.0 p 602010000 -1.0 p 603010000 * dh-0.Om

cv 631 1 dpllv (bar)

*20563100 dpllv sum 1.00-05 -0.0792 0

**20563101 0.0 1.0 p 602020000 -1.0 p 602010000 1.0

cntrlvsr 632

*20563101 0.0 1.0 cntrlvar 620 -1.0 p 602010000 1.0

cntrlvar 632

v• 632 . dpllv gravity term [pal
'20563200 dpgt OuR 9.8067 0.0 1

'20563201 0.0 1.7317 rho 602010000

** cv 633 : dp4l [bar] *20563300 dp4l sum 1.0e-05 -0.0562 0

**20563301 0.0 1.0 p 301010000 -1.0 p 602020000 1.0

cntrlvar 634

*20563301 0.0 1.0 p 301010000 -1.0 cntrlvar 620 1.0

cntrlvar 634

** cv 634 dp4l gravity term [pal

*20563400 dpgt sum 9.8067 0.0 1

'20563401 0.0 0.364 rho 602020000

cv 635 hot leg dp (bar] *20563500 hldp sum 1.0e-05 -0.2117 0

'20563501 0.0 1.0 p 301010000 -1.0 p 603010000 1.0 cntrlvar

636

** cv 636 hldp gravity term [pal

'20563600 dpgt sum 9.8067 0.0 1

'20563601 0.0 2.0957 rho 602010000

"- cv 637 dp42x [bar]

'20563700 dp42x sum 1.Oe-05 -1.1424 0

"20563701 0.0 1.0 p 301060000 -1.0 p 301010000 1.0

cntrivar 638

'20563701 0.0 1.0 cntrlvar 621 -1.0 p 301010000 1.0

cntrlvar 638

"* cv 638 dp42x gravity term (pa6

'20563800 dpgt sum 9.8067 0.0 1

'20563801 0.0 9.2065 rho 301020000

" cv 639 dp43x [bar]

'20563900 dp43x sum 1.0l-05 -0.9681 0

"-20563901 0.0 1.0 p 313010000 -1.0 p 301060000 1.0

cntrlvar 640

'20563901 0.0 1.0 p 313010000 -1.0 cntrlvar 621 1.0

cntrlvar 640

" cv 640 dp43x gravity term [pal

'20664000 dpg3t sum 9.8067 0.0 1

'20664001 0.0 -9.2065 rho 301080000

" cv 641 steam generator dp [bar]

'20564100 sgdp sum 1.0e-05 -2.1105 0

'20564101 0.0 1.0 p 313010000 -1.0 p 301010000 * dh-O.Om

" cv 642 : dp44 [bar]

'20564200 dp44 sum 1.0e-OS -0.1801 0

"-20564201 0.0 1.0 p 652010000 -1.0 p 313010000 1.0

cntrlvar 643

'20564201 0.0 1.0 entrlvar 622 -1.0 p 313010000 1.0

cntrlvar 643

c: ¢v 643 : dp44 gravity term [pa)

'20564300 dpgt sum 9.8067 0.0 1

'20564301 0.0 -0.364 rho 652010000

" cv 644 : dpl2vg (bar]

'20564400 dpl2vg sum 1.0e-05 -0.0576 0

"20564401 0.0 1.0 p 652020000 -1.0 p 652010000 1.0

cntrlvar 645

*20564401 0.0 1.0 cntrlvar 623 -1.0 cntrlvar 622 1.0

cntrlvar 645

** cv 645 dpl2vg gravity term [pal

'20564500 dpgt sum 9.8067 0.0 1

'20564501 0.0 -4.4007 rho 652020000

" cv 646 : dpl2vp [bar]

*20564600 dpl2vp sum 1.0e-05 -0.0634 0

**20564601 0.0 1.0 p 654010000 -1.0 p 652020000 1.0

cotrivar 647

'20564601 0.0 1.0 cntrivar 624 -1.0 cntrlvar 623 1.0

cntrlvar 647

cv 647 1 dpl2vp gravity term [pal

'20564700 dpgt sum 9.8067 0.0 1

'20564701 0.0 1.967 rho 653010000

" c 648 : intermediate leg dp [bar]

*20564600 ildp sum 1.Oe-05 -0.3011 0

"-20564801 0.0 1.0 p 654010000 -1.0 p 313010000 1.0

cntrivar 649

'20564801 0.0 1.0 cntrlvar 624 -1.0 p 313010000 1.0

cntrlvar 649

** ev 649 : ildp gravity term [pa)

'20564900 dpgt sum 9.8067 0.0 1

'20564901 0.0 -2.797 rho 652020000

Scv 650: dpl2p [bar]

'20565000 dpl2p sum 1.0a-05 0.0 1

**20565001 0.0 1.0 p 655010000 -1.0 p 654010000 1.0

cntrlvar 651

'20565001 0.0 1.0 p 655010000 -1.0 cntrlvar 624 1.0

cntrlvar 651

cv 651 : dpl2p gravity term [pal

'20565100 dpgt Sum 9.8067 0.0 1

*20565101 0.0 0.232 rho 654010000

cv 652 a dpl3h [bar]

'20565200 dpl3h sum 1.0e-OS -0.0303 0

'20565201 0.0 1.0 p 656010000 -1.0 p 655010000 * dh-O.Om

8110000 hi-ag angijun

'1 8110101 802010000 401000000 1.0936e-02 0.57 0.46 00100

8110101 802010000 401000000 1.0936e-02 0.616 0.46 130100

8110201 0 6.367908400 6.56940e+00 0.O0000e+00

prim, ststem: 8g vatopni prekat in u-cevi

4010000 ag-tube pipe

4010001 11

*1 4010101 0.04394 1 0.010342 11

4010101 0.04394 1 0.0103423 11

4010201 0 10

4010301 0.798 1 2.0 5 1.725 7 2.0 11

4010401 0 11

4010501 0 11

4010601 84.0 1 90.0 5 45.0 6 -45.0 7 -90.0 11

4010701 0.728 1 2.0 5 1.685 6 -1.665 7 -2.0 11

*! 4010801 0.ls-03 0.091 1 0.01*-03 0.01968 11

4010801 0.Ie-05 0.091 1 0.Ols-07 0.01968 11

*I 4010901 0.44 0.60 1 0.01 0.01 5 0.22 0.22 6 0.01

0.01 10

4010901 0.01 0.01 1 0.0 0.0 10

4011001 00 11

'1 4011101 00100 1 00000 10

4011101 100000 10

4011201 103 1.55556e,07 5.63746:+02 0.000000o00 0 0 1

4011202 103 1.SS187e+07 5.63172-002 0.OOOO0e.00 0 0 2

4011203 103 1.548268*07 5.62658e+02 0.O0000e+00 0 0 3

4011204 103 1.54466s*07 5.62198e÷02 0.00000.00 0 0 4

4011205 103 1.541050+07 5.617840.02 0.000000+00 0 0 S

4011206 103 1.53771.407 5.61454e002 0.00000+00 0 0 6

4011207 103 1.535687:07 5.61159:.02 0.000006+00 0 0 7

4011208 103 1.53523 +07 5.60864e÷02 0.O000ei+00 0 0 8

4011209 103 1.53457e,07 5.60605e.02 0.00000+00 0 0 9

4011210 103 1.533910e07 5.60379e+02 0.O0000e+00 0 0 10

4011211 103 1.$3325e.07 5.60180e'02 0.00000 00 0 0 11

4011300 0

4011301 6.73340e,00 6.73340e+00 0.00000+00 1

4011302 6.72420e÷00 6.72420e+00 0.O0000e+00 2

4011303 6.71600eO00 6.716000+00 0.O0000e.00 3

4011304 6.70880eO00 6.706800+00 0.00000e00 4

4011305 6.70230e.00 6.70230e+00 0.O0000O+00 S

4011306 6.69730e+00 6.69730e.00 0.00000e+00 6

4011307 6.69270e000 6.692700e00 0.00000.00 7

4011308 6.68790e.00 6.68790e+00 0.00000e÷00 6

4011309 6.68370e.00 6.68370e+00 0.00000*00 9

4011310 5.86580e'00 5.86580e+00 0.000000+00 10

4011401 .01968 0.0 1.0 1.0 10

* prim. sistem: sg izstopni prekat

4130000 o-ch branch

4130001 1 0

'2 4130101 0.0 0.798 35.061e-03 0.0 -85.0 -0.728 0.le-03

0.091 00

4130101 0.0 0.798 35.061e-03 0.0 -85.0 -0.728 0.le-04

0.091 00

4130200 103 1.53427e.07 5.60188e002

*1 4131101 401010000 413000000 0.010342 0.60 0.44 130100

4131101 401010000 413000000 0.0103423 0.3 0.2 130000

4131201 6.67690o+00 6.96280e+00 0.O0000e+00

* prim. sisatem: 39 izatop

8610000 sg-cl angljun

'1 8610101 413010000 652000000 1.0936e-02 0.46 0.57 00100

8610101 413010000 852000000 1.09360-02 0.01 0.02 130100

8610201 0 6.31440e÷00 6.53290e÷00 0.00000s+00

Bass uparjalnik 2

*•*** ....... .............

* prim. sistem: ag vatop

16
* oak. slstem: dvlznl kanal

4030000 riser pipe

4030001 6

4030101 0.0 6

4030201 0.01291 1 0.0214 4 0.048695 5

4030301 2.0 4 2.9605 5 0.8295 6

* povecanje masn sekundarnega hiadila

*4, 4030401 0.11513 4 0.17171 5 0.04041 6

4030402 0.12513 4 0.18172 5 0.04042 6

4030501 0 6

4030601 90.0 6

4030701 2.0 4 2.9605 5 0.8295 6

4030801 0.le-03 0.03503 5 0.le-03 0.249 6

4030901 5.46 S.46 1 3.32 3.32 4 0.1 0.1 5

4031001 00 6

4031101 100100 4 100000 5

4031201 100 6.88635e*06 1.24544s,06 2.58278es06

0.O0000e+00 I

4031202 100 6.87346e.06 1.25147e+06 2.58289e*06

0.O0000eO00 2

4031203 100 6.86224e.06 1.25111e+06 2.56298e+06

0.00000e.00 3

4031204 100 6.852410+06 1.250562a06 2.58305e+06

0.O0000oe00 4

4031205 100 6.64126e+06 1.25006e+06 2.58314ea06

0.O0000e+00 5

4031206 100 6.83290e+06 1.249380+06 2.58318e+06

0.O0000oa00 6

4031300 0

4031301 4.72633e-02 2.73670e-01 0.O0000e+00 1

4031302 5.13252e-02 3.89160e-01 0.O0000e00 2

4031303 5.53480e-02 4.406208-01 0.00000e.00 3

4031304 6.06002e-02 4.894306-01 0.o0000o.00 4

4031305 7.43054e-02 7.346508-01 0.O0000e+OO S

4031401 0.027 0.0 1.0 1.0 5 * 44

6.522340-02

1.893800-01

2.99390.-Ol

3.94690e-01

4.19940e-01

4.017 2

00-01

4100801 0.le-03 0.8000 1 0.le-03 0.41905 2

4100901 0.0 0.0 1

4101001 00 2

4101101 100000 1

4101201 102 6.81865Se06 1.00000+00 0.00000e÷00 0 0 1

4101202 102 6.818400+06 1.00000+00 0.O0000e÷00 0 0 2

4101300 0

4101301 -9.21311e-03 4.437318-02 0.00000e,00 1

* sek. siltem: spoj uparjalnika in parovoda

4110000 ag-sl angljun

4110101 410010000 420000000 0.0011401 0.222 1.0 130100

4110201 0 6.85760e.00 6.87050a*00 0.O0000e+0

* ask. siltem: povratni kanal (zgornji obrocasti del)

4190000 udownann branch

4190001 1 0

4190101 0.0 1.9430 0.3078 0 90.0 1.9430 0.1e-03 0.1930

00

4190200 102 6.824949.06 8.101OO-03

'4191101 410000000 419010000 0.44915 0.0 0.0 00100

4191101 410000000 419010000 0.0 0.5 0.5 130100

4191110 0.1930 0.0 1.0 1.0

4191201 3.045000-01 3.67423e-04 0.0000e,00

* ask. aistem: povratni kanal (arednji obrocasti del)

4080000 odownann branch

4080001 2 0

4080101 0.0 0.8275 0.081723 0 -90.0 -0.8275 0.le-03

0.176 00

4080200 102 6.834160+06 0.O0000e*00

4081101 419000000 408000000 0.0 0.09 0.15 130000

*4082101 408010000 409000000 0.030415 0.0 0.0 00100

4082101 408010000 409000000 0.0 0.43 0.60 130100

4081110 0.1930 0.0 1.0 1.0

4082110 0.1760 0.0 1.0 1.0

4081201 1.76401s-04 -3.00110e-01 0.O0000e+O0

4082201 1.16890e-01 1.38490e-01 0.00000*,00

* aek. aistem: povratni kanal (spodnji teoni del)

4090000 pipedown pipe

4090001 5

4090101 0.0 5

4090201 0.0 1 0.005836 4

4090301 2.9625 1 2.0 S

4090401 0.06909 1 0.01167 4 0.01456 S

4090501 0 5

4090601 -90.0 5

4090701 -2.9625 1 -2.0 S

4090801 0.le-03 0.05983 1 0.le-03 0.0431 S

4090901 0.47 0.S7 1 0.05 O.OS 4

4091001 00 5

4092202 200100 1 200000 4

4091201 103 6.84846e.06 5.42776e+02 0.O0000eO00 0 0 1

4091202 103 6.867000.06 5.427889e02 0.O0000e.00 0 0 2

4091203 103 6.88200e+06 5.427990.02 0.O0000e+00 0 0 3

4 091204 103 6.89700a.06 5.42811s*02 0.00000e.00 0 0 4

4091205 103 6.91205÷+06 5.428490802 0.000008400 0 0 S

4091300 0

4091301 4.67180e-01 4.671808-01 0.00000e,00 1

4091302 4.67090e-01 4.670908-01 0.O0000eO00 2

4091303 4.6 7

000e-01 4.67000e-01 0.O0000e.00 3

4091304 4.67080e-al 4.670808-01 0.oooooeo00 4

4091410 0.0431 0.0 1.0 1.0 4

* a8k. sistem: spoj povratnega in dvilnega kanala

* ni -abrupt area change- models - regulacija recirkulacije

4350000 dra valve

4350101 409010000 403000000 0.025761 0.0 0.0 100000

4350201 0 1.05820e-01 1.44390e-01 0.00000s.00

4350300 srvvlv

4350301 424

4350401 0.01 0.01 0.01 * zaprto

4350402 1.0 1000.0 1000.0 * odprto

* ccci ag2 recirkulacija: 4x : 4 * 0.525 kg/s - 2.100 kg/a

20542400 reg435 SUm 1.0 0.02847 0 3 0.01 1.0

20542401 0.0002100 -0.0001 mflowj 435000000 1.0 cntrlvar

424

'20542400 reg43S constant 1.0

*..*......** .. * *****ftfi.......

* hhss toplotna telesa ag 2

* u cevi

14013000 10 4 2 1 0.00984

14013100 0 1

14013101 3 0.01111

14013201 3 3

14013301 0.0 3

14013401 570.330 I

* prim. --.

14013501 401020000

14013502 401030000

14013503 401040000

14013504 401050000

14013505 401060000

14013506 401070000

14013507 401080000

24013508 401090000

14013509 401100000

14013510 401110000

4 -- > ask.

14013601 403010000

14013602 403020000

14013603 403030000

14013604 403040000

14013605 403050000

14013606 403050000

14013607 403040000

14013608 403030000

14013609 403020000

14013610 403010000

* sek. sistem: separator pare

4070000 separ aeparatr

4070001 3 0

4070101 0.0 1.9430 0.09467 0 90.0 1.9430 O.le-04 0.249

00

4070200 100 6.024890*06 1.24924o.06 2.58329e+06 1.46050e-01

4071101 407010000 410000000 4.86950-02 0.82 0.14 01000

0.0

4072101 407000000 408000000 44.91508-02 0.26 0.23 01000

0.0

4073101 403010000 407000000 4.86958-02 0.0 0.0 01000

4071201 -9.28200e-02 3.063308-01 0.oo000oo00

4072201 4.68582e-03 -1.701668-02 0.00000e+00

4073201 7.22507e-02 7.614800-Ol 0.O0000e+00

• ask. siltm: zgornji parni prostor

4100000 atmdame pipe

4100001 2

4100101 0.0 2

4100201 0.0 1

4100301 1.0800 1 0.4000 2

4100401 0.54287 1 0.134040 2

4100501 0.0 2

4100601 90.0 2

4100701 1.0000 1 0.4000 2

566.810 2

0 1 1

0 1 1

0 1 1

0 1 1

0 1 1

0 1 1

0 1 2

0 1 1

0 1 1

0 1 1

0 1 1

0 1 1

0 1 1

0 1 1

0 1 1

0 1 1

0 1 1

011

0 1 1

563.420 3 560.15 4

68.0 1

68.0 2

68.0 3

68.0 4

58.65 5

58.65 6

68.0 7

6a.0 0

68.0 9

68.0 10

68.0 1

68.0 2

68.0 3

68.0 4

58.65 5

58.65 6

68.0 7

68.0 8

68.0 9

68.0 10

14013701 0 0 0 0 10

14013801 0 10. 10. 0. 0. 0. 0. 1. 10

14013901 0 10. 10. 0. 0. 0. 0. 1. 10

* dividing plate in channel head

14011000 1 4 1 1 0.0

14011100 0 1

14011101 3 0.012

14011201 1 3

14011301 0.0 3

14011401 597.0 1 588.0 2 570.0 3 561.0 4

14011501 401010000 0 1 0 0.26643 1

17
14011601 413010000 0 1 0 0.26643 1

14011701 0 0 0 0 1

14011801 0 10. 10. 0. 0. 0. 0. 1. 1

14011901 0 10. 10. 0. 0. 0. 0. 1. 1

* caInnel head : zunanja stena --. plosca

14012000 2 4 1 1 0.0

14012100 0 1

14012101 3 0.0590

14012201 1 3

14012301 0.0 3

14012401 597.0 1 588.0 2 570.0 3 561.0 4

14012501 401010000 0 1 0 0.40167 1

14012502 413010000 0 1 0 0.40167 2

14012601 0 0 0 0 0.40167 1

14012602 0 0 0 0 0.40167 2

14012701 0 0 0 0 2

14012501 0 10. 10. 0. 0. 0. 0. 1. 2

14012901 0 10. 10. 0. 0. 0. 0. 1. 2

* tubesheet

14014000 2 4 1 1 0.0

14014100 0 1

14014101 3 0.1645

14014201 1 3

14014301 0.0 3

14014401 597.0 1 566.0 2 570.0 3 561.0 4

14014501 401010000 0 1 0 0.1139 1

14014502 413010000 0 1 0 0.1139 2

14014601 409050000 0 1 0 0.1139 1

14014602 403010000 0 1 0 0.1139 2

14014701 0 0 0 0 2

14014801 0 10. 10. 0. 0. 0. 0. 1. 2

14014901 0 10. 10. 0. 0. 0. 0. 1. 2

: riser (brez upper cylindrical shell) --. plosca: hhll

14031000 5 4 1 1 0.0

14031100 0 1

14031101 3 0.0159

14031201 1 3

14031301 1.0 3

14031401 597.0 1 566.0 2 570.0 3 561.0 4

14031501 403010000 0 1 0 2.895 1

14031502 403020000 0 1 0 2.895 2

14031503 403030000 0 1 0 2.895 3

14031504 403040000 0 1 0 2.895 4

14031505 403050000 0 1 0 4.286 5

14031601 0 0 0 0 2.995 1

14031602 0 0 0 0 2.695 2

14031603 0 0 0 0 2.695 3

14031604 0 0 0 0 2.895 4

14031605 0 0 0 0 4.286 5

14031701 10228 0.2 0 0 5

14031801 0 10. 10. 0. 0. 0. 0. 1. S

14031901 0 10. 10. 0. 0. 0. 0. 1. 5

• upper-inner cylindrical shell --. plosca

14032000 2 4 1 1 0.0

14032100 0 1

14032101 3 0.006

14032201 1 3

14032301 0.0 3

14032401 597.0 1 566.0 2 570.0 3 551.0 4

14032501 406010000 0 1 0 0.6633 1

14032502 419010000 0 1 0 1.5537 2

14032601 403060000 0 1 0 0.6633 1

14032602

14032701

14032601

14032901

407010000 0 1 0 1.$537 2

0 0 0 0 2

0 10. 10. M. 0. 0. 0. 1. 2

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

• upper sleve and upper head ---. plosce 14101.. .14104

14101000 1 4 1 1 0.0

14101100 0 1

14101101 3 0.0210

14101201 1 3

14101301 0.0 3

14101401 597.0 1 566.0 2 970.0 3 561.0 4

14101501 0 0 0 0 1.005 1

14101601 410020000 0 1 0 1.005 1

14101701 0 0 0 0 1

14101501 0 10. 10. 0. 0. 0. 0. 1. 1

14101901 0 10. 10. 0. 0. 0. 0. 1. 1

14092000

14092100

14092101

14092201

14092301

14092401

14092501

14092502

14092503

14092504

14092601

14092602

14092603

14092604

14092701

14092601

14092901

4 4 1 1 0.0

0 1

3 0.00276

1 3

0.0 3

597.0 1 586.0 2 570.0, 3

0 0 0 0 1.2026 1

0 0 0 0 1.2026 2

0 0 0 0 1.2028 3

0 0 0 0 1.2026 4

409020000 0 1 0 1.2028 1

409030000 0 1 0 1.2028 2

409040000 0 1 0 1.2028 3

409050000 0 1 0 1.2028 4

0 0 0 0 4

0 10, 10. 0, 0. 0. 0. 1. 4

0 10. 10. 0. 0. 0. 0. 1. 4

561,0 4

14102000

14102100

14102101

14102201

14102301

14102401

14102501

14102601

14102701

14102601

14102901

14103000

14103100

14103101

14103201

14103301

14103401

14103501

24103601

14103701

14103801

14103901

14104000

14104100

14104101

14104201

14104301

14104401

14104501

14104601

14104701

14104801

14104901

1 4 1 1 0.0

0 1

3 0.0258

1 3

0.0 3

597.0 1 5$6.0 2 570.0 3

0 0 0 0 3.3670 1

410010000 0 1 0 3.3870 1

0 0 0 0 1

0 10. 10. 0. 0. 0. 0. 1. 1

0 10. 10. 0. 0. 0. 0. 1. 1

1 4 1 1 0.0

0 1

3 0.0947

1 3

0.0 3

597.0 1 588.0 2 570.0 3

0 0 0 0 0.4463 1

419010000 0 1 0 0.4463 1

0 0 0 0 1

0 10. 10. 0. 0. 0. 0. 1. 1

0 10. 10. 0, 0. 0. 0. 1. 1

1 4 1 1 0.0

0 1

3 0.0245

1 3

0.0 3

597.0 1 586.0 2 570.0 3

0 0 0 0 3.2448 1

408010000 0 1 0 3.2448 1

0 0 0 0 1

0 10. 10. 0. 0. 0, 0. 1. 1

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

561.0 4

561.0 4

561.0 4

* ssggccvv sg 2 kontrolne spremmnli ivke

...... *........ ..... .ft . . *

• cv 4031 *921 nivo v povratnem kanalu [m)

20540300 levdc sum 1.0 13.45 1

20540301 0.0 2.0 voidf 409050000 2.0 voidf 409040000

20540302 2.0 void! 409030000 2.0 voidf 409020000

20540303 2.9625 voidf 409010000 0.6275 voidf 406010000

20540304 1.9430 voidf 419010000

* cv 405: sg2: mass selumdarnega hladila [kg]

20540500 isgi0as sum 1.0 790.0 1 *.g÷ 20540501 0.0 0.11513 rho 403010000 0.11513 rho

403020000

*÷÷ 20540502 0.11513 rho 403030000 0.11513 rho

403040000

*.. 20540503 0.17171 rho 403050000 0.04041 rho

403060000

20540501 0.0 0.12513 rho 403010000 0.12513 rho 403020000

20540502 0.12513 rho 403030000 0.12513 rho 403040000

20540503 0.18171 rho 403050000 0.04041 rho 403060000

20540504 0.09466 rho 407010000 0.54287 rho 410010000

20540505 0.13404 rho 410020000 0,30760 rho 419010000

20540506 0.06172 rho 406010000 0.06909 rho 409010000

20540507 0.01167 rho 409020000 0.01167 rho 409030000

20540508 0.01167 rho 409040000 0.01456 rho 409050000

5***......... * ..... ........ 

* awt main feedwater 2

konstantni m! tok

4340000 MfV tMmPjun

4340101 431000000 432000000 0.0266

4340200 1 SOS * mi

4340201 -1.0 0.52517 0. 0.

4340202 0.0 0.52517 0. 0.

* downcmr --. ploace 4091-01, 4092-01-02-03-04

14091000 1 4 1 1 0.0

14091100 0 1

14091101 3 0.00394

14091201 1 3

14091301 0.0 3

14091401 597.0 1 56.0 2 570.0 3 561.0 4

14091501 0 0 0 0 4.0116 1

14091601 409010000 0 2 0 4.0116 1

14091701 0 0 0 0 1

14091601 0 10. 10. 0. 0. 0. 0. 1. 1

14091901 0 10. 10. 0. 0. 0. 0. 1. 1

18
4340203 6.0 0.0 0. 0.

* volumski mfw tok

-20540200 vmfr div 1.0 0.0 1

*20540201 rhof 432010000 flowi 432010000

* feedwater line

4320000 fwline branch

4320001 1 0

4320101 5.5579-04 10.0 0 0 60.0 7.0 0.019-03 0.0266 00

4320200 103 6.862756+06 4.90974e+02

•4321101 432010000 408000000 0.0006786 0. 0. 00100

4321101 432010000 408000000 0.0 1.0 0. 130100

4321201 1.11560e900 1.115609+00 0.00000e+00

* vir napajalne vode

4310000 fwsource t]dpvol

4310101 1.0 0.0 10.0 0 0 0 0.01*-03 0.0 00

4310200 103

4310201 0 70.0.5 491.0

*ccci "regulacija- zg2 nivoja * ohkonstantni mfw 434 reguliramo nivo v povratnem kanalu

4290000 v429 tmdpvol

4290101 1.0 0.0 10.0 0.0 0.0 0.0 0.20-03 0.0 0

4290200 103

4290201 0 70.0.5 491.0

4300000 J430 tedpjun

4300101 429000000 419010000 0.0

4300200 1 0 cntrlvar 403 - ag level

4300201 -1.0 0.0 0.0 0.0

4300202 13.35 1.5 0.0 0.0

4300203 13.45 0.0 0.0 0.0

4300204 13.55 -1.5 0.0 0.0

*4300000 j430 tmdpjun

'4300101 429000000 419010000 0.0 *4300200 1 0 cntrlvar 405 * 8gmMass

*4300201 -1.0 0.0 0.0 0.0

'4300202 790.0 1.5 0.0 0.0

*4300203 800.0 0.0 0.0 0.0

-4300204 810.0 -0.50 0.0 0.0

* sail parovod 2

steam line from porv.sv.miv

4200000 8taline anglvol

4200101 0.0 31.65 68.5e-03 0 -45.0 -18.670 0.01-3 0.052S

00

4200200 102 6.812559÷06 1.00000e.00

* hh8s

* 14201000 1 4 2 1 0.0525

14201000 1 4 2 0 0.0525 - ffll

14201100 0 1

14201101 3 0.0603

14201201 1 3

14201301 0.0 3

14201401 570.330 1 S66.810 2 563.420 3 560.15 4

14201501 420010000 0 1 1 31.65 3

14201601 0 0 0 1 31.65 1

14201701 0 0 0 0 1

14201801 0 10. 10. 0. 0. 0. 0. 1. 1

14201901 0 10. 10. 0. 0. 0. 0. 1. 1

*ccci regulacija tcold 2 preko tlaka sekundarne strani

* delta tcold : bethey referenca : 559.85 k

20540000 dtcold sum 1.0 0.0 0

20540001 560.35 -1.0 tempf 855010000

- 20540001 559.35 -1.0 teupf 855010000 * 10

20544400 p444 sum 1.0 68.120.05 0

20544401 0.0 1.0 p 444010000 300. cntrlvar 400

4150000 venturi sngljun

4150101 420010000 444000000 0.0 0.0 0.0 130000

4150201 0 6.877400.00 6.877400+00 0.000000.00

4440000 turbine tmdpvol

4440101 10.0 0.0 1000.0 0 0.0 0 0.2a-03 0 0

4440200 2 0 cntrlvar 444

4440201 -1.0 68.12s.05 1.0

4440202 1.0e005 1.00+05 1.0

4440203 100.00.05 100.00.05 1.0

* rrces cevovodi primarnega kroge 2

* * prim. sistem: hot leg do surge line

• 8030000 hleg snglvol

* 8030101 0.010936 1.4441 0.0 0.0 0.0 0.0 0.1e-03 0.1180

00

*8030200 103 1.559570,07 S.637908,02

8030000 hlog pipe

8030001 5

8030101 0.010936 5

8030201 0.010936 4

8030301 0.28002 5

8030401 0.0 5

8030501 0.0 5

8030601 0.0 5

8030701 0.0 5

8030801 O.le-03 0.1180 5

8030901 0.0 0.0 4

8031001 00 5

8031101 100000 4 *fvcahs:v.0

* should be input as not used

8031201 103 1.55942e,07 5.63762e,02 0.00000o+00 0 0 1

19

8031202 103 1.55935e+07 5.637620+02 0.00000+000 0

8031203 103 1.55928e+07 5.637628+02 0.O0000e.00 0

6031204 103 1.559210+07 5.637620+02 0.00000s.00 0

8031205 103 1.559140,07 5.63762e.02 0.00000e.00 0

8031300 0

8031301 6.367600,00 6.36760 ,00 0.000000:00 1

8031302 6.367600.00 6.36760e-00 0.00000.00 2

8031303 6.367600+00 6.367600+00 0.00000+000 3

8031304 6.36760e.00 8.36760e*00 0.O0000e.00 4

* prim. sists.: hot leg spoj pri el

8130000 h1813 angljun

*1 8130101 803010000 802000000 0.0 0.0 0.0 00000

8130101 803010000 802000000 0.0 0.265 0.265 130000

8130201 0 6.367700+00 6.367700+00 0.000000+00

0 2 0 3

0 4

0 5

• ' prim. sistem, hot leg od a1 do 8g

* 8020000 hileg pipe

• 6020001 2

* 8020101 0.010936 2

8020201 0.010936 1

* 8020301 1.1891 1 1.0558 2

* 8020401 0.0 2

8020501 0.0 2

* 8020601 9.0 1 70.0 2

• 8020701 0.1800 1 1.7317 2

* 8020801 0.1e-03 0.1180 2

*! 8020901 0.31 0.31 1

* 8020901 0.24 0.24 1

* 8021001 00 2

0021101 100000 1

* 8021201 103 1.55880*+07 S.637900+02 0.00000e0,0 0 0 1

* 8021202 103 1.557380+07 5.63790e.02 0.000000.00 0 0 2

* 9021300 0

* 8021301 6.29920e,00 6.29920e+00 0.O0000e÷00 I

8020000 hleg pipe

8020001 10

8020101 0.010936 10

8020201 0.010936 9

8020301 0.23782 5 0.37116 10

8020401 0.0 10

8020601 0.0 10

8020601 9.0 5 70.0 10

8020701 0.036 S 0.34634 10 * ++

8020801 0.10-03 0.1180 10

8020901 0.0267 0.0267 9

8021001 00 10

8021101 100000 S 100000

8021201 103 1.558660,07

8021202 103 1.55853.007

8021203 103 1.55841e,07

8021204 103 1.55829:007

8021205 103 1.55816+.07

8021206 103 1.55791s+07

8021207 103 1.557520.07

8021209 103 1.$57140+07

8021209 103 1.556760+07

0021210 103 1.558370.07

8021300 0

9 * v.0

S.63760e÷02

5.63760:+02

5.63760 +02

9.63759e.02

5.837590,02

5.637580,02

5.637570.02

5.637569+02

5.637550.02

5.637540+02

0.O0000eO00

0.O00000.00

0. O0000e00

0.00000e+00

0.000000.00

0.O0000e+00

0.000000.00

0.00000e,00

0.000000.00

0.000000+00

0

0

0

0

0

0

0

0

0

0

0 1

0 2

0 3

0 4

0 S

0 6

0 7

0 8

0 9

0 10

8021301

8021302

8021303

8021304

0021305

8021306

6.36770a.00 6.367700.00 0.000000+00 1

6.387709+00 6.367700+00 0.00000*00 2

6.387700,00 6.367700+00 0.O0000e+00 3

6.367700+00 6.367700.00 0.00000+000 4

6.36770e+00 6.367700,00 0.00000e.00 5

6.36780e÷00 6.64560e+00 0.000000+00 6
8021307 6.36780e.00 6.64S60e+00 0.00000+0O0 7

8021308 6.36780e*00 6.64570e+00 O.00000*e00 8

8021309 6.36790e+00 6.64580e.00 O.O0000oe0 9

............................................

* eg

* prim. sixtem: intermediate lag down

# 8520000 ilega pipe

* 8520001 2

8520101 0.010936 2

8520201 0.010936 1

* 8520301 2.5122 1 2.0697 2

* 8520401 0.0 2

* 8520501 0.0 2

6520601 -76.0 1 -72.0 2

8520701 -2.4337 1 -1.9670 2

•* 8520801 0.18-03 0.1180 2

* 8520801 0.1e-04 0.1180 2

*2 8520901 0.11 0.11 1

* 8520901 0.1 0.1 1

* 6521001 00 2

8521101 100000 1

8521201 103 1.53406e+07 5.60210e.02 0.OOOOOe+00 0 0 1

* 8521202 103 1.53516e.07 5.60220ei02 0.OOOOOe00 0 0 2

* 8521300 0

* 8521301 6.246500+00 6.24650a+00 0.O00000*O0 1

8520000 ileg_a pipe

8520001 10

8520101 0.010936 10

8520201 0.010936 9

8520301 0.50244 5 0.41394 10

8520401 0.0 10

8520501 0.0 10

8520601 -76.0 5 -72.0 10

8520701 -0.48674 5 -0.39340 10 *++

*I 8520801 0.le-03 0.1180 10

6630000 jun863 sngljun

#1 8630101 852010000 853000000 0.0 0.20 0.20 00000

8630101 852010000 853000000 0.0 0.0 0.0 130000

8630201 0 6.31430e+00 6.59380e.00 0.000000+00

* prim. sistem: intermediate leg

8530000 ileg.b snglvol

* 8530101 0.010936 1.1027 0.0 0.0 9.0 0.180 0.le-03

0.1180 00 I8530200 103 1.53553s+07 S.602200+02

8530000 ileg.. pipe

8530001 5

8530101 0.010936 5

8530201 0.010936 4

8530301 0.22054 5

8530401 0.0 5

$530501 0.0 5

8530601 9.0 S

8530701 0.036 5

8530801 0.le-03 0.1180 5

8530901 0.0 0.0 4

8531001 00 S

8531101 100000 4 t*vcahs:v-O

* should be input as

8531201 103 l.53487e.07 5.60192e802

8531202 103 1.53479a.07 5.601910+02

8531203 103 1.53471e+07 S.60191et02

8531204 103 1.53463e*07 5.60191e+02

8531205 103 1.53455e.07 S.60191e.02

8531300 0

not used

0.0000000

0.00000+e00

0.O0000.00

O.OOOOOe.00

0.00000+00

8541201 103 1.53434e.07 5.601910e02 0.00000000 0 0 1

8541202 103 1.53399e÷07 5.60190e002 0.OO000e0+0 0 0 2

8541203 103 1.53364e.07 5.601890.02 O.OOOOOe÷O0 0 0 3

8541204 103 1.53329e+07 S.60188e+02 O.OOOOOe.o0 0 0 4

8541205 103 1.532940÷07 5.60186e÷02 0.00000.00 0 0 5

8541300 0

8541301 6.314400600 6.59380e.00 0.00000.00 1

8541302 6.314400+00 6.593908.00 O.OOOOOe•00 2

8541303 6.31450e+00 6.59400e+00 O.OOOOO00O 3

8541304 6.31450s+00 6.S94000.00 O.OOOOOe.00 4

* rcp-2

RCP+ *

*.... *.. *.. ....................... 

8000000 in2 branch

8000001 1 0

8000101 0.010936 0.232 0.0 0.0 90.0 0.232 0.Ole-04 0.118

00

8000200 100 1.561510+07 1.24642e+06 2.44514+06 0.ooo00ea.00

8001101 854010000 800000000 0.0 0.0 0.0 130000

8001201 6.31570e-00 6.59530e+00 0.00000e+00

• pump loop 2

7020000 pump2 pump

7020101 0.0 0.097 14.0628e-03 0.0 60.0 0.084 00

7020108 800010000 0. 0.47 0.49 100000 •+÷ upor ustaavijene

crpalke ?

7020109 801000000 0. 0.49 0.47 100000

7020200 0 1.56151e÷07 1.248420+06 2.445146+06 O.OOOOOe+O0

7020201 0 6.315706+00 6.59530e+00 O.OOOOOe00

7020202 0 1.06000e÷00 1.06000e÷00 0.000006+00

* pump index and option Card

7020301 -2 0 -2 -1 0 505 0 * trip 505: 8i - pump 2

stop

* pump description card

*! 7020302 311.0 1.0 0.063056 78.0 0.0

7020302 311.0 1.0 0.067939 78.0 0.0

* 7020302 311.0 1.0 0.068797 78.0 0.0 * 2#

7020303 5.0 751.0 0.0 0.0 74.39 71.39 0.0 *++ rated

density

m l. two phase pump head multiplier tables

7023000 0 0.0 0.0, 0.2 0.0, 0.4 1.0, 0.9 1.0, 1.0

0.0

* mt two phase pump torque multiplier tables

7023100 0 0.0 0.0, 0.2 0.0, 0.4 1.0, 0.9 1.0, 1.0

0.0

0

0

0

0

0

0 1

0 2

0 3

0 4

0 5

8531301

8531302

8531303

8531304

6.31430e+00 6.31430e+00 O.OOOOOeO00 1

6.314400.00 6.31440e+00 0.O0000e+00 2

6.31440e800 6.314400+00 0.000006,00 3

6.31440e+00 6.31440e800 0.O0000e00 4

8520801 0.le-04 0.1180 10

*! 8520901 0.11 0.11 9

8520901 0.011 0.011 9

8521001 00 10

8521101 100000 9

8521201 103 1.53271e+07 5.

8521202 103 1.53297e.07 5

8521203 103 1.533230+07 S

8521204 103 1.533490+07 5

8521205 103 1.53375e.07 5

8521206 103 1.533980.07 5

8521207 103 1.53418$e07 5

8521208 103 1.534398÷07 5

8521209 103 1.53459e+07 5.

8521210 103 1.53480a+07 5

8521300 0

8521301 6.31450SO00

8521302 6.31450e800

8521303 6.31450e.00

0521304 6.31440a.00

8521305 6.314400e00

8521306 6.31440e÷00

8521307 6.31440*+00

8521308 6.314400+00

8521309 6.31440e+00

6.594:

6 .5942

6.5942

6.5942

6.593!

6.5932

6.5932

6.$931

6.5932

.60182eo02

.601836.02

.60185e÷02

.60186e.02

.60187a+02

.60188e*02

.60189e+02

.601899÷02

.60190e802

.60191e.02

10O00 0.4

00e.00 0.2

OOe.00 0.2

00000 0.2

90e+00 0.2

900e00 0.2

90*e00 0.2

806+00 0.2

80+e00 0.2

0.O0000e+00

0.O00000e00

0.00000e+00

0.000008+00

0.00000+e00

0.O0000+e00

0.O0000e.00

O.OOOOe+O0

0.O00000e00

O.OOOOOe+O0

0

0

0

0

0

0

0

0

0

0

0 1

0 2

0 3

0 4

05

0 6

0 7

0 8

0 9

0 10

8640000 jun864 sngljun

*! 8640101 853010000 854000000 0.0 0.20 0.20 00000

8640101 853010000 854000000 0.0 0.0 0.0 130000

8640201 0 6.31440e÷00 6.31440e+00 O.O00000e00

* - prim. sistem: intermediate leg up

8540000 ileg_c anglvol

* '8540101 0.010936 1.7870 0.0 0.0 90.0 1.7870 0.16-03

0.1180 00

* 8540101 0.010936 1.7671 0.0 0.0 90.0 1.7871 0.le-03

0.1180 00

* *÷+ podaljoek 0.1 -m zaradi sklenitva rca elevacti v rx

(napeka haze pod.)

* 8540200 103 1.53446e+07 5.60220e#02

8540000 ileg-C pipe

8540001 5

8540101 0.010936 S

8540201 0.010936 4

6540301 0.35742 5

8540401 0.0 5

8540501 0.0 5

8540601 90.0 5

8540701 0.35742 5

8540801 0.le-03 0.1180 S

6540901 0.0 0.0 4

8541001 00 S

8541101 100000 4 'fvcahs:V.O

* should be input as not used

20

O0000e000

000000*00

O0000e÷00

00000*.00

O0000e.00

000000-00

00000O+00

O0000e+00

O000000+0

1

2

3

4

S

6

7

8

9'

* pump velocity table (red/a)

7026100 505

7026101 300.0 311.0

7026102 305.0 201.0 310.0

7026103 320.0 113.1 330.0

7026104 340.0 75.4 350.0

7026105 370.0 47.1 400.0

7026106 500.0 22.0 700.0

7026107 916.0 10.5 917.0

8010000 out2 branch

8010001 1 0

141.1

68.0

62.9

37.7

15.7

0.0
8010101 0.0 0.084 5.460e-03 0.0 -90.0 -0.084 O.01e-04

0.0 00

6010200 100 2.56151e+07 1.246420.06 2.44514e,06 0.00000e+00

8011101 801010000 655000000 0.0 0.0 0.0 130000

8011201 6.31570*+00 6.59530e.00 0.00000o+00

* hhll-hh6s rcp2

17020000 1 3 1 1 0.0

17020100 0 1

17020101 2 0.1

17020201 1 2

17020301 1.0 2

17020401 360.0 3

17020501 702010000 0 1 1 1.0 1

17020601 0 0 0 1 1.0 1

17020701 10701 1.0 0.0 0.0 1

17020801 0. 10. 10. 0. 0. 0. 0. 1. 1

.... .... **.* ......... ...... *...... ... fl.........

• * prim. mistem, cold log a

* 5S50000 cIgsa branch

• 6550001 1 0

• *1 8550101 0.010936 1.6656 0.0 0.0 0.0 0.0 0.10-03

0.1180 00

• 8550101 0.010936 1.0656 0.0 0.0 0.0 0.0 0.10-04 0.1180

00

* 8550200 103 1.589206+07 5.60350e,02

* 61 551101 855010000 656000000 0.0 0.07 0.07 00000

* 8551101 655010000 356000000 0.0 0.002 0.002 130000

* 8551201 6.241300800 6.241300.00 0.00000e+00

-* prim. slistes: cold log b

6560000 8 cleg b angIvol

*B I6560101 0.010936 1.8656 0.0 0.0 0.0 0.0 0.10-03

0.1180 00

6560101 $ 0.010936 1.8656 0.0 0.0 0.0 0.0 0.10-04 0.1100

00

• 6560200 103 1.586756,07 5.603500.02

18021301

18021401

18021501

16021502

18021503

18021601

10021602

18021603

16021701

18021601

16021901

1.0 3

597.0 1 568.0 2 570.0 3 561.0 4

603010000 10000 1 0 0.1070 5

602010000 10000 1 0 0.0681 10

802060000 10000 1 0 0.1376 15

0 0 0 0 0.1070 5

0 0 0 0 0.0881 10

0 0 0 0 0.1376 15

10229 0.0667 0 0 1S

0 10. 10. 0. 0. 0. 0. 1. 15

0 10. 10. 0. 0. 0. 0. 1. 15

6560000 cleghj pipe

6560001 5

6560101 0.010936 5

6560201 0.010936 4

8560301 0.37312 5

8560401 0.0 S

8560501 0.0 5

8560601 0.0 5

8560701 0.0 5

6560601 0.10-03 0.1180 5

6560901 0.0 0.0 4

8561001 00 5

6561101 100000 4 •fvcahstvO

• should be input a not used

8561201 103 1.567080+07 5.603490+02 0.00000.00

6561202 103 1.58700e+07 5.60349*.02 0.00000s400

6561203 103 1.586910+07 5.60349e+02 0.O0000e+00

6561204 103 1.568020.07 5.603490e02 0.000000.00

6561205 103 1.56673e+07 5.60349e.02 0.000009.00

8561300 0

0561301 6.30990e*00 6.30990e+00 0.00000e+00 1

6561302 6.309900,00 6.30990*+00 0.O0000Oi0 2

8541303 6.30990e+00 6.309900400 0.00000.000 3

6561304 6.309900+00 6.309900+00 0.000008.00 4

0

0

0

0

0

0

0

0

0

0

1

2

3

4

5

18-

16;

16

16

16

16

18•

16.

186

16!

16;

16!

• intermediate leg - cov a prirobnicam: hhll

18521000 4 4 1 1 0.0

18521100 0 1

16521101 3 0.0226

18521201 1 3

16521301 1.0 3

18521401 597.0 1 588.0 2 570.0 3 56

10521501 652010000 0 1 0 0.9313 1

18521502 652020000 0 1 0 0.7673 2

18521503 853010000 0 1 0 0.4088 3

18521504 654010000 0 1 0 0.6625 4

18521601 0 0 0 0 0.9313 1

16521602 0 0 0 0 0.7673 2

16521603 0 0 0 0 0.4088 3

18521604 0 0 0 0 0.6625 4

16521701 10227 0.166 0 0 4

16521601 0 10. 10. 0. 0. 0. 0. 1. 4

16521901 0 10. 10. 0. 0. 0. 0. 1. 4

1.0 4

8550000 clega pipe

8550001 5

8550101 0.010936 5

8550201 0.010936 4

• 6550301 0.37312 5

0550301 0.246875 5 * ReP#

8550401 0.0 5

6550501 0.0 5

8550601 0.0 5

65S0701 0.0 S

6550801 0.10-03 0.1180 5

6550901 0.0 0.0 4

8551001 00 5

8551101 100000 4 •fvcahoAv.0

• should be input as not used

8551201 103 1.58753 +07 5.60350e002 0.O0000e+00

6551202 103 1.58745e÷07 5.60349e+02 0.00000o.00

6551203 103 1.587360+07 5.603490.02 0.00000e+00

8551204 103 1.567276+07 5.603496+02 0.000006,00

6551205 103 1.567160.07 5.603495e02 0.000000+00

...................

• hhs toplotna telesa - primarni covovod 2

*......... *.* ......................

vsa toplotna telesa primarnih cevovodov so poonstavljena v

plosce

0

0

0

0

0

0

0

0

0

0

1

2

3

4

5

* * hot leg - coe s prirobticamt: hhll

• 16021000 3 4 1 1 0.0

18021100 1 0 1

' 18021101 3 0.0286

1 18021201 1 3

* 18021301 1.0 3

• 18021401 597.0 1 566.0 2 570.0 3

• 18021501 803010000 0 1 0 0.5353 1

* 18021502 802010000 0 1 0 0.4406 2

• 18021503 802020000 0 1 0 0.6679 3

• 16021601 0 0 0 0 0.5353 1

• 18021602 0 0 0 0 0.4406 2

16021603 8 0 0 0 0 0.6879 3

• 16021701 10229 0.333 0 0 3

* 18021801 0 10. 10. 0. 0. 0. 0. 1. 3

* 16021901 0 10. 10. 0. 0. 0. 0. 1. 3

• hot leg - cv a prirobuicami: hh•l

18021000 15 4 1 1 0.0

18021100 0 1

18021101 3 0.0286

18021201 1 3

21

561.0 4

intermedista log - cov s prirob1icmi: bhll

521000 20 4 1 1 0.0

521100 0 1

521101 3 0.0226

521201 1 3

521301 1.0 3

521401 597.0 1 586.0 2 570.0 3 561

521501 652010000 10000 1 0 0.1663 S

521502 652060000 10000 1 0 0.1535 10

521503 653010000 10000 1 0 0.0616 15

521504 654010000 10000 1 0 0.1325 20

521601 0 0 0 0 0.1863 5

521602 0 0 0 0 0.1535 10

521603 0 0 0 0 0.0818 15

521604 0 0 0 0 0.1325 20

521701 10227 0.0332 0 0 20

521801 0 10. 10. 0. 0. 0. 0. 1. 20

521901 0 10. 10. 0. 0. 0. 0. 1. 20

* cold log - cwv a prirobnicamit hhll

16551000 2 4 1 1 0.0

18551100 0 1

16551101 3 0.0279

18551201 1 3

15551301 1.0 3

16551401 597.0 1 588.0 2 570.0 3

16551501 655010000 0 1 0 0.6915 1

16551502 656010000 0 1 0 0.6915 2

16551601 0 0 0 0 0.6915 1

16551602 0 0 0 0 0.6915 2

18551701 10227 0.166 0 0 2

16551601 0 10. 10. 0. 0. 0. 0. 1. 2

16551901 0 10. 10. 0. 0. 0. 0. 1. 2

1.0 4

561.0 4 6551300

6551301

8551302

8551303

6561304

0

6.309600+00 6.309608.00 O.00000,e00 1

6.30960e*00 6.30980s#00 0.00000+0O0 2

6.30980e.00 6.309@0e800 0.000000*00 3

6.309606*00 6.309600e00 0.O000OO0 4

8580000 junas8 ingijun

8500101 855010000 856000000 0.0 0.002 0.002 130000

6580201 0 6.309800+00 6.30950e,00 0.000000e00 cold log - cev a priroboucami: bhll
18551000

18551100

18551101

18551201

18551301

18551401

18551501

18551502

18551601

18551602

18551701

18551801

18551901

10 4 1 1 0.0

0 1

3 0.0279

1 3

1.0 3

597.0 1 588.0 2 570.0 3 561.0 4

858010000 10000 1 0 0.1383 5

856010000 10000 1 0 0.1383 10

0 0 0 0 0.1383 5

0 0 0 0 0.1383 10

10227 0.0332 0 0 10

0 10. 10. 0. 0. 0. 0. 1. 10

0 10. 10. 0. 0. 0. 0. 1. 10

* ddhh2 i dh korekcija nekaterih rc82 tlacnlih zagnaval

.............................................................. •

* cv 820 dh korigirano tlacno zaznavalo 802-10 [pal

20582000 pk80202 sum 9.8067 0.0 1

20582001 0.0 0.10197 p 802100000 -0.15 rho 802100000 * R.

: ,v 821 a dh korigirano tlacno zazoavalo 401-06 (pal

20582100 pk40106 sum 9.8067 0.0 1

20582101 0.0 0.10197 p 401060000 -0.8425 rho 401060000

• cv822 dh korigirano tlacno zaznavalo 852-01 (pal

20582200 pk85201 sum 9.8067 0.0 1

20582201 0.0 0.10197 p 852010000 -0.15 rho 852010000 •R

* CV 823 a d korigirano tlacno zaznavalo 852-10 [pal

20582300 pk85202 sum 9.8067 0.0 1

20582301 0.0 0.10197 p 852100000 - 0.15 rho 852100000 * R.

: c 824 1 dh korigirano tlacno zaznavalo 854-05 (pal

20582400 pk85401 suN 9.8067 0.0 1

20582401 0.0 0.10197 p 8840S0000 -0.15 rho 854050000 R +÷

** ccvvii dpmeasured - gravity term - zanka 2

** a blok cv je uporablian mad rc.2 dp inicializacijo

upostevana so vse dh korekcije tlacnih zaznaval

CV 830 t dp2lh (bar)

•20583000 dp2lh sum 1.00-05 .0.0763 0

•20583001 0.0 1.0 p 802010000 -1.0 p 803010000 * dh-O.Om

"V C 831 : dp2lv (bar]

*20583100 dp2lv sum 1.00-05 -0.0792 0

*'20S83101 0.0 1.0 p 802020000 -1.0 p 802010000 1.0

cutrIvar 832

'20583101 0.0 1.0 c¢trlvar 820 -1.0 p 802010000 1.0

c0trIvar 832

** ev 832 dp2lv gravity term [pal

'20583200 dpgt sum 9.8067 0.0 1

*20583201 0.0 1.7317 rho 802010000

cv 833 dpSl (bar]

•20S83300 dp51 sam 1.0e-05 -0.0562 0

**20583301 0.0 1.0 p 401010000 -1.0 p 802020000 1.0

catrIvar 834

'20583301 0.0 1.0 p 401010000 -1.0 cntrivar 820 1.0

cntrlvar 834

C cv 834 dpSl gravity term (pal

'20583400 dpgt OEM 9.8067 0.0 1

'20583401 0.0 0.364 rho 802020000

** Cv 835 hot leg 4p (bar]

"20583500 hIdp Sum 1.0.-OS -0.2117 0

'20583501 0.0 1.0 p 401010000 -1.0 p 803010000 1.0 cntrlvar

836

** cv 836 hldp gravity term (pal

'20583600 dpgt sum 9.8067 0.0 1

'20583601 0.0 2.0957 rho 802010000

cv 837 t dpS2x (bar]

'20583700 dpS2x sum 1.Oe-05 -1.1424 0

-20583701 0.0 1.0 p 401060000 -1.0 p 401010000 1.0

cntrlvar 838 *20583701 0.0 1.0 cntrlvar 821 -1.0 p 401010000 1.0

catrlvar 838

** CV 838 a dp52x gravity term (pal

'20583800 dpt sum 9.8067 0.0 1

-20S83801 0.0 9.2065 rho 401020000

** cv 839 : dpS3x (bar]

'20583800 dpS3x sum 1.08-05 -0.9681 0 **20583901 0.0 1.0 p 413010000 -1.0 p 401060000 1.0

cntrivar 840

-20583901 0.0 1.0 p 413010000 -1.0 ctrilvar 821 1.0

catrlvar 840

* Cv 840 : dps3x gravity term (pa]l

:20584000 dpgt sum 9.8067 0.0 1

"20584001 0.0 -9.2065 rho 401080000

CV 841 1 steam generator dp [bar)

"20584100 sgdp sum 1.08-05 -2.1105 0

'20584101 0.0 1.0 p 413010000 -1.0 p 401010000 * dh.O.0a

ev C- 842 1 dpS4 [bar]

:20584200 dp54 sum 1.00-05 -0.1801 0

.20584201 0.0 1.0 p 852010000 -1.0 p 413010000 1.0

catrIvar 843

'20584201 0.0 1.0 cntrlvar 822 -1.0 p 413010000 1.0

catrIvar 843

Cv 843 : dpS4 gravity term (pal

"20584300 dpgt aum 9.8067 0.0 1

-20584301 0.0 -0.364 rho 852010000

22

- cv 844 : dp22vg (bar]

-20584400 dp22vg sum 1.Oe-0S -0.0576 0

"-20584401 0.0 1.0 p 852020000 -1.0 p 852010000 1.0

cntrlvar 845

'20584401 0.0 1.0 cntrIvar 823 -1.0 cntrlvar 822 1.0

cntrivar 845

Scv 845 a dp22vg gravity term (pal

'20584S00 dpgt sum 9.8067 0.0 1

-20S84501 0.0 -4.4007 rho 852020000

• CV 846 a dp22vp [bar]

*20584600 dp22vp suam 1.0e-0S -0.0634 0

•"20584601 0.0 1.0 p 854010000 -1.0 p 852020000 1.0

cntrlvar 847

'20584601 0.0 1.0 cntrlvar 824 -1.0 cntrivar 823 1.0

cntrlvar 847

* CV 847 a dp22vp gravity term (pal

'20884700 dpgt sum 9.8067 0.0 1

*20584701 0.0 1.967 rho 853010000

CV 848 i intersediate leg dp (bar]

'20S84800 ildp sum 1,00-05 -0.3011 0

*-20584801 0.0 1.0 p 854010000 -1.0 p 413010000 1.0

cntrivar 849

'20584801 0.0 1.0 cntrlvar 924 -1.0 p 413010000 1.0

cntrlvar 849

' CV 849: ildp gravity term (pal

'20584900 dpgt sum 9.8067 0.0 1

'20584901 0.0 -2.797 rho 852020000

CV $O 850 dp22p (bar]

'20585000 dp22p sum 1.Oe-OS 0.0 1

-"20585001 0.0 1.0 p 855010000 -1.0 p 854010000 1.0

cotrlvar 851

'2058001 0.0 1.0 p 855010000 -1.0 cntrIvar 824 1.0

cntrlvar 851

Cv 851 B dp22p gravity term (pal

'20585100 dpgt sum 9.8067 0.0 1

'20585101 0.0 0.232 rho 854010000

CV 852 a dp23h [bar)

*20585200 dp23b sum 1.0e-OS -0.0303 0

'2058201 0.0 1.0 p 856010000 -1.0 p 855010000 * dh.o.OM

.....................

• sgg uparjalnik 3
* k•ck : inicializacija uperjalnika

SsMase skundarnega hledila Je ustrezna (., 790 kg - apodnja maja)

* pri recirkulacijskem razmsrju 4x

* :kasneje ji bila mues ob dvigu nivoja povecana ns 800 kg,

downcomr

• je nekoliko povecan, da preprecimo prolivanja kapljevine

cat rob

* ;odstopek tlaka ns eskundarni strani (1.1 bar) zmanjsan z

dvigom

• tcold ns zgornjo tolerancno majo (+0.5 k) --. puek akoraj

doasez

• spodnjo toleranco (68.7 bar) : 68.59 bar

* :rcs tcold : 286.7 c *- 0.5 c (559.85 k)

* prim. cistem: mg vetop

9110000 hl-ag snglJun

*l 9110101 902010000 501000000 1.0936o-02 0.57 0.46 00100

9110101 902010000 501000000 1.09365-02 0.616 0.46 130100

9110201 0 6.36790s.00 6.56940o.00 0.O0000e+0

* prim. aistes: 3g vstopni prskat in u-covl

5010000 ag-tube pipe

5010001 11

• 5010101 0.04394 1 0.010342 11

5010101 0.04394 1 0.0103423 11

S010201 0 10

5010301 0.798 1 2.0 5 1.725 7 2.0 11

5010401 0 11

5010501 0 11

5010601 85.0 1 90.0 5 45.0 6 -45.0 7 -90.0 11

5010701 0.728 1 2.0 5 1.685 6 -1.685 7 -2.0 11

*! S010801 0.18-03 0.091 1 0.Ole-03 0.01968 11

5010801 0.le-05 0.091 1 0.018-07 0.01968 11

*t 5010901 0.44 0.60 1 0.01 0.01 5 0.22 0.22 6 0.01

0.01 20

5010901 0.01 0.01 1 0.0 0.0 10

5011001 00 11

*! 5011101 00100 1 00000 10

5011101 100000 10

S011201 103 1.$5556e.07 S.63746e+02 0.O0000*O00 0 0 1

5011202 103 1.551870+07 5.63172*.02 0.O0000eO00 0 0 2

S011203 103 1.54826@+07 5.62658S.02 0.00000e.00 0 0 3

5011204 103 1.54466s+07 5.62198sa02 0.O0000e+00 0 0 4

5011205 103 1.541058s07 5.61784e,02 0.O0000eO00 0 0 5

5011206 103 1.53771e+07 5.61454es02 0.O0000e+00 0 0 6

5011207 103 1.535870+07 5.612590+02 0.O0000e.00 0 0 7

5011208 103 1.53523es07 5.60864s.02 0.00000a.00 0 0 8

5011209 103 1.53457e+07 5.60605e.02 0.O0000e.00 0 0 9

5011210 103 1.533910.07 5.60379*.02 0.O0000e+00 0 0 10

5011211 103 1.53325s.07 5.60180s.02 0.00000o.00 0 0 11

5011300 0

5011301 6.73340e+00 6.733400.00 0.O0000eO00 1

8011302 6.72420ss00 6.72420es00 0.O0000eO00 2

5011303 6.71600es00 6.71600s.00 0.O0000eO00 3

5011304 6.708800e00 6.708800.00 0.O0000O.00 4

5011305 6.70230se00 6.70230o.00 0.O0000O00 S

5011306 6.69730e.00 6.69730s.00 0.O0000e.00 6

5011307 6.69270a.00 6.69270s+00 0.00000*O0 7

5011308 6.68790e,00 6.68790s.00 0.00000s00 8

5011309 6.68370s:.00 6.68370s.00 0.O0000Os0 9

5011310 5.865080.00 5.86580s.00 0.O00OOsO0 10

5011401 .01968 0.0 1.0 1.0 10

* prim. iastem: mg izatopni prskat

5130000 o-0h branch

5130001 1 0

)1 5130101 0.0 0.790 35.061e-03 0.0 -85.0 -0.728 0.ls-03

0.091 00

5130101 0.0 0.798 35.081e-03 0.0 -85.0 -0.728 0.1s-04

0.091 00

5130200 103 1.53427s.07 5.60188e+02

*1 5131101 501010000 513000000 0.010342 0.60 0.44 00100

5131101 501010000 513000000 0.0103423 0.3 0.2 1300C0

5131201 6.67690s,00 6.96280es00 0.O0000O00

* prim. sistem: ag izatop

9610000 ag-cl 3ngljUn

*I 8610101 513010000 952000000 1.09360-02 0.46 0.57 00100

9610101 513010000 952000000 1.0936s-02 0.01 0.02 130100

9610201 0 6.31440Se00 6.53290s.00 0.O0000eO00

*•it*.**t***** .tti*t~tt .tli*t•••••t**t 

* ask. cutss:t dvizni kanal

5030000 riaer pipe

5030001 6

5030101 0.0 6

5030201 0.01291 1 0.0214 4 0.048695 5

5030301 2.0 4 2.9605 5 0.8295 6

* o:vcaenae wea askundarnsga hladila

*++ 5030401 0.11523 4 0.17171 5 0.04041 6

5030401 0.12513 4 0.18171 5 0.04041 6

5030501 0 6

5030601 90.0 6

5030701 2.0 4 2.9605 5 0.8295 6

5030801 0.10-03 0.03503 5 0.ls-03 0.249 6

5030901 5.46 5.46 1 3.32 3.32 4 0.1 0.1 5

5031001 00 6

5031101 100100 4 100000 5

5031201 100 6.88635..05 1.245440.06 2.58278e.06

0.O0000O.00 1

5031202 100 6.87346*.06 1.251470.06 2.58289s.06

0.O0000e00 2

5031203 100 6.862240.06 1.25111se06 2.58298s.06

0.O0000e00 3

5031204 100 6.85241s.06 1.25062e+06 2.58305eu06

0.O0000O00 4

5031205 100 6.84126e.06 1.25006s.06 2.58314s.06

0.000000,00 5

5031206 100 6.83290e+06 1.24938e+06 2.56318o.06

0.O0000O.00 6

S031300 0

5031301 4.72634s-02 2.73670s-01 0.00000..,0 1

5031302 5.13251@-02 3.89160e-01 0.00000e00 2

5031303 5.53478e-02 4.40620o-01 0.00000o.00 3

5031304 6.06000e-02 4.894308-01 0.00000e.00 4

5031305 7.43053e-02 7.34650s-01 0.O0000eO00 S

5031401 0.027 0.0 1.0 1.0 5

• sek. sisteu: asperstor pare

5070000 mepyr sesprstr

23

5070001 3 0

5070101 0.0 1.9430 0.09447 0 90.0 1.9430 0.le-04 0.249

0

5070200 100 6.82489s+06 1.24924s.06 2.58329o.06 1.46050o-01

5071101 507010000 510000000 4.86950-02 0.82 0.14 01000

0.0

5072101 507000000 508000000 44.91500-02 0.26 0.23 01000

0.0

5073101 503010000 507000000 4.86950-02 0.0 0.0 01000

5071201 -9.28200o-02 3.06330*-Ol 0.O0000e00

5072201 4.68581s-03 -1.70166e-02 0.00000e00

S073201 7.22506s-02 7.61480e-01 0.00000*o00

* uok. ictsum: tgornji parni prostor

5100000 studoms pipe

5100001 2

5100101 0.0 2

5100201 0.0 1

5100301 1.0800 1 0.4000 2

5100401 0.54287 1 0.134040 2

5100501 0.0 2

5100601 90.0 2

5100701 1.0600 1 0.4000 2

5100801 0.1-O03 0.8000 1 0.10-03 0.41905 2

5100901 0.0 0.0 1

5101001 00 2

5101101 100000 1

5101201 102 6.81065o.06 1.00000000 0.O0000e.00 0 0 1

5101202 102 6.81840e.06 1.00000 00 0.000000+00 0 0 2

5101300 0

5101301 -9.21296e-03 4.43731e-02 0.O0000O00 1

a sak. Siutma: spoj uperJelnika in perovoda

5110000 ag-cl sngijun

5110101 910010000 520000000 0.0011401 0.222 1,0 130100

5110201 0 6.85760ss00 6.87050oS00 0.00000@.00

* sok. mistem: povratni kanal (zgornji obrocasti del)

5190000 udownann branch

5190001 1 0

5190101 0.0 1.9430 0.3078 0 90.0 1.9430 0.Ie-03 0.1930

00

5190200 102 6.82494e+06 8.101OOO-03

*5191101 510000000 519010000 0.44915 0.0 0.0 00100

5191101 510000000. 519010000 0.0 O.S 0.5 130100

5191110 0.1930 0.0 1.0 1.0

5191201 3.045000-01 3.67449.-0D 0.00000a.00

- ask. sictam: povrstni kanal (rodnjli obrocasti del)

5080000 mdownann branch

5080001 2 0

5080101 0.0 0.8278 0.081723 0 -90.0 -0.8275 0.1o-0O

0.176 00

5080200 102 6.834160+06 0.00000..00

5081101 519000000 508000000 0.0 0.09 0.15 00000

*5082101 508010000 509000000 0.030415 0.0 0.0 00100

S082101 508010000 509000000 0.0 0.43 0.60 130100

5081110 0.1930 0.0 1.0 1.0

5082110 0.1760 0.0 1.0 1.0

5081201 1.764460-04 -3.00110-01 0.O0000eO00

5082201 1.16890o-01 1.38490*-01 0.O0000e00

* ask. sisetm: povratni kanal (spodnji cevni del)

5090000 pipedown pipe

5090001 5

5090101 0.0 5

6.52236e-02

1.89380e-01

2.99390-Ol

3.94690e-01

4.19940o-01

4.017200-01
S090201 0.0 1 0.005536 4

5090301 2.9625 1 2.0 5

5090401 0.06909 1 0.01167 4 0.01456 S

5090501 0 5

5090601 -90.0 5

5090701 -2.9625 1 -2.0 S

5090501 0.1.-03 0.05953 1 0.1.-03 0.0431 5

S090901 0.47 0.57 1 0.05 0.05 4

5091001 00 5

5091101 100100 1 100000 4

5091201 103 6.845460.06 5.427760+02 0.000000.00

5091202 103 6.867000.06 5.42708e.02 0.00000*+00

5091203 103 6.55200o.06 5.427990402 0.000000+00

5091204 103 6.597000.06 5.42511e.02 0.000000*00

5091205 103 6.91205e+06 5.425490+02 0.000000+00

5091300 0

5091301 4.67180o-01 4.671004-01 0.00000e+00 1

5091302 4.670900-01 4.67090-01 O0.000000+00 2

5091303 4.67050.-Ol 4.670800-01 0.O0000oo00 3

3091304 4.670800-01 4.670500-01 0.O0000Oe0 4

5091410 0.0431 0.0 1.0 1.0 4

15013000 10 4 2 1 0.00984

15013100 0 1

0

0

0

0

0

0 1

0 2

0 3

0 4

0 5

15013101 3 0.01111

15013201 3 3

15013301 0.0 3

15013401 570.330 1

- prim. --*

15013501 S01020000

15013502 501030000

15013503 501040000

15013504 501050000

15013505 501060000

15013506 501070000

15013507 501050000

15013505 501090000

15013509 S01100000

15013510 501110000

* --. sak.

15013601 503010000

15013602 503020000

15013603 503030000

15013604 503040000

15013605 503050000

15013606 503050000

15013607 503040000

15013605 503030000

15013609 503020000

15013610 503010000

566.810 2 563.420 3 560.15 4

0 1 1 65.0 1

0 1 1 65.0 2

0 1 1 65.0 3

0 1 1 68.0 4

0 1 1 58.65 5

0 1 1 55.65 6

0 1 1 65.0 7

0 1 1 68.0 8

0 1 1 68.0 9

0 1 1 65.0 10

0 1 1 64.0 1

0 1 1 68.0 2

0 1 1 65.0 3

0 1 1 65.0 4

0 1 1 55.65 S

0 1 1 55.65 6

0 1 1 65.0 7

0 1 1 68.0 a

0 1 1 65.0 9

0 1 1 68.0 10

15014701

15014501

15014901

* riser (breo upper cylindrical shell) - plosca: bull

15031000 5 4 1 1 0.0

15031100 0 1

15031101 3 0.0159

15031201 1 3

15031301 1.0 3

15031401 597.0 1 555.0 2 570.0 3 561.0 4

15031501 503010000 0 1 0 2.595 1

15031502 503020000 0 1 0 2.895 2

15031503 503030000 0 1 0 2.895 3

15031504 503040000 0 1 0 2.895 4

15031505 503050000 0 1 0 4.286 5

15031601 0 0 0 0 2.895 1

15031602 0 0 0 0 2.695 2

15031603 0 0 0 0 2.595 3

15031604 0 0 0 0 2.595 4

15031605 0 0 0 0 4.256 5

15031701 10231 0.2 0 0 5

15031501 0 10. 10. 0. 0. 0. 0. 1. 5

15031901 0 10. 10. 0. 0. 0. 0. 1. 5

* upper-inner cylindrical shell --. plosca

15032000 2 4 1 1 0.0

15032100 0 1

15014301 0.0 3

15014401 597.0 1 558.0 2 570.0 3 561.0 4

15014501 501010000 0 1 0 0.1139 1

15014502 513010000 0 1 0 0.1139 2

15014601 509050000 0 1 0 0.1139 1

15014602 503010000 0 1 0 0.1139 2

0 0 0 0 2

0 10. 10. 0. 0. 0. 0. 1. 3

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

* Oak. sistem: spoj povratnega in dviznmga kanala

* ni -abrupt area change- modela - regulacija recirkulacije

5350000 dras valve

5350101 509010000 503000000 0.025761 0.0 0.0 100000

5350201 0 1.05820~-01 1.44390e-01 O.OOOOOo00O

5350300 srvvlv

5350301 524

5350401 0.01 0.01 0.01 * zaprtO

5350402 1.0 1000.0 1000.0 * odpr•o

* ccci s93 recirkulacija: 4i : 4 * 0.525 kg/s - 2.100 kg/s

20552400 rng535 sum 1.0 0.02847 0 3 0.01 1.0

20552401 0.0002100 -0.0001 oflowi 535000000 1.0 cntrlvar

524

*20552400 ragS3S constant 1.0

................ . . *.......t***............... .......

dolocitev vpliva recirkulacije na aso sekundarn•ga hladila

v uparjalniku ,

** ccci 8g3 recirkulacila: Os: 1.050 kg/s a 2x -.-. lOOOs:

4.200 kg/s - 4X

*20552000 refflow function 1.0 1.050 0

*20552001 time 0 520

*20252000 reac-t 0

20252001 0.0 1.050 1000.0 4.200

*20552400 rag53S su 1.0 0.0151535 0 3 0.01 1.0

20552401 0.0 0.0001 cntrlvsr 520 -0.0001 mflowj 535000000 1.0

cntrlvar 524

•bhss toplotna tolesa ag 3

..................... .................

u cevi

15013701 0 0 0 0 10

15013501 0 10. 10. 0. 0. 0. 0. 1. 10

15013901 0 10. 10. 0. 0. 0. 0. 1. 10

Sdividing plate in channel head

15011000

15011100

15011101

IS011201

15011301

15011401

15011501

15011601

15011701

15011803

15011901

1 4 1 1 0.0

0 1

3 0.012

1 3

0.0 3

597.0 1 558.0 2 570.0 3

S01010000 0 1 0 0.26643 1

513010000 0 1 0 0.26643 1

0 0 0 0 1

0 10. 10. 0. 0. 0. 0. 1. 1

0 10. 10. 0. 0. 0. 0. 1. 1

561.0 4

561.0 4

15032101

15032201

15032301 IS032301

15032401

15032501

15032502

15032601

15032602

15032701

15012501

15032901

3 0.006

1 3

0.0 3

597.0 1 585.0 2 570.0 3

505010000 0 1 0 0.6633 1

519010000 0 1 0 1.5537 2

503060000 0 1 0 0.6633 1

507010000 0 1 0 1.5537 2

0 0 0 0 2

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

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

561.0 4

* cnannsl head : zunanja steno --. , plo41ca

15012000 2 4 1 1 0.0

15012100 0 1

15012101 3 0.0595

15012201 1 3

15012301 0.0 3

15012401 597.0 1 555.0 2 570.0 3

15012501 501010000 0 1 0 0.40167 1

15012502 513010000 0 1 0 0.40167 2

15012601 0 0 0 0 0.40147 1

15012602 0 0 0 0 0.40167 2

15012701 0 0 0 0 2

15012601 0 10. 10. 0. 0. 0. 0. 1. 2

15012901 0 10. 10. 0. 0. 0. 0. 1. 2

Stubtasheet

15014000 2 4 1 1 0.0

15014100 0 1

15014101 3 0.1545

15014201 1 3

24

* upper slaem and upper ead ---. plosce 15101.. .15104

15101000 1 4 1 1 0.0

15101100 0 1

15101101 3 0.0210

15101201 1 3

15101301 0.0 3

15101401 597.0 1 588.0 2 570.0 3 561.0 4

15101501 0 0 0 0 1.005 1

15101601 510020000 0 1 0 1.005 1

15101701 0 0 0 0 1

15101501 0 10. 10. 0. 0. 0. 0. 1. 1

15101901 0 10. 10. 0. 0. 0. 0. 1. 1

15102000 1 4 1 1 0.0

15102100 0 1

15102101 3 0.0258

15102201 1 3

15102301 0.0 3

15102401 597.0 1 585.0 2 570.0 3 561.0 4

15102501 0 0 0 0 3.3870 1
1S102601 510010000 0 1 0 3.3870 1

15102701 0 0 0 0 1

15102801 0 10. 10. 0. 0. 0. 0. 1. 1

15102901 0 10. 10. 0. 0. 0. 0. 1. 1

15103000 1 4 1 1 0.0

15103100 0 1

15103101 3 0.0947

15103201 1 3

15103301 0.0 3

15103401 597.0 1 580.0 2 570.0 3 561.0 4

15103501 0 0 0 0 0.4463 1

15103601 519010000 0 1 0 0.4463 1

15103701 0 0 0 0 1

15103801 0 10. 10. 0. 0. 0. 0. 1. 1

15103901 0 10. 10. 0. 0. 0. 0. 1. 1

15104000 1 4 1 1 0.0

15104100 0 1

15104101 3 0.0245

15104201 1 3

15104301 0.0 3

15104401 597.0 1 588.0 2 570.0 3 561.0 4

15104501 0 0 0 0 3.2448 1

15104601 506010000 0 1 0 3.2448 1

15104701 0 0 0 0 1

15104801 0 10. 10. 0. 0. 0. 0. 1. 1

15104901 0 10. 10. 0. 0. 0. 0. 1. 1

: downcomer -- a pl0sCe 5091-01, 5092-01-02-03-04

15091000 1 4 1 1 0.0

15091100 0 1

15091101 3 0.00394

15091201 1 3

15091301 0.0 3

15091401 597.0 1 588.0 2 570.0 3 561.0 4

15091501 0 0 0 0 4.0116 1

15091601 509010000 0 1 0 4.0116 1

15091701 0 0 0 0 1

15091601 0 10. 10. 0. 0. 0. 0. 1. 1

15091901 0 10. 10. 0. 0. 0. 0. 1. 1

15092000 4 4 1 1 0.0

15092100 0 1

15092101 3 0.00276

15092201 1 3

15092301 0.0 3

15092401 597.0 1 588.0 2 570.0 3 561.0 4

15092501 0 0 0 0 1.2028 1

15092502 0 0 0 0 1.2028 2

15092503 0 0 0 0 1.2028 3

15092504 0 0 0 0 1.2028 4

15092601 509020000 0 1 0 1.2020 1

15092602 509030000 0 1 0 1.2028 2

15092603 509040000 0 1 0 1.2028 3

15092604 509050000 0 1 0 1.2028 4

15092701 0 0 0 0 4

15092801 0 10. 10. 0. 0. 0. 0. 1. 4

15092901 0 10. 10. 0. 0. 0. 0. 1. 4

• 3.ggccvv o9 3 kontrolne uprmwnljivke

- cv S03, sg32 nivo v povratneu kanalu [m)

20550300 ITvdC Sum 1.0 13.45 1

20550301 0.0 2.0 voidf S09050000 2.0 voidf 509040000

20S50302 2.0 voidf 509030000 2.0 voidf 509020000

20550303 2.9625 voldf 509010000 0.8275 voidf 508010000

20550304 1.9430 voidf 519010000

*cv SOS: 9g3: masa sakundarnega hladila (kg]

20SSOSO 0 sgmaga Sum 1.0 790.0 1

-+. 20550501 0.0 0.11513 rho S03010000 0.11513 rho

503020000

*.+ 20550502 0.11513 rho 503030000 0.11513 rho

503040000

*a, 20550503 0.17171 rho 503050000 0.04041 rho

503060000

20550501 0.0 0.12513 rho 503010000 0.12513 rho 503020000

20550502 0.12513 rho 503030000 0.12513 rho 503040000

20550503 0.18171 rho 503050000 0.04041 rho 503060000

20550504 0.09466 rho 507010000 0.54207 rho 510010000

20550505 0.13404 rho 510020000 0.30780 rho 519010000

2055050 0.08172 rho 508010000 0.06909 rho 509010000

20550507 0.01167 rho 509020000 0.01167 rhO 509030000

20550508 0.01167 rho 509040000 0.01456 rho 509050000

*saff main feedvater 3

............... ............. ...... 

* konstantai ew tok

5340000 Efa tmdpjun

5340101 531000000 532000000 0.0266

5340200 1 SOS - si

5340201 -1.0 0.52517 0. 0.

5340202 0.0 0.52517 0. 0.

5340203 6,0 0.0 0. 0.

• volumaki mNw tok

-20550200 yeNu div 1.0 0.0 1

*20550201 rhof 532010000 eflowr 532010000

* feedvater line

5320000 Mvline branch

5320001 1 0

5320101 S.5575-04 10.0 0 0 60.0 7.0 0.Ole-03 0.0266 00

5320200 103 6.862750+06 4.80974o.02

*5321101 532010000 508000000 0.0006786 0. 0. 00100

5321101 532010000 S08000000 0.0 1.0 0. 130100

5321201 1.115605+00 1.11560e+00 0.O0000e+00

• vir napajalne vode

5310000 fwsource tdpvol

5310101 1.0 0.0 10.0 0 0 0 0.01e-03 0.0 00

5310200 103

5310201 0 70.0+5 491.0

25

* cci "regulaciija sg3 nivoja

" ob konstantni eNV 534 regulirao nivo v povratnea kanalu

5290000 v529 tedpvol

5290101 1.0 0.0 10.0 0.0 0.0 0.0 0.2e-03 0.0 0

5290200 103

5290201 0 70.0+S 491.0

5300000 J530 tdpjun

5300101 529000000 519010000 0.0

5300200 1 0 cntrlvar 503 * 89 level

5300201 -1.0 0.0 0.0 0.0

5300202 13.35 1.5 0.0 0.0

5300203 13.45 0.0 0.0 0.0

5300204 13.SS -1.5 0.0 0.0

*5300000 J530 twdpjun

*5300101 529000000 519010000 0.0

-5300200 1 0 cntrlvar SOS * ag Wass

*5300201 -1.0 0.0 0.0 0.0

*5300202 790.0 1.5 0.0 0.0

*5300203 800.0 0.0 0.0 0.0

'5300204 810.0 -0.50 0.0 0.0

.. *..... .......... ......... 

* 8811 parovod 3

* team line frm porvavvlmiv

5200000 m*aline anglvol

5200101 0.0 31.65 68.Se-03 0 -45.0 -18.670 0.01-3 0.0525

00

S200200 102 6.812555÷06 1.000000*00

ahhmm

* 15201000 1 4 2 1 0.0525

15201000 1 4 2 0 0.0525 * ffll

15201100 0 1

15201101 3 0.0603

15201201 1 3

15201301 0.0 3

15201401 570.330 1 566.810 2 563.420 3 560.15 4

15201501 520010000 0 1 1 31.65 1

15201601 0 0 0 1 31.65 1

15201701 0 0 0 0 1

15201801 0 10. 10. 0. 0. 0. 0. 1. 1

15201901 0 10. 10. 0. 0. 0. 0. 1. 1

ccci regulacija tcold 3 preko tlaka aekundarne strani

................ *................... 

delta 5 Cold , bethay reference .559.85 k

20550000 dtcold mm 1.0 0.0 0

20550001 560.35 -1.0 tempf 955010000

* 20550001 559.35 -1.0 t*MPf 9SS010000 * 80

20554400 V544 mm 1.0 68.128.05 0
20554401 0.0 1.0 p 544010000 300. cntrlvar 500

SISO000 venturi sngljun

5150101 520010000 544000000 0.0 0.0 0.0 130000

5150201 0 6.87740e000 6.87740&.00 0.O0000.00

5440000 turbine tmdpvol

5440101 10.0 0.0 1000.0 0 0.0 0 0.2o-03 0 0

5440200 2 0 cntrlvar 544

5440201 -1.0 68.12e+05 1.0

5440202 1.0e+05 1.0O.0S 1.0

5440203 100.0e+05 100.0e+05 1.0

*rccss cevovodi priernega kroga 3

* prim. sietem: hot leg do surge line

9030000 hleg snglvol

* 9030101 0.010936 1.4441 0.0 0.0 0.0 0.0 0.le-03 0.1180

00

- 9030200 103 1.55957e+07 5.63790ea02

9030000 hleg pipe

9030001 5

9030101 0.010936 5

9030201 0.010936 4

9030301 0.28882 5

9030401 0.0 5

9030501 0.0 5

9030601 0.0 S

9030701 0.0 5

9030801 0.le-03 0.1180 5

9030901 0.0 0.0 4

9031001 00 5

9031101 100000 4 *fvcahs:v-0

should be input as not used

9031201 103 1,559420+07 5.63762u÷02 0.O0000e*00 0 0 1

9031202 103 1.55935o÷07 S.63762e602 0.O0000e÷00 0 0 2

9031203 103 1.55928o+07 5.63762*+02 0.O0000O.00 0 0 3

9031204 103 1.55921e+07 5.63762e÷02 0.O0000O00 0 0 4

9031205 103 1.559140+07 5.637620÷02 0.O0000+O00 0 0 5

9031300 0

9031301 6.36760e+00 6.36760e+00 0.O0000e÷00 1

9031302 6.36760e*00 6.36760e+00 0.O0000O+0 2

9031303 6.36760e+00 6.36760+.00 0.O0000e+00 3

9031304 6.36760e+00 6.36760@+00 0.00000*.00 4

: prim. sistem: hot leg spoj pri sl

9130000 U1913 sangljun

*1 9130101 903010000 902000000 0.0 0.0 0.0 00000

9130101 903010000 902000000 0.0 0.265 0.265 1230000

9130201 0 6.36770*.00 6.367700.00 0.O00000.00

prim. eistem: hot leg od al do ag

9020000 hleg pipe

9020001 2

9020101 0.010936 2

9020201 0.010936 1

9020301 1.1891 1 1.6558 2

9020401 0.0 2

9020501 0.0 2

* 9020601 9.0 1 70.0 2

* 9020701 0.1900 1 1.7317 2 * 9020801 0.le-03 0.1180 2

S! 9020901 0.31 0.31 1

9020901 0.24 0.24 1

* 9021001 00 2

* 9021101 100000 1

9021201 103 l.55880e,07 5.63790@+02 0.O0000e+00 0 0 1

9021202 103 1.55738e.07 5.63790e÷02 0.O0000e+00 0 0 2

* 9021300 0 9021301 6.29920e.00 6.29920e+00 0.O000OOe+0 0

• 9521001 00 2

* 9521101 100000 1

* 9521201 103 1.53406o+07 5.60210e*02 0.O0000e.00 0 0 1

• 9521202 103 1.535160.07 5.602200+02 0.oo000oo.00 0 0 2

* 9521300 0

• 9521301 6.24650e+00 6.24650.+00 0.O0000e+00 0

9520000 ileg_a pipe

9520001 10

9520101 0.010936 10

9520201 0.010936 9

9520301 0.S0244 S 0.41394 10

9520401 0.0 10

9520501 0.0 10

9520601 -76.0 5 -72.0 10

9520701 -0.48674 5 -0.39340 10 *

*t 9520801 0.le-03 0.1180 10

9520801 0.le-04 0.1160 10

*I 9520901 0.11 0.11 9

9020000 hleg pipe

9020001 10

9020101 0.010936 10

9020201 0.010936 9

9020301 0.23782 5 0.37116 10

9020401 0.0 10

9020501 0.0 10

9020601 9.0 5 70.0 10

9020701 0.036 5 0.34634 10 - ++

9020801 0.lA-03 0.110 10

9020901 0.0267 0.0267 9

9021001 00 10

9021101 100000 5 100000 9 * v-0

9021201 103 1.55866e.07 5.63760e÷0

9021202 103 1.55853e+07 5.63760e+0

9021203 103 1.55841e.07 5.63760e.0

9021204 103 1.55829e.07 5.63759e.0

9021205 103 l.SS816e.07 5.63759e*0

9021206 103 1.S57910.07 5.637580.0:

9021207 103 1.55752e.07 5.63757e+0;

9021208 103 1.557140.07 S.637560+0:

9021209 103 1.55676e.07 S.63755o÷0;

9021210 103 1.55637e.07 5.63754e.0:

9021300 0

9021301 6.367706+00 6.36770e.00 0

9021302 6.36770e+00 6.367700+00 0

9021303 6.36770e.00 6.36770e+00 0

9021304 6.36770eo00 6.36770e+00 0

9021305 6.36770e+00 6.367700+00 0

9021306 6.36780e+00 6.64560+000 0

9021307 6.36780e+00 6.64560e+00 0

9021308 6.36780e+00 6.64570e,00 0

9021309 6.36790e.00 6.645$0e+00 0

2

2

2

2

2

2

2

2

2

2

0.O0000e+0

0.O0000+e00

0.O0000+eO0

0.0000+eo00

0.O0000+e00

0.0000+e00

0.O0000eO.00

0.O00000e00

0.O0000e+00

0.O0000eO00

0

0

0

0

0

0

0

0

0

0

0 1

0 2

0 3

0 4

0 5

0 6

0 7

0 8

0 9

0 10

9520901 0.011 0.011 9

9521001 00 10

9521101 100000 9

9521201 103 1.53271e+07

9521202 103 1.532978+07

9521203 103 1.53323e607

9521204 103 1.533490407

9521205 103 1.53375e+07

9521206 103 1.53398e.07

9521207 103 1.53418e+07

9521208 103 1.53439o.07

9521209 103 1.53459e÷07

9521210 103 1.534800.07

9521300 0

5.60182o÷02

5.60183e.02

5.60185e+02

5.601866e02

5.601672+02

5.601B8e.02

5.60189e+02

5.60189e+02

5.60190e+02

5.60191e÷02

0.000000e00

0.O0000O00

0.000000+00

0.O00000e00

0.O00000e00

0. 00000+e00

0.000000.00

0.O00000e00

0.O00000O00

0.O0000e+00

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

1

2

3

4

S

6

7

8

9

10

.00000e*00

.O0000O00

.O00000e00

.O00000e00

.0000 +00

.O0000o.0

.O0000O+00

.O00000O00

.O00000e00

1

2

3

4

5

6

7

8

9

a g .......-........................

9521301 6.314506+00 6.594100+00 0.O0000e+00 1

9521302 6.31450e+00 6.594000+00 0.O0000e+00 2

9521303 6.31450e+00 6.59400e+00 0.O0000O00 3

9521304 6.31440*+00 6.594000+00 0.O0000e+00 4

9521305 6.31440e+00 6.59390e+00 0.O0000e÷00 5

9521306 6.31440e+00 6.59390e+00 0.O0000O00 6

9521307 6.314400.00 6.59390o+00 0.O0000e+00 7

9521308 6.31440e:00 6.593800+00 0.O0000e+0 8

9521309 6.31440e+00 6.59380o0e0 0.00000÷+0 9

9630000 jun963 sngljun

*I 9630101 952010000 953000000 0.0 0.20 0.20 130000

9630101 952010000 953000000 0.0 0.0 0.0 130000

9630201 0 6.31430ei00 6.5938000 .OO0000e+00

* prim. eistem: interm•'diate leg

9530000 ileg_b snglvol

9530101 0.010936 1.1027 0.0 0.0 9.0 0.180 0.1e-03

0.1180 00

9530200 103 1.535530.07 5.60220e+02

9530000 ileg. b pipe

9530001 S

9530101 0.010936 5

9530201 0.010936 4

9530301 0.22054 5

9530401 0.0 5

9530501 0.0 5

9530601 9.0 5

9530701 0.036 5

9530801 0.lo-03 0.1180 5

9530901 0.0 0.0 4

9531001 00 5

t

t

t

t)

t

t

t

prim. siste:m intermediate leg down

9520000 lloga pipe

9520001 2

9520101 0.010936 2

9520201 0.010936 1

9520301 2.5122 1 2.0697 2

9520401 0.0 2

9520501 0.0 2

9520601 -76.0 1 -72.0 2

9520701 -2.4337 1 -1.9670 2

*I 9520801 0.le-03 0.1100 2

9520801 0.ls-04 0.1180 2

*1 9520901 0.11 0.11 1

9520901 0.1 0.1 1

26
9531101 100000 4 *fveahesv.O

* should be Input as not used

9531201 103 1.53487*.07 5.60192e.02 O.00000e.00 0 01

9531202 103 1.53479o+07 5.60191e.02 O.O0000e.O0 0 0 2

9531203 103 1.534716+07 5.60191e÷02 O.00000e÷00 0 0 3

9531204 103 1.53463e+07 S.60191e.02 0.00000e*00 0 0 4

9531205 103 1.534550+07 5.60191e+02 0.O0000oOe0 0 0 5

9531300 0

9531301 6.31430e.00 6.31430e.00 0.O0000*O00 1

9531302 6.314400.00 6.31440e+00 0.O0000e+00 2

9531303 6.31440e+00 6.31440e+00 0.O0000e00 3

9531304 6.31440e-00 6.31440e.00 0.O0000e+00 4

9640000 jun964 sngljun

*1 9640101 953010000 954000000 0.0 0.20 0.20 00000

9640101 953010000 954000000 0.0 0.0 0.0 130000

9640202 0 6.31440e.00 6.314400.00 0.O0000Oe00

* . prim. slatem: intermediate leg up

* 9540000 lieg_c snglvol

* *9540101 0.010936 1.7870 0.0 0.0 90.0 1.7870 0.le-03

0.1180 00

* 9540101 0.010936 1.7871 0.0 0.0 90.0 1.7871 0.le-03

0.1180 00

* *.. podaljeek 0.1 m zaradi sklenitve rcs elevacij v rx

(napaka haze pod.)

* 9540200 103 1.534460+07 5.60220e.02

9540000 lieg_c pipe

9540001 5

9540101 0.010936 5

9540201 0.010936 4

9540301 0.35742 5

9540401 0.0 5

9540501 0.0 5

9540601 90.0 5

9540701 0.35742 5

9540801 0.le-03 0.1180 5

9540901 0.0 0.0 4

9541001 00 5

9541101 100000 4 *fvcahs:v-O

* should be input as not used

9541201 103 1.53434e+07 5.60191*.02 O.OOOOOe.00 0 0 1

9541202 103 1.533990.07 5.60190e.02 0.O0000Oe0 0 0 2

9542203 103 1.53364o÷07 5.60159e÷02 O.OOOOOe.00 0 0 3

9541204 103 1.53329e.0 7 5.60188e.02 O.OOOOOe.00 0 0 4

9541205 103 1.53294eo07 5.60186e*02 0.O0000O+0 0 0 S

9541300 0

9541301 6.31440e+00 6.59300e.00 0.O0000eO00 2

9541302 6.31440e.00 6.59390e*00 0.O0000oOe0 2

9541303 6.31450e.00 6.59400e+00 0.O0000e+00 3

9541304 6.314500+00 6.594000+00 O.OOOOOe+o0 4

• rcp-3

RCP•

9000000 1n3 branch

9000001 1 0

9000101 0.010936 0.232 0.0 0.0 90.0 0.232 0.0*-04 0.118

00

9000200 100 1.56151e.07 1.24842e.06 2.44514e006 O.OOOOOe.00

9001101 954010000 900000000 0.0 0.0 0.0 130000

9001201 6.31570e,00 6.59530e.00 O.OOOOe*O0

* pump loop 3

7030000 punp3 pump

7030101 0.0 0.097 14,06280-03 0.0 60.0 0.094 00

7030108 900010000 0. 0.47 0.49 100000 *÷s upor ustavljene

crpalke ?

7030109 901000000 0. 0.49 0.47 100000

7030200 0 1.56151e.07 1.24042e-06 2.44514e806 0.O0000e.00

7030201 0 6.315700+00 6.59530e.00 0.000000+00

7030202 0 1.06000e.00 1.06000e+00 0.O0000e.00

* pump index and option card

7030301 -2 0 -2 -1 0 505 0 * trip 505: si -. pump 3

stop

* pump description card

e1 7030302 311.0 1.0 0.063056 76.0 0.0

7030302 311.0 1.0 0.067939 78.0 0.0

* 7030302 311.0 1.0 0.068797 78.0 0.0 * 8#

7030303 S.0 751.0 0.0 0.0 74.39 71.39 0.0 *.. rated

density

* mh two phase pump head multiplier tables

7033000 0 0.0 0.0, 0.2 0.0, 0.4 1.0, 0.9 1.0. 1.0

0.0

* et two phase pump torque multiplier tables

7033100 0 0.0 0.0. 0.2 0.0, 0.4 1.0, 0.9 1.0, 1.0

0.0

• pump velocity table (rad/s)

7036100 505

7036101 300.0 311.0

7036102 305.0 201.0 310.0 141.1

7036103 320.0 113.1 330.0 88.0

7036104 340.0 75.4 350.0 62.8

7036105 370.0 47.1 400.0 37.7

7036106 500.0 22.0 700.0 15.7

7036107 916.0 10.5 917.0 0.0

9010000 out3 branch

9010001 1 0

9010101 0.0 0.084 5.460e-03 0.0 -90.0 -0.084 0.Ole-04

0.0 00

9010200 100 1.56151e÷07 1.248420.06 2.44514*.06 0.O0000o.00

9011101 901010000 955000000 0.0 0.0 0.0 130000

9011201 6.31570e+00 6.59530e.00 O.OOOOOe.O0

+ hhll-hhss rcp3

17030000 1 3 1 1 0.0

17030100 0 1

17030101 2 0.1

17030201 1 2

17030301 1.0 2

17030401 560.0 3

17030501 703010000 0 1 1 1.0 1

17030601 0 0 0 1 1.0 1

17030701 10701 1.0 0.0 0.0 1

17030801 0. 10. 10. 0. 0. 0. 0. 1. 1

27

.* prim. sistes: cold leg a

9SS0000 clega branch

9550001 1 0

* *! 9550101 0.010936 1.8656 0.0 0.0 0.0 0.0 0.1l-03

0.1180 00

* 9550101 0.010936 1.8656 0.0 0.0 0.0 0.0 0.1e-04 0.1180

00

* 9550200 103 1.58910e007 5.60350*e02 S*1 95551101 955010000 956000000 0.0 0.07 0.07 00000

• 9551101 955010000 956000000 0.0 0.002 0.002 130000

• 9551201 6.241308+00 6.24130e+00 O.OOOOOe.00

9550000 clega pipe

9550001 5

9550101 0.010936 5

9550201 0.010936 4 + 9550301 0.37/312 5

9550301 0.24875 5 • RCP+

9550401 0.0 5

9550501 0.0 5

9550601 0.0 5

9550701 0.0 5

9550801 0.le-03 0.1180 5

9550901 0.0 0.0 4

9551001 00 5

9551101 100000 4 *fvcahs;v.0

* should be input as not used

9551201 103 1.58753e+07 5.603S0e.02 0.O0000e*00 0 0 2

9551202 103 1.587450-07 5.603490e02 O.OOOOOeO00 0 0 2

9551203 103 1.55736e.07 5.60349e.02 0.O0000e+00 0 0 3

9551204 103 1.56727*+07 5.603490.02 0.O0000e*00 0 0 4

9551205 103 1.58718e.07 5.603494+02 0.O0000e00 0 0 5

9551300 0

9551301 6.30980e.00 6.30980e.00 0.OOOOOe00 1

9551302 6.30980e+00 6.30980o.00 O.OOOOOeO00 2

9551303 6.30980e.00 6.30980e*00 O.OOOOO00O 3

9551304 6.30980e÷00 6.30980e+00 0.O0000e.00 4

9580000 jungS8 engljun

9580101 955010000 956000000 0.0 0.002 0.002 130000

9580201 0 6.309800*00 6.30980e.00 0.OOOOO 00

* prim. siatem: cold leg b

+ 9560000 cleg_b snglvol

'2 9560101 0.010936 1.8656 0.0 0.0 0.0 0.0 0.1e-03

0.1180 00

* 9560101 0.010936 1.6656 0.0 0.0 0.0 0.0 0.18-04 0.1180

00

* 9560200 103 1.588758+07 5.60350e+02

9560000 cleg b pipe

9560001 5

9560101 0.010936 5

9560201 0.010936 4

9560301 0.37312 5

9560401 0.0 5

9560501 0.0 5

9560601 0.0 5

9560701 0.0 5

9560801 0.10-03 0.1180 5

9560901 0.0 0.0 4

9561001 00 5

9561101 100000 4 *fvcahs:v.O

• should be input as not used

9561201 103 1.587080+07 S.60349o.02 0.O0000&O00 0 0 1
9561202

0561303

9561294

9561205

9561300

9561301

9561302

9561303

9561304

103 1.567000.07 S.603495002 0*.0000000 0 0 2

103 1.586910+07 5.60349e+02 0.00000e+00 0 0 3

103 1.506620+07 5.60349o*02 0.00000e+00 0 0 4

103 1.586730.07 5.603490,02 0.00000*00 0 0 5 0

6.30990*.00 6.309900.00 0.00000÷0O0 1

6.309900e00 6.30990e+00 0.00000+0o0 2

6.309900.00 6.30990e+00 0.O0000e÷00 3

6.309900+00 6.309900.00 0.000000+00 4

* Sbus toplotna telexa - prlaen cevovod 3

• va toplotna tolesa primarunib cevovodov so poenostavljena v

ploce

b bot leg - cyv . prizrbicami. bhll * 19021000 3 4 1 1 0.0

* 19021100 0 1

• 19021101 3 0.0286

• 19021201. 1 3

• 19021301 1.0 3

* 19021401 597.0 1 568.0 2 S70.0

* 19021501 903010000 0 1 0 0.5353

2 19021502 902010000 0 1 0 0.4408

* 19021503 902020000 0 1 0 0.6679

• 19021601 0 0 0 0 0.5353 1

* 19021602 0 0 0 0 0.4408 2

• 19021603 0 0 0 0 0.6S79 3

* 19021701 10232 0.333 0 0 3

* 19021601 0 10. 10. 0. 0. 0. 0. 1. 3

* 19021901 0 10. 10. 0. 0. 0. 0. 1. 3

h bot leg - cv a prirobuicami, bbll

19021000 15 4 1 1 0.0

19021100 0 1

19021101 3 0.0286

19021201 1 3

19021301 1.0 3

19021401 597.0 1 586.0 2 570.0 3

19021501 903010000 10000 1 0 0.1070

19021502 902010000 10000 1 0 0.0801

19021503 902060000 10000 1 0 0.1376

19021601 0 0 0 0 0.1070 5

19021602 0 0 0 0 0.0861 10

19021603 0 0 0 0 0.1376 15

19021701 10232 0.0667 0 0 15

19021801 0 10. 10. 0. 0. 0. 0. 1. 15

19021901 0 10. 10. 0. 0. 0. 0. 1. IS

1

2

3

3 561.0 4

561.0 4

S

10

15

* 19521602 0 0 0 0 0.7673 2

* 19521603 0 0 0 0 0.4088 3

* 19521604 0 0 0 0 0.6625 4

* 19521701 10230 0.166 0 0 4

* 19521801 0 10. 10. 0. 0. 0. 0. 1. 4

* 19521901 0 10. 10. 0. 0. 0. 0. 1. 4

* intermedate I" - cev a priroboicami: h1l1

19521000 20 4 1 1 0.0

19521100 0 1

19521101 3 0.0226

19521201 1 3

19521201 1.0 3

19521401 597.0 1 588.0 2 570.0 1 561.0 4

19521501 952010000 10000 1 0 0.1863 5

19521502 952060000 10000 1 0 0.1535 10

19521503 953010000 10000 1 0 0.0818 15

19521504 954010000 10000 1 0 0.1325 20

19521601 0 0 0 0 0.1863 5

19521602 0 0 0 0 0.1535 10

19521603 0 0 0 0 0.0818 15

19521604 0 0 0 0 0.1325 20

19521701 10230 0.0332 0 0 20

19521601 0 10. 10. 0. 0. 0. 0. 1. 20

19521901 0 10. 10. 0. 0. 0. 0. 1. 20

**cold leg - ev a prirobnieam~it 5511

• 19551000 2 4 1 1 0.0

* 19551100 0 1

* 19551101 3 0.0279

* 19551201 1 3

* 19551301 1.0 3

* 19551401 597.0 1 588.0 2 570.0 3 561.0 4

• 19551501 955010000 0 1 0 0.6915 1

• 19551502 956010000 0 1 0 0.6915 2

2 19551601 0 0 0 0 0.6915 1

* 19551602 0 0 0 0.6915 2

* 19551701 10230 0.166 0 0 2

* 19551601 0 10. 10. 0. 0. 0. 0. 1. 2

• 19551901 0 10. 10. 0. 0. 0. 0. 1. 2

cold leg - cov a prirobuicami hhll

19551000 10 4 1 1 0.0

19551100 0 1

19551101 3 0.0279

19551201 1 3

19551301 1.0 3

19551401 597.0 1 588.0 2 570.0 3 561.0 4

19551501 955010000 10000 1 0 0.1383 5

19551502 956010000 10000 1 0 0.1383 10

19551601 0 0 0 0 0.1363 5

19551602 0 0 0 0 0.1383 10

19551701 10230 0.0332 0 0 10

19551801 0 10. 10. 0. 0. 0. 0. 1. 10

19551901 0 10. 10. 0. 0. 0. 0. 1. 10

* ddhh3 dh korakcija nekaterih rc83 tlacnih szanaval

.... •.. .*..... t.*e.* **...t**t• ..........

cv 920 t di korigirano tiacnco zasnavalo 902-10 [pal

20592000 pc90202 sun 9.8067 0.0 1

28

20592001 0.0 0.10197 p 902100000 -0.15 rho 902100000 * R.

cv 921 * d.korigiren tiacho zaznavalo S01-06 (pal

20592100 pkS0106 sum 9.8067 0.0 1

20592101 0.0 0.10197 p 501060000 -0.8425 rho 501060000

cv 922 dh korigirano tlacco zazoavalo 952-01 [pal

20592200 pkP5201 sum 9.8067 0.0 1

20592201 0.0 0.10197 p 952010000 -0.15 rho 952010000 * R*

• cv 923 t di korigiranto tlacno zaznavalo 952-10 (pal

20592300 p

1 95202 sum 9.8067 0.0 1

20592301 0.0 0.10197 p 952100000 0.15 rho 952100000 * R+

• cv 924 : dh korigirawo tlacno zaznavalo 954-05 (pal

20592400 pk95401 sum 9.8067 0.0 1

20592401 0.0 0.10197 p 954050000 -0.15 rho 954050000 * R3

•* ccvvii dpmeasured - gravity term - zanka 2

• ta blok cv is uporablian med rca8 dp inicializacilo

upostevam so vae dI. kcoekcijoe lacnih saznaval

• cv 930 1 dp3lh (bar)

-20593000 dp3lb sum 1.0e-05 -0.0763 0 '20593001 0.0 1.0 p 902010000 -1.0 p 903010000 * dh.O.Om

• cv 931 1 dp3lv (bar) '20593100 dp3lv sum 1.00-05 -0.0792 0

"'.20593101 0.0 1.0 p 902020000 -1.0 p 902010000 1.0

cotr•lvar 932

'20593101 0.0 1.0 cntrlvar 920 -1.0 p 902010000 1.0

cotrlvar 932

cv 932 dp3lv gravity term [pal •20593200 dpgt sum 9.8067 0.0 1

'20593201 0.0 1.7317 rho 902010000

*' ev 933 : dp6l (barl

'20593300 dp6l sum 1.0-OS -0.0562 0

•"20593301 0.0 1.0 p 501010000 -1.0 p 902020000 1.0

cntnivar 934

*20593301 0.0 1.0 p 501010000 -1.0 catrlvar 920 1.0

cntrlvar 934

• c 934 dp6l gravity term (pal

'20593400 dpgt sm 9.8067 0.0 1

'20593401 0.0 0.364 rho 902020000

ttcv 93S hot log dp [bar]

"20593500 hlip sum 1.06-05 -0.2117 0

'20593501 0.0 1.0 p 501010000 -1.0 p 903010000 1.0 cntrlvar

936

cv 936 :ldp gravity term (pal

'20593600 dpgt sm 9.8067 0.0 1

t

t

• intermediate leg - cev 8 prirobaicami: hll

19521000 4 4 1 1 0.0

19521100 0 1

19521101 3 0.0226

19521201 1 3

19521301 1.0 3

19521401 597.0 1 588.0 2 570.0 3 561.0 4

19521501 952010000 0 1 0 0.9313 1

19521502 952020000 0 1 0 0.7673 2

19521503 953010000 0 1 0 0.4088 3

19521504 954010000 0 1 0 0.6625 4

19521601 0 0 0 0 0.9313 1
'20593601 0.0 2.0957 rho 902010000

'* CV 937 t dp62x (bar) '20593700 dp62x sum 1.0.-05 -1.1424 0

**20593701 0.0 1.0 p 501060000 -1.0 p 501010000 1.0

cntrlvar 938

*20593701 0.0 1.0 cntrivar 921 -1.0 p S01010000 1.0

cotrivar 935

** cv 935 1 dp62x gravity terM [pa)

'20593800 dpgt am 9.8067 0.0 1

'20593801 0.0 9.2065 rho 501020000

* v 939 - dpa3x (bar]

'20593900 dp63x sue 1.0.-05 -0.9681 0

"-20593901 0.0 1.0 p 513010000 -1.0 p 501060000 1.0

cntrIvar 940 *20593901 0.0 1.0 p 513010000 -1.0 cntrIvar 921 1.0

cntrIvar 940

::CV 940 : dpf3x gravity term (pal

'20594000 dpgt mm 9.0067 0.0 1

'20594001 0.0 -9.2065 rho 501080000

" CV 941 1 stoea gener&tor Op [bar]

'20594100 sgdp smi 1.0.-OS -2.1105 0

'20594101 0.0 1.0 p 513010000 -1.0 p 501010000 * dh-0.00

Cv v 942 : dP64 (bar]

*20594200 dp44 sun 1.0O-05 -0.1801 0

**20594201 0.0 1.0 p 952010000 -1.0 p 513010000 1.0

cntrivar 943

'20594201 0.0 1.0 cntrIvar 922 -1.0 p 513010000 1.0

cntrivar 943

'* cv 943 : dp64 gravity term (pal *20594300 dpgt sue 9.6067 0.0 1

'20594301 0.0 -0.364 rho 952010000

" cv 944 t dp32vg [bar]

'20594400 dp32vg sum 1.0.-OS -0.0576 0

**20594401 0.0 1.0 p 952020000 -1.0 p 952010000 1.0

cntrlvar 945

'20594401 0.0 1.0 cntrIvar 923 -1.0 cntrivar 922 1.0

cntrIvar 945

" cv 945 a dp32vg gravity term [pa)

'20594500 dpgt am 9.8067 0.0 1

"-20594501 0.0 -4.4007 rho 952020000

-' cv 946 a dp32vp [bar] *20594600 dp32vp sum 1.0.-OS -0.0634 0

*"20594601 0.0 1.0 p 954010000 -1.0 p 952020000 1.0

cntrlvar 947

*20594601 0.0 1.0 cntrIvar 924 -1.0 cntrIvar 923 1.0

cntrivar 947

** cv 947 : dp32vp gravity term [pa)

'20594700 dpqt sum 9.8067 0.0 1

*20594701 0.0 1.967 rho 953010000

*' c 946 : internediate leg dp (bar)

'20394800 1dlp sum 1.0.-05 -0.3011 0

**20594801 0.0 1.0 p 954010000 -1.0 p 513010000 1.0

cntrlvar 949

'20594801 0.0 1.0 cntrivar 924 -1.0 p 513010000 1.0

cntrivar 949

" cv 949 ildp gravity term (pal

'20594900 pM siz 9.8067 0.0 1 ,20594901 0.0 -2.797 rho 952020000

*' cvSO adp32p [bar)

'20595000 dp32p sum 1.0.-05 0.0 1

"-20595001 0.0 1.0 p 955010000 -1.0 p 954010000 1.0

cntrivar 951

*20595001 0.0 1.0 p 955010000 -1.0 cntrivar 924 1.0

cntrivar 951

** cv951 : dp32p gravity term [pa)

'20595100 dpgt am 9.0067 0.0 1 *20595101 0.0 0.232 rho 954010000

** cv 952 a dp33h [bar]

*20595200 dp33h sum 1.0Oa05 -0.0303 0

'20595201 0.0 2.0 p 956010000 -1.0 p 955010000 * d0O.Om

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

'20595900 dpOr3 am 1.Oe-OS -0.2700 0

;20595901 0.0 1.0 p 903010000 -1.0 p 141010000 1.0 cntrivar

960

*v c 960 a dpO200 gravity term (pa)

'20596000 dp"t sOU 9.8067 0.0 1

'20596001 0.0 0.714 rho 141010000

' cv 961 a dp3 [bar)

S20596100 dp3 sm 1.0.-05 -2.8840 0

'20596101 0.0 1.0 p 903010000 -1.0 p 956010000 1.0 cntrIvar

962

": c 962 a dp3 gravity term [pal

'20596200 dpgt am 9.8067 0.0 1

-20S96201 0.0 0.29 rho 903010000

sline surge line

*.***.*..........4...............*.............* ..... *.......

** cv 953

'20595300

*20595301

954

* cv 954

'20395400

*20595401

**v 955

'20595500

-20595501

956

" cv 956

'20595600

'20593601

dp052 (bar)

dpOS2 sum 1.Oe-05 -0.5301 0

0.0 1.0 p 119040000 -1.0 p 956010000 1.0 cntrivar

dpOS2 gravity term (pa)

dpgrt sm 9.8067 0.0 1

0.0 -4.498 rho 119030000

a dpO53 (bar)

dpO53 am 1.Oe0OS -0.9551 0

0.0 1.0 p 123010000 -1.0 p 119040000 1.0 cntrlvar

a cpOS3 gravity term (pa)

dpgt sm 9.8067 0.0 1

0.0 -1.503 rho 119050000

2120000 surlin2 pipe

2120001 3

2120101 1.445e-03 3

2120201 1.445e-03 2

2120301 0.6713 3

2120401 0.0 3

2120501 0.0 3

2120601 90.0 3

2120701 0.8713 3

2120801 O.le-03 0.0429 3

2120901 0.12 0.12 2

2121001 00 3

2121101 100000 2

2121201 103 1.55561e+07 6.07063e+02 0.O0000e+00

2121202 103 1.555060+07 6.09028e*02 0.O0000e*00

2121203 103 1.55453et07 6.10258e+02 0.O0000e+00

2121300 0

2121301 -9.16295e-04 -9.24924e-04 0.O0000e÷O0 1

2121302 -9.19462e-04 -9.281490-04 0.00000 00 2

0 0 1 0 0 2

0 0 3

'4 cv 957 a dp0200 (bar)

*20595700 dp0200 sum 1.Oe-05 -1.2043 0

'20595701 0.0 1.0 p 141010000 -1.0 p 123010000 1.0 cnitrIvar

953

'* cv 938 a dp0200 gravity terM (pa)

'20595800 dpgt ms 9.8067 0.0 1

'20S95801 0.0 5.552 rho 131070000

'4 cv 959 a dpOr3 (bar)

29

2220000 jun222 sagljun

2220101 215010000 212000000 0.0 0.12 0.12 130000

2220201 0 -9.11450e-04 -9.11456e-04 0.O0000e+00

2150000 surlinS pipe

2150001 4

2150101 1.445e-03 4

2150201 1.445e-03 3

2130301 0.85 1 2.0793 4

2150401 0.0 4

2150301 0.0 4

2150601 90.0 1 1.0 4

2150701 0.85 1 2.0793 4

2130801 0.1-03 0.0429 4

2150901 0.12 0.12 3

2151001 00 4

2151101 100000 3

2151201 103 1.56035et07 5.78967o.02 0.O00000*00 0 0 1

2131202 103 1.55933e*07 5.840510+02 0.00000*00 0 0 2

2151203 103 1.55792e*07 S.92217e.02 0.00000e00 0 0 3
2151204 203 1.55655e.07 6.00374*.02 0.00000+.00 0 0 4

2151300 0

2151301 -5.677416-04 -2.67743e-04 0.00000e+00 1

2151302 -6.009916-04 -8.60991*-04 0.00000s.00 2

2151303 -6.965686-04 -8.965660-04 0.00000e*00 3

* connection to hot leg 1

2250000 jun225 sngljun

2250101 603010000 215000000 1.445e-03 0.21 0.76 130100

2250201 0 1.10509e-04 1.105086-04 0.00000*00

2031101 100000 9

2031201 102 1.553966+07

2031202 102 1.553285.07

2031203 102 1.55254e.07

2031204 102 1.551950+07

2031205 102 1.55167607

2031206 102 1.551555.07

2031207 102 1.SS1435.07

2031208 102 1.551300+07

2031209 102 1.551185.07

2031210 102 1.55106e+07

0.00000e+00

0.00000e.00

0.000000+00

1.29000e-01

1.000006+00

1.000005+00

1.00000e.00

1.000005+00

1.000006+00

1.000000+00

0.000006.00

0.000000o00

0.00000e.00

0.000000*00

0.O00000e*00

0.000006,00

0.00000+00

0.000006,00

0.00000e+00

0.000000.00

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

h* s surge line wall: hhll

12210000 7 4 2 1 0.02145

12210100 0 1

12210101 3 0.03015

12210201 1 3

12210301 1.0 3

12210401 618.00 4

12210501 215010000 0 1 1 0.6500

12210502 215020000 0 1 1 2.0793

12210503 215030000 0 1 1 2.0793

12210504 215040000 0 1 1 2.0793

12210505 212010000 0 1 1 0.6713

12210506 212020000 0 1 1 0.8713

12210507 212030000 0 1 1 0.8713

12210601 0 0 0 1 0.6500 1

12210602 0 0 0 1 2.0793 2

12210603 0 0 0 1 2.0793 3

12210604 0 0 0 1 2.0793 4

12210605 0 0 0 1 0.5713 5

12210606 0 0 0 1 0.9713 6

12210607 0 0 0 1 0.8713 7

12210701 10233 0.142 0 0 7

12210801 0. 10. 10. 0. 0. 0. 0. 1. 7

12210901 0. 10. 10. 0. 0. 0. 0. 1. 7

1

2

3

4

5

6

7

.......... *....

2031300 0

2031301 1.71838e-07 1.718396-07 0.00000e÷0 1

2031302 -6.74590e-07 -6.745955-07 0.00000+e00 2

2031303 -2.89946e-06 S.462306-01 0.00000e.00 3

2031304 -3.51120-o01 9.20837e-07 0.00000e.00 4

2031305 -5.53443e-02 -1.268185-06 0,O0000eO00 S

2031306 -6.5$7456-02 -2.976426-06 0.00000e.00 6

2031307 -S.54882e-02 -4.61656e-06 0.00000e.00 7

2031308 -4.91295e-02 -6.232506-06 0.00000e.00 8

2031309 -3.94933*-02 -7.81372e-06 0.00000e+00 9

* hhas prz walls hhll

* 12200000 10 4 1 1 0.0

12200000 10 4 1 0 0.0 * ffll

12200100 0 1

12200101 3 0.01609

12200201 1 3

12200301 1.0 3

12200401 597.0 1 588.0 2 570.0 3 S61.0 4

12200501 203010000 0 1 0 0,76115 1

12200502 203020000 0 1 0 0.78115 2

12200503 203030000 0 1 0 0.78115 3

12200504 203040000 0 1 0 0.78115 4

12200505 203050000 0 1 0 0.76115 5

12200506 203060000 0 1 0 0.78115 6

12200507 203070000 0 1 0 0.78115 7

12200508 203080000 0 1 0 0.76115 8

12200509 203090000 0 1 0 0.78115 9

12200510 201100000 0 1 0 0.76115 10

12200601 0 0 0 0 0.78115 1

12200602 0 0 0 0 0.78115 2

12200603 0 0 0 0 0.78115 3

12200604 0 0 0 0 0.78115 4

12200605 0 0 0 0 0.7:115 5

12200606 0 0 0 0 0.78115 6

12200607 0 0 0 0 0.78115 7

12200608 0 0 0 0 0.76115 8

12200609 0 0 0 0 0.76115 9

12200610 0 0 0 0 0.78115 10

12200701 10234 0.1 0 0 10

12200801 0. 10. 10. 0. 0. 0. 0. 1. 10

12200901 0. 10. 10. 0. 0. 0. 0. 1. 10

* hhas prz heaters

12011000 1 4 1 1 0.0

12011100 0 1

12011101 3 0.00465

12011201 1 3

12011301 1.0 3

12011400 0

12011401 619.31 1 619.3 2 619.1 3 618.6 4

12011501 0 0 0 0 0.4852 1

30

12011601 203010000 0 1 0 0.4882 1

12011701 10218 1.0 0.0 0.0 1

12011801 0 10. 10. 0. 0. 0. 0. 1. 1

12011901 0 10. 10. 0. 0. 0. 0. 1. 1

20521600 przpow function 1.0 1400.0 0

20521801 time 0 216

* ccci : grelec deluje 1 mad iniciliLzacijo

20221800 reac-t 0

20221001 -1.0 1400.0

20221802 0.0 1400.0

........... *... **...**.....*.......

* ccwCVt 202 s prz level Inl

20520300 przlev sum 1.0 4.08 1

20520301 0.0 0.9967 voidf 203010000 1.2149 voidf

203020000

20520302 1.2149 voidf 203030000 1.2149 voidf

203040000

20520303 1.2149 voidf 203050000 1.2149 voidf

203060000

20520304 1.2149 voidf 203070000 1.2149 voidf

203080000

20520305 1.2149 voidf 203090000 1.2149 voidf

203100000

.......*.***..............

* ccci fiksirsna tlak in nivo tlacnika

• charging vol

7110000 charg tmdpvol

7110101 1.0 0.0 10.0 0 0 0 0 0 0

7110200 103

7110201 0 1SS.06.05 565.0

* regulacija nivoja

7120000 jun712 tmdpjun

7120101 711000000 215000000 0.0

7120200 1 0 cntrlvar 203

7120201 3.0 2.0 0.0 0.0

7120202 4.08 0.0 0.0 0.0

7120203 5.0 -2.0 0.0 0.0

2320000 1un232 sngljun

2320101 231000000 203010000 0.0 0.0 0.0 130000

2320201 0 3.565796-02 9.365046-06 0.000041e00

* umetai tlacnik

2310000 uprz td1pvo

2310101 1.0 0.0 10.0 0. 0. 0. 0 0 0

2310200 102

2310201 0.0 155.16.05 1.0

*pprrzz tlacnik

................. *............ .......

2210000 jun221 sngljun

2210101 212010000 203000000 0.0 0.91 0.034 130100

2210201 0 -9.232606-04 -9.257686-04 0.000000,00

2030000 przpipe pipe

2030001 10

2030101 0.0 10

2030201 0.0 9

2030301 0.99670 1 1.21490 10

2030401 0.03005 1 0.04194 10

2030501 0.0 10

2010601 90.0 10

2030701 0.99670 1 1.2149 10

2030801 0.16-03 0.0 10

2030901 0.0 0.0 9

2031001 00 10
*llpp l.p.s.i. in akumulatorji

* trip 659 : odpre akumulatorja 2 in 3

* trip 658 : zapre akumulatoria 2 in 3

. trip 522 ; vkljuci lpsi crpalki

* accumulator vessel2

8330000 accumu2 accum

8330101 0.0 8.358 0.423 0.0 90.0 8.358 3.96-5 0.0 O00

8330200 41.8.5 290. 0.0

* zeta iztoka Je 0.335, zeta kolena je 0.2, upostevamo 5 kolen

8331101 805000000 0.00114 1.335 1.335 000000

8332200 0.286 0.0 0.119 0.119 0.00927 0 0 0

* accumulator no 2 pipe

8050000 accul2 engivol

8050101 0.0 21. 0.0239 0.0 20.0 10.005 1.0-4 0.0

00

8050200 3 4.23739e-06 2.90000e.02

* accumulator no 2 valve

8060000 sccvl2 valve

* zeta kolena je 0.2. upoetevemo 5 kolen od 10

8060101 805010000 856000000 0.00114 1.0 1.0 100000

8060201 0 0.O0000.00 0.O0000O.00 0.O0000Os00

*8060300 mtrvlv

*8060301 659 658 5.0 0.0

9060300 trpvlv

8060301 659

* accumulator vessel3

9330000 accumu3 accum

9330101 0.0 8.358 0.423 0.0 90.0 8.358 3.96-5 0.0

00

9330200 41.8÷5 290. 0.0

* zeta iztoka je 0.335, zeta kolena je 0.2, upostevamo 4 kolena

* od 8

9331101 905000000 0.00114 1.335 1.335 000000

9332200 0.286 0.0 0.119 0.119 0.00927 0 0 0

* accumulator no 3 pipe

9050000 accul3 englvol

9050101 0.0 21. 0.0239 0.0 20.0 10.005 1.0-4 0.0

00

9050200 3 4.23739&.06 2.90000e+02

* accumulator no 2 valve

9060000 accvl2 valve

* zeta kolena Je 0.2 upostevamo 4 kolena od 8

9060101 905010000 956000000 0.00114 0.80 0.80 100000

9060201 0 0.O0000e+00 0.O0000e00 0.O0000e÷00

*9060300 mtrvlv

*9060301 659 658 S.0 0.0

9060300 trpvlv

9060301 659

* lpis pump no 2

6070000 lpie2 tmdpjun

8070101 804000000 855010000 0.00599

8070200 1 0 cntrlvar 807

6070201 0,0 0.0 0.0 0.0

8070202 0.67787+5 3.88941 0.0 0.0

8070203 1.5411.5 1.78996 0.0 0.0

8070204 3.8507.5 1.49164 0.0 0.0

8070205 6.767+5 0.99442 0.0 0.0

8070206 8.517+5 0.49721 0.0 0.0

8070207 9.077.S 0.09944 0.0 0.0

8070208 9.100+5 0.0 0.0 0.0

* hpis tank no 2 - rvet2

8040000 rwst2 tmdpvol

8040101 0.0 6.1 28.32 0.0 90.0 6.1

8040200 013

8040201 0.0 1.02+5 307. 0.0

* lpis pump no 3

9070000 lpie3 tsdpjun

9070101 904000000 955010000 0.00599

9070200 1 0 cntrlvar 907

9070201 0.0 0.0 0.0 0.0

9070202 0.67787+5 1.86941 0.0 0.0

9070203 1.5411+5 1.78996 0.0 0.0

9070204 3.8507+5 1.49164 0.0 0.0

9070205 6.767+5 0.99442 0.0 0.0

9070206 8.517+5 0.49721 0.0 0.0

9070207 9.077+5 0.09944 0.0 0.0

9070208 9.100+5 0.0 0.0 0.0

* hpis tank no 3 - rwst3

9040000 rwet3 tmdpvol

9040101 0.0 6.1 28.32 0.0 90.0 6.1

9040200 013

9040201 0.0 1.02+5 307. 0.0

1.0-4 0.0 0

1.0-4 0.0 0

20532101 rho 308010000 cntrlvar 320

* cv 322 : ztsgl wide range sgl level (ml

20532200 ztsgl sum 1.0 0.0 1

20532201 11.255 1.0 cntrivar 321 *

• atw pump no 1, before ultimate procedure

3700000 afvli tmdpjun

3700101 368000000 332000000 0.0006786

3700200 1 626 cntrlvar 322

3700201 -1.0 0.0 0.0 0.0

3700202 0.0 0.30329 0.0 0.0

3700203 13.32 0.30329 0.0 0.0

3700204 13.4 0.24263 0.0 0.0

3700205 13.5 0.16726 0.0 0.0

3700206 13.6 0.09169 0.0 0.0

3700207 13.7 0.01611 0.0 0.0

3700208 13.71 0.00855 0.0 0.0

3700209 13.715 0.00477 0.0 0.0

3700210 13.72 0.0 0.0 0.0

* eaV pump no 1, after ultimate procedure

3710000 afclii tmdpjun

3710101 369000000 332000000 0.0006786

3710200 1 526 cntrlvar 322

3710201 -1.0 0.0 0.0 0.0

3710202 0.0 0.30329 0.0 0.0

3710203 13.14 0.30329 0.0 0.0

3710204 13.20 0.24263 0.0 0.0

3710205 13.25 0.16726 0.0 0.0

3710206 13.30 0.09169 0.0 0.0

3710207 13.325 0.01611 0.0 0.0

3710208 13.34 0.00855 0.0 0.0

3710209 13.35 0.00477 0.0 0.0

• steam dump no 1, after ultimate procedure

3720000 edumpl twApjun

3720101 320010000 367000000 0.00216475

3720200 1 526 p 310020000

3720201 -1.0 0.0 0.0 0.0

3720202 -0.5 0.0 0.0 0.0

3720203 0.0 0.0 0.0 0.0

3720204 1.÷5 0.0078 0.0 0.0

3720205 70.+5 0.546 0.0 0.0

3720206 100.+S 0.78 0.0 0.0

* eteam dump no 1

3670000 sdumpl tmdpvol

3670101 0.0 6.1 28.32 0.0 90.0 6.1 1.0-4 0.0 0

3670200 003

3670201 0.0 1.02+5 507.

* Efw tank-i no 1

3680000 afvtli tmdpvol

3680101 0.0 6.1 28.32 0.0 90.0 6.1 1.0-4 0.0 0

3680200 003

3680201 0.0 1.02+5 307.

* afv tank-ii no 1

3690000 afwtlii tsdpvol

3690101 0.0 6.1 28.32 0.0 90.0 6.1 1.0-4 0.0 0

3690200 003

3690201 0.0 1.02+5 307.

****,******* ...................... ................... ttt•

• filter: crpalka ne dela sunkovito.

" razmearje faktorjev 0.3.0.7.1.0 je lahko drugacno.

* Ctv 907: cold leg - rest delta pressure (filtered)

20590700 clrcetd3 sum 1.0 151.0+S 0

20590701 0.0 -0.3 p 904010000 0.3 p 955010000 0.7 cntrlvar

907

* ctv 807: cold leg - rwat delta pressure (filtered)

20580700 clrvetd2 sum 1.0 151.0.5 0

20580701 0.0 -0.3 p 804010000 0.3 p 855010000 0.7 cntrlvar

807

* aaffw poaozno napajanje in steam dump

* cv 320 : dplr2 dp 8g9 nr level [pal

* 0.0197 - 1/9.8067

20832000 dplr2 sum 1.0 0.0 1

20532001 0.0 0.10197 p 308010000 -0.10197 p 310010000

20532002 0.121 rho 308010000 0.440 rho 310010000

* cv 321 : ztlr2 narrow range sgl level (m]

20532100 zt3r2 div 1.0 0.0 1

31
• cv420 . dp2r2 dp Sg2 or level (pa)

0.0197 - 1/9.0067

20542000 dp2r2 sum 1.0 0.0 1

20542001 0.0 0.10197 p 408010000 -0.10197 p 410010000

20542002 0.121 rho 406010000 0.440 rbo 410010000

: ev 421 t zt2r2 narrow range s92 level to)

20542100 st2r2 div 1.0 0.0 1

20542101 rho 406010000 cntrlvar 420

• Cv 422 1 ztsg2 wide range ag2 level [a]

20542200 ztsg2 sm 1.0 0.0 1

20542201 11.285 1.0 cstrlvar 421 *.+

Ssfw pump no 2, before ultimate procedure

4700000 afw2i tmdpjUn

4700101 466000000 432000000 0.0006786

4700200 1 626 cntrlvar 422

4700201 -1.0 0.0 0.0 0.0

4700202 0.0 0.30329 0.0 0.0

4700203 13.32 0.30329 0.0 0.0

4700204 13.4 0.24263 0.0 0.0

4700205 13.5 0.16726 0.0 0.0

4700206 23.6 0.09169 0.0 0.0

4700207 13.7 0.0161& 0.0 0.0

4700208 13.71 0.00855 0.0 0.0

4700209 13.715 0.00477 0.0 0.0

4700210 13.72 0.0 0.0 0.0

Safwv p• no 2, after ultimate procedure

4710000 afw2Ii tedpjun

4710101 469000000 432000000 0.0006766

4710200 1 526 cotrivar 422

4710201 -1.0 0.0 0.0 0.0

4710202 0.0 0.30329 0.0 0.0

4710203 13.14 0.30329 0.0 0.0

4710204 13.20 0.24263 0.0 0.0

4710205 13.25 0.16726 0.0 0.0

4710206 13.30 0.09169 0.0 0.0

4710207 13.325 0.01611 0.0 0.0

4710206 13.34 0.00855 0.0 0.0

4710209 13.35 0.00477 0.0 0.0

• steam dump no 2, after ultimate procedure

4720000 adump2 tmdpjun

4720101 420010000 467000000 0.00216475

4720200 1 526 p 410020000

4720201 -1.0 0.0 0.0 0.0

4720202 -0.5 0.0 0.0 0.0

4720203 0.0 0.0 0.0 0.0

4720204 1..S 0.0076 0.0 0.0

4720205 70..5 0.546 0.0 0.0

4720206 100.45 0.78 0.0 0.0

• afw tank-ii no 2

4690000 &fWt2ii tMdgVol

4690101 0.0 6.1 28.32 0.0 90.0 6.1 1.0-4 0.0 0

4690200 003

4690201 0.0 1.02+5 307.

..............................................................•

• cv 520 dp3r2 dp ag3 nr level (pal

• 0.0197 - 1/9.6067

20552000 dp3r2 mm 1.0 0.0 1

20552001 0.0 0.10197 p 506010000 -0.10197 p 510010000

20552002 0.121 rho 508010000 0.440 rho 510010000

• cv 521 zt3r2 narrow range 893 level 1m1

20552100 zt3r2 div 1.0 0.0 1

20552101 rho 508010000 cntrlvar 520

• CV 522 ztsg3 wide range sg3 level tm]

20552200 ztsg3 mm 1.0 0.0 1

20552201 11.255 1.0 cntrlvsr 521 •.+

a fvw pump no 3. before ultimate procedure

5700000 af31 tedpjun

5700101 566000000 532000000 0.0006796

5700200 1 626 cntrlvar 522

5700201 -1.0 0.0 0.0 0.0

5700202 0.0 0.30329 0.0 0.0

5700203 13.32 0.30329 0.0 0.0

5700204 13.4 0.24263 0.0 0.0

5700205 13.5 0.16726 0.0 0.0

5700206 13.6 0.09169 0.0 0.0

5700207 13.7 0.01611 0.0 0.0

5700208 13.71 0.00855 0.0 0.0

5700209 13.715 0.00477 0.0 0.0

5700210 13.72 0.0 0.0 0.0

• af pump no 3. after ultimate procedure

5710000 afw3ii tedpJun

5710101 569000000 532000000 0.0006766

5710200 1 526 cutrIvar 522

5710201 -1.0 0.0 0.0 0.0

5710202 0.0 0.30329 0.0 0.0

5710203 13.14 0.30329 0.0 0.0

5710204 13.20 0.24263 0.0 0.0

5710205 13.25 0.16726 0.0 0.0

5710206 213.30 0.09169 0.0 0.0

5710207 13.325 0.01611 0.0 0.0

5710208 13.34 0.00655 0.0 0.0

5710209 13.35 0.00477 0.0 0,0

Sstem dump no 3. after ultimate procedure

5720000 aduap3 tmdpun

5720101 520010000 567000000 0.00216475

5720200 1 526 p 510020000

5720201 -1.0 0.0 0.0 0.0

5720202 -0.5 0.0 0.0 0.0

5720203 0.0 0.0 0.0 0.0

5720204 1..5 0.0076 0.0 0.0

5720205 70.+5 0.546 0.0 0.0

5720206 100.-5 0.76 0.0 0.0

& steam dump no 3

5670000 Sdhmp3 tmdpvol

5670101 0.0 6.1 28.32 0.0 90.0 6.1 1.0-4 0.0 0 5670200 003

5670201 0.0 1.02+5 507.

• afv tank-i no 3

5660000 atwt3i tmdpvol

5660101 0.0 6.2 28.32 0.0 90.0 6.1 1.0-4 0.0 0

5660200 003

5680201 0.0 1.02+5 307.

a te tank-Li no 3

5690000 afwt3ii tmdpvol

5690101 0.0 6.1 28.32 0.0 90.0 6.1 1.0-4 0.0 0

5690200 003

5690201 0.0 1.02+5 307.

*Z11 gllo : cl1

1600000 break sngljun

1800101 655010000 162000000 2.09117e-05 4. 4. 130102

0.92 0.92

1600110 .00516 0.0 1.0 1.0

1800301 0 -5.43513e-07 -5.43513e-07 0.00000•00

1.20000 bline snglvol

1820101 1.6619-3 10.0 0.0 0.0 0.0 0.0 1.0e-04 0.0 00

1620200 3 1.S6753e•07 5.331120•02

1830000 bvent valve

1830101 162010000 186000000 1.65e-03 0.0 0.0 100100

1830201 0 0.O00000.00 0.O0000e•00 0.O0000e+00

1630300 mtrvlv

1630301 S01 603 20. 0.0

1960000 tank tmlpvol

18"0101 1.0 0.0 5.02 0.0 0.0 0.0 1.00-04 0.0 00

1:60200 2

1860201 0.0 l.O.05 1.0

• ccvvhbll toplotne izgube

.++ t okolice - 25 c

cV 220, lower plenum beat losses

20522000 iphi function 1.0 0.0 1 3 -4900.0 0.0

20522001 tempf 123010000 220

20222000 reac-t 670

20222001 -1.0 0.0

20222002 298.0 0.0

20222003 560.0 -4900.0

steam dump no 2

4670000 sduMp2 tmdpvol

4670101 0.0 6.1 28.32 0.0 90.0 6.1

4670200 003

4670201 0.0 1.02+S 507.

t a, tank-i no 2

4660000 afwt21 t•dpvol

4600101 0.0 6.1 28.32 0.0 90.0 6.1

4660200 003

4660201 0.0 1.02•5 307.

1.0-4 0.0 0

1.0-4 0.0 0

32
* cv 221: core bypass heat losses

20522100 cobyhl function 1.0 0.0 1 3 -4S76.0 0.0

20522101 tempt 133010000 221

20222100 reac-t 670

20222101 -1.0 0.0

20222102 290.0 0.0

20222103 560.0 -4576.0

* cv 222: upper plenum . upper head heat losses

20522200 uphhl function 1.0 0.0 1 3 -6292.0 0.0

20522201 temfp 153010000 222

20222200 reac-t 670

20222201 -1.0 0.0

20222202 298.0 0.0

20222203 560.0 -6292.0

* cv 223: reactor downcaer heat losses

20522300 dm01l function 1.0 0.0 1 3 -6032.0 0.0

20522301 tempt 119040000 223

20222300 reac-t 670

20222301 -1.0 0.0

20222302 296.0 0.0

20222303 560.0 -6032.0

* cv 224: cold leg 1 heat losses

20522400 cllhl function 1.0 0.0 1 3 -5356.0 0.0

20522401 tempt 653010000 224

20222400 reac-t 670

20222401 -1.0 0.0

20222402 298,0 0.0

20222403 560.0 -5356.0

20522801

* cv 229:

20522900

20522901

* cv 230:

20523000

20523001

* cv 231.

20523100

20523101

* c• 232:

20523200

20523201

* cv 233:

20523300

20523301

20223300

20223301

20223302

20223303

• cv 234:

20523400

20523401

20223400

20223401

20223402

20223403

* cv235:

20523500

20523501

222

20523502

22S

20523503

228

20523504

231

20523S05

234

20523506

tempt 403020000 225

hot leg 2 heat losses

hl2hl function 1.0 0.0 1 3 -2704.0 0.0

tempt 856010000 226

cold leg 3 beat losses

cl3hl function 1.0 0.0 1 3 -5356.0 0.0

tempf 953010000 224

steam generator 3 heat losses

sg3hl function 1.0 0.0 1 3 -10096.0 0.0

tempf 503020000 225

hot leg 3 heat losses

hl3hl function 1.0 0.0 1 3 -2704.0 0.0

tempt 956010000 226

surge line heat losses

SihI function 1.0 0.0 1 3 -3560.0 0.0

tempf 215010000 233

reac-t 670

-1.0 0.0

298.0 0.0

568.0 -3560.0

pressurizer heat losses

przhl function 1.0 0.0 1 3 -4000.0 0.0

tempf 203020000 234

reac-t 670

-1.0 0.0

298.0 0.0

610.0 -4000.0

20100100 tbl/fctn 1 -i • stainless steel

20100200 tbl/fctn 2 2 • boron nitride (heater rods)

20100300 tbl/fctn 1 -1 • inconel 600

* thermal conductivity data

* stainless steel

20100101 293. 13.9: 373. 15.1. 473. 16.7, 573. 18.3, 673.

19.6. 673. 23.0,

20100102 1073. 26.1

* boron nitride

• 20100201 473, 1073. 2. 0. 0. 0. 0. 0. 0.

20100201 293. 1073. 2. 0. 0. 0. 0. 0. 0.

* inconel 600

20100301 293. 14.9. 373. 15.6, 473. 17.2, 673. 20.4, $73.

23.7, 1073. 27.4

* volumetric heat capacity data

• stainless steel

20100151 3.S7870+6, 3.06776+6, 4.09766.6, 4.20898+6,

4.26474+6, 4.41405.6,

20100152 4.65555+6

• boron nitride

• 20100251 473. 1073. 1.46.6 1.62-3 0. 0. 0. 0. 0.

20100251 293. 1073. 1.46+6 1.62+3 0. 0. 0. 0. 0.

* inconel 600

20100351 3.76320+6, 3.85526+6, 4.02919+6, 4.26422+6,

4.66003.6, 4.98467+6

*.. .*................. 

* comparison report dodatki

20516000 avgrhof sum 0.0633 0.0 1

20516001 0.0 1.0 rhof 131010000 1.0 rhof 131020000 1.0 rhof

131030000

20516002 1.0 rhof 131040000 1.0 rhof 131050000 1.0 rhof

131060000

20516003 1.0 hnot 131070000 1.0 rhof 131060000 1.0 rhof

131090000

20516004 1.0 rhof 131100000 1.0 rhof 131110000 1.0 nhof

131120000

20516100 clevl sum 1.0 0.0 1 • 101.94 . 1000*1/9.81

tipA--.pAI

20516101 0.0 101.94 cntrlvar 240 -5.61 rhog 131060000

20516200 clev2 sum 1.0 0.01 1

20516201 0.0 1.0 contrlvar 160 -1.0 rhog 131060000

* ctv 163: collapsed liquid core level (m)

20516300 corelevl div 1.0 0. 1 3 0.0 9.5

20516301 cntrlvsr 162 contrlver 161

. ......................... 

* ctv 146: maxima httemp rx core, right-wall surface

20514600 msxrxt stdfnctn 1.0 600. 1

20514601 max httemp 131000106 httemp 131000206

20514602 httemp 131000306 httee 131000406

20514603 httemp 131000506 httemp 131000606

20514604 httemp 131000706 httemp 131000606

* cv 225:

20522500

20522501

20222500

20222501

20222502

20222503

*cv 226:

20522600

20522601

20222600

20222601

20222602

20222603

steam generator 1 heat losses

sglhl function 1.0 0.0 1 3 -18096.0 0.0

tempt 303020000 225

reac-t 670

-1.0 0.0

296.0 0.0

555.0 -18096.0

hot leg 1 heat losses

hllhl function 1.0 0.0 1 3 -2704.0 0.0

tempf 656010000 226

reac-t 670

-1.0 0.0

296.0 0.0

564.0 -2704.0

system heat losses

sumhl sum 1.0 0.0

0.0 1.0 cntrlvar 220

1.0 cntrlvar 223

1.0 cntrlvar 226

1.0 cntrlvar 229

1.0 cntrlvar 232

3.0 cntrlvar 701

1

1.0 cntrlvar 221

1.0 cntrlvar 224

1.0 cntrlvar 227

1.0 cntrlvar 230

1.0 cntrlvar 233

1.0 cntrlvar

1.0 cntrivar

1.0 cntrlvar

1.0 cntrlvar

1.0 cntrlvar

. . ............... ... 

: MOs beat structure thermal property data

* cv 227: cold leg 2 heat losses

20522700 cl2hl function 1.0 0.0 1 3 -5356.0 0.0

20522701 tempt 653010000 224

* cv 228: steam generator 2 heat losses

20522800 sg2hl function 1.0 0.0 1 3 -18096.0 0.0

........................ * *.•* * ........... • e * ..

* composition type and data format

33
20S1460S httee 2fil0600•0 httewp 131001006

20514606 httemp 31000906 httesp 131001206

zacetno stanje: mcp(0) + msm2(0) * mm3(0)

- 1949 KG * 206K 0 286 KG . 2521 KG

20517000 mtp sum,1.0 1949.0 0

20517001 2521.0 -1.0 cntrlvar 271 -1.0 cntrlvar 275

20517002 -1.0 cntrlvar 276 #1.0 cntrlvar 274

.tt*............*...*............tt . ........... *....t...... **

end ***

34
Appendix A - Listing of the middle BETSY nodalization - restart input

- bethey - bethm3lhl.dat restart (100 - 8630.0 eec) * comparison report sahteva dodatne cv

* spuscena spodnja maja s. lastnosti ta borov nitrid

* v post-test preracunu (november 91 -- )t

* odprava separatorjev

* abrupt-normal zlom

* reasirjena tabela topi prey. za material 1 (brez

eketrapolacije)

• koncni spoj-zlom iz btestm3n2.dat (junij 1993)

* niso upostevane tudi nbam3l.dat spremeebe (ae ismam npr

mtrvlv 183)

• zIom v 300. seokundi

• .. opozorilo I

100 restart transnt

103 8000

201 1450.0 1.0-6 0.02 3 500 25000 25000

202 1700.0 1.0-6 0.005 3 2000 40000 40000

203 8630.0 1.0-6 0.02 3 500 25000 25000

* 202 2800.0 1.0-6 0.04 3 500 25000 25000

* 202 1400.0 1.0-6 0.04 3 500 25000 25000

asome requested minor edit

'311 cntrlvar 244

diT. p. ((pa)

'312 cntrlvar 245

press. (kpa)

'313 cntrlvar 246

(kpa]

'314 cntrivar 247

(kpa]

'315 cntrlvar 248

diff. p. (kp*)

*316 cntrlvar 249

side diff. p. (cpa)

•317 cntrlvar 250

[kpa)

'318 cntrivar 251 (kpa'

3129 cntrlvar 252

diff. p. [kpa)

!320 cutrlvar 253

side diff. p. (kpal

'321 cntrlVar 254

[k(pa

'322 cntrlvar 255

(kpa]

*323 cntrlvar 256

diff. p. (kpa)

'324 ontrlvar 257

side diff. p. (kpa)

'325 cntrlvar 258

outlet diff. p. (kpa)

'326 cntrivar 259

press. [kpae

'327 cntrlvar 260

diff. p. (kpa)

'328 cntrlvar 261

diff. press. (kpa)

*329 cntrlvar 262

outlet diff. p. [kpa)

'330 cntrlvar 263

press. (klpa

'331 cntrlvar 264

ditt, p. (cpa)

'332 entrivar 265

diff. press. lkpa)

'333 cntrlvar 266

Cutlet diff. p. (kpa)

'334 antrlvar 267

press. ((cpa)

*335 cntrlvsr 268

diff. p. (kpal

'336 centrvar 265

diff. press. (kpa]

-337 cntrivar 270

press. (kpa) '..

• dpO50 downcomuer to upp. head

* dpOrl pressure vessel dif.

* dpi

* dpl2pg

* dpl2vg

* dpl2vp

•'#2

* dp22pg

" dp22vg

" dp22vp

' dp3

• dp32pg

* dp32vg

* dp32vp

"dp4l

' dp426

" dp4r2

* dpS

' dpSl

" dp526

• dpSr2

* dP6

' dp6l

" dp426

" dp6r2

cll to hll diff. press.

pump 1 diff. press.

loop seal 1 downf, side

loop seal 1 upflov.

c12 to h12 diff. press.

pump 2 diff. press.

loop seal 2 downf, side

± loop seal 2 upflow.

: c13 to h13 diff. press.

pump 3 diff. press.

loop seal 3 dowen. side

loop seal 3 upflow.

sgl u-tube in. to

sgl inlet plenum diff.

sgl u-tube upflow side

sgl boiler section

sg2 u-tube in. to

sg2 inlet plenum diff.

* ag2 u-tube upflow side

sg2 boiler section

s sg3 u-tube in. to

* sg3 inlet plenum diff.

sg3 u-tube upflow side

sg3 boiler section

'338 cntrlvar 271

mass flow (kg)

*339 cntrlvar 274

mass flow (kg)

*340 cntrlvar 305

invet. (kg]

'341 cntrlvar 405

invet. (kg)

'342 entrlver 505

invet. (kg)

'343 entrIvar 275

invetory (kg)

'344 cntrlvar 276

invetory (kg)

'345 ontrlvar 277

(epa)

*346 entrlvar 278

,=pal

'347 cntrlvar 279

(epa)

'348 cntrlvar 280

pressure ina"]

' 349 ontrlvar 281

pressure (]al

'350 cntrlvar 282

pressure trpa]

'351 mflowj 123010000

rate (kg/s)

'352 mtlowj 332010000

rate ((kg/s

'353 mflowj 432010000

rate (kg/se

'354 mflowj 532010000

rate [kg/s)

'355 mtlowj 180000000

[kg/s)

'356 mflowj 311000000

flow rate (kg/s)

-357 mflowj 411000000

flow rete (kg/s]

*358 etlow0 511000000

flow rate [kg/s]

'359 mflowi 807000000

rate (kg/s)

'360 mflouj 907000000

rate [kg/fs)

;361 cntrlvar 283

[kj/kg]

'362 tempf 123010000

(k]

'363 tempf 141010000

(k]

'364 tempf 151010000

temperature (k]

*365 tempf 153010000

temperature (k)

'366 tempf 602010000

(k)

• intqmb

* intqmsi

' mgvl

* mgv2

* mgvi

'mea2

• p*47

* p' 5 7

* p'.67?

' pep

* p*aa2

* p*8a3

* qeO5

* qesnt3l

* qmani2

* qmanii

* qagyll

' qmagvl2

* qmgvli

* qumb12

•qmbli1

time integrated break

time integrated lpsi

sgl secondary side mass

sg2 secondary side mass

sg3 secondary side mass

accumulator 2 sass

accumulator 3 mass

sgl steam dam pressure

sg2 steam dome pressure

sg3 steam dame pressure

pressurizer top

accumulator 2 gas phase

accumulator 3 gas phase

downcomer mass flow

egl feedwster mass flow

sg2 feedwater mass flow

sg3 feedwater sass flow

break sass flow rate

sgl steam line mass

sg2 steam line mass

sg3 steam line mass

1psi in c12 mass flow

lpsi in c13 mass flow

'301 voidg 60301000

fraction 1

'302 voidg 65601001

fraction 1

*303 voidg 8030100(

fraction I

'304 voidg 85601003

fraction

'305 voidg 90301001

fraction

'306 voidg 95601004

fraction

*** dp - p(low press.

'307 ontrivar 240

press. [kpa)

*308 entrlvar 241

press. (kpa]

'309 cntrlvar 242

(kpal

'310 cntrlvar 243

I(pa)

0

0

0

0

0

0

0 • albcl: hil spool piece void

00 * albfl: ll spool piece void

(0 ' albc21 h12 spool piece void

(0 * albf2:sc12 spool piece void

O0 ' albc3: hi) spool piece void

30 * albfit c13 pool piece void

tap) - p(high press. tap)

" dp0200 i core heat. length diff.

" dpupl i upper plenum diff.

* dp034 guide tube dir. press.

* dpuhead upper head df. press.

* sebreak b break specific enthalpy

* tfOl2a

* tf0304

* tf041

" tf042

Sttf112

core inlet temperature

cOre outlet temperature

upper head (bottom)

* upper head (top)

hot leg I temperature

- dppl : pressurizer diff.

I
*147 tempt 558010000 (k)

e364 tempf 802010000

(k]

*369 tempf 555010000

(k)

*370 tompf 902010000

(k)

*371 tompf 955010000

(k) .

"372 tempt 3090S0000

temperature (k)

*373 tempf 409050000

temperature (k)

-374 tempf 509050000

temerature (k]

:375 httemp 131000701

*376 httemp 131000801

•377 httemp 131000901

middle to

-376 httemp 131001001

*379 httemp 131001101

tab.1 str.28/87)

*360 httemp 131001201

381 CntrIvar 146

(k)

;162 cntrivar 286

*383 cntrlvar 287

(rpm

*354 cutrivar 268S

: 38S cativa 289

*386 cntrlvar 290

'357 entrlva* 110

*388 cntrlvar 291

*199 dt 0

transient (i) *390 amas 0

*tf2li

*tf233

*tf312

*t9333

*tf4S4c

t cold Leg I temperature

hot leg 2 temperature

cold leg 2 temperature

hot leg 3 temperature

cold leg 3 temperature

s bottm of t9g dovncmr

* ttSS4c bottom of ag2 dowacomer

* tf6S4c : bottom of sg3 dovncomer

" t802091 I * t802181 :

* t&02191 : rod temperature from

t802201 top core elevation (k)

t802241 *..+* to - 7 (I Omemb& v

ta0d281 d :ma ma. clad temperature

vP1

VP2

VP3

w+02

w~troc

zt2OO0

zecors

pump 1 rotation speed

pump 2 rotation apeed

pump 3 rotation speed

core (electrical) power

trace heating Dkvi

s core level to]

siollen level SI]

* comparison report variables request

301 catrlvar 280 * p+p PRESSURIZER TOP PRESSURE

ImpAI

302 cntrlvar 278 * p÷S7 a eg2 STEAK DONE PRE SURE

IMPA)

303 cntrlvar 163 * zt0200 CORE COLOAPS• D LIQUID LEVEL [N)

304 tempg 131120000 * tf03046 CORE OUTLET STEAM

TEMPERATURS IkI

305 cntrlvar 146 . tma MAX. CLAD MALLI

TASMEATURE (k)

306 voidg 655070000 * aibfti cl1 SPOOL PIROc VOID

FRACTION I I I*

307 mtlovj 180000000 - qmb BEAK MASS FLOW RATE (KG/B)

308 cntrlvar 405 * mi : ig2 SECONDARY SIDE MAS

INV•T. (KG)

309 cotrlvar 170 * mcp PRIMARY MASS INVETORY

310 entrivar 371 * intqmb t BEA DISCHARGED MASS

[KG)

313 cntrlvar 110 * ztO200 : SIMPL. CORE COLLAPSED

LIQUID LEZvE (N)

317 cntrlvar 240 * dp0200 CORE BRAT. LENGTH DIFF.

PRESS. [EpA]

318 cntrlvar 241 * dpupi UPPER PLEMNM DIFF.

PRSs. (EPAI

319 cntrlvar 242 * dp034 GUIDE TOUE DIV. PES8.

(EpA)

320 cntrIvar 243 * dpusad: UPPER BEAD DIV. PRESS.

321 cntrlvar 244 * dPOSO DOWMNNC0(ER TO UPP. READ

DIV. P. (A)

322 cntrlvar 245 * dporl PRESSURE VESSEL DIV.

PRESS. (SpA)

323 cntrlvar 246 * dpl cll TO hil DIV?. PRESS.

EXPA)

324 cntrlvar 247 * dpl2pg pump I DIFF. PRESS.

(KpA)

328 Cntrlvar 248 * dp12v : LOOP SSEA 1 DOWNF. SIDE

DIPF. P. (EPA)

326 c¢trlvar 249 * dpl2vp LOOP SEAL 1 UPFLOW. BIDE

01FF. P. (EPA)

327 cntrlvar 250 * dp : c12 TO h12 DIFF. PRESS.

326 cntrlvar 251 * dp22pg pump 2 DIFF. PRESS.

329 cntrlvsr 252 * dp22vg LOOP SEAL 2 DOm. SIDE

DIFF. P. (EpA]

330 ontrivar 253 * dp22iv LOOP SEAL 2 UPLOW. SIDE

DIFF. P. [EA

333 cntrlvar 256 DIFF. P. [rpA

334 cntrlvar 257

DIFF. P. [(pA)

33S cntrlvar 255

DIFF. P. (IpAi

336 cntrlvar 259

PRESS. (EpAl

337 cntrivar 260

DIFF. P. (WA)

33S cotrivar 261

PRESS. (W]A

339 cntrlvar 262

DIFF. P. (KpA)

340 catrlvar 263

PRESS. (WpA]

341 Ontrlvar 264

DIFF. P. (EWA)

342 cntrlvar 265

PuRS. EpAI]

343 cntrlvar 266

DIFF. P. (EV]A

344 cntrlvar 267

PRESS. (EpA)

345 cntrlvar 26S

DIFF. P. [WA

346 catrIvar 269

PSS. (EpA)

347 cntrlvar 270

[EPA) *++

348 ontrlvar 271

MASS FLOW[MKG)

349 cntrlvar 274

MASS FLOW IKG)

350 cntrlvar 305.

ISMT. (KG)

351 cntrlvar 405

I•VE. [sK]

353 catrlvar S0S

INVET. (in)

353 cantrlvar 275

INV•MOY ([K

354 cntrlvar 276

IBVETORY (KG)

355 c¢trlvar 277

356 cntrlvar 276

ImpA)

357 ontrIvar 279

mpAR)

355 cntrlvar 280

359 cntrlvar 281

PRESSURE EmpA) 360 Cntrivar 282

PRESSURE [spA]

361 mflowj 223010000

[KG/SI

• dp32v : LOOP SL 3 DOWN?. SIDE

" dp32vp LOOP SEAL 3 UPPLOW. SIDE

* dp4l

" dP4i6

* dp4r2

" dps

" dpSl

" dpS26

* dpsr2

*dp6l

*dp426

*dp6r2

gif u-tUnE IN. TO 0(7102

:gl INLET PUMEM DIFF.

8gl u-tUSE UPPLOW SIDE

egl BROILE SECTION DIFF.

g92 u-tU92 IN. TO OUTLET

i sg2 INLET PLEUEM DIFF.

ag2 u-tUBE UPPLOW SIDE

si2 BOILSR SECTION DIFF.

:g3 u-tU2E IN. TO OUTLET

sg3 INLET PLENM DIFF.

sg3 u-tU9E UPFL40W SIDE

SIa3 BOILS SECTION DIFF.

* dppl P ESSURISRA DIFF. PRESS.

* dtcalc i time step along

* r : mass error (kg)

* intqmb

* mgvl

* mgv2

* mgv3 •WV2

* p447

* p+57

* p.67

• p*•p

* p+sm2

*p+Sm3

: TIME INTWEGATED BEAK

TIME INTEGATED Ipsi

sg1 SECOWDARY SIDE MASS

9g2 SECONDARY SIDE MASS

sgls SECODAY SIDS MASS

ACCUMULATOR 2 MASS

ACCUMULATOR 3 MASS

agi $STAM DONE PRESSURE

*g2 STEAM DOME PRESSURE

&9a3 STEAM DOME PRESSURE

PRESSURIZER TOP PRESSURE

ACC:UULATOR 2 GAS PHASE

ACCUMULATOR 3 GAS PEAS

** dodatni *kontrolni" iLpis,

:391 catrlvar 111

392 CntrIvar 203 *

*393 cntrivar 303 I

-394 cntrlvar 403 *

"395 cntrlv•r S03 *

*396 catrlvar 335 S

"397 c 'trlvar 283 *

*398 cntrlvar 295 *

ikj/kgl

reactor vessel level (m] prz level [mW

ag 1 downcomor level In]

ag 2 dovncomar level [(n

ag 3 downcomer level (a)

beat losses [v]

&@break break specific enth&lpy

pabreek break specific ant•alpy

331 cntrlvar 254

(EPA)

332 cntrlvar 255

[EPA)

• dp3 c13 TO h13 DIFF. PREBS.

• dp32pg pump 3 DIFF. PRESS. • qeOS : DOINC EA KASS FLOW RATE

2
362 eflosi 332010000

RATE 1KG/SI

363 uflovj 432010000

RAT (KG/I

364 mefovj 532010000

RATE (KG/SI

365 mflovi 180000000 WG/8]

366 uflowj 311000000

RATE (KG/SI

367 mflovj 411000000

RATE (KG/SI

368 aflowj 511000000

RAT2 (KG/SI

369 flovi 607000000

RATE (KG/SI

370 Uflowr 907000000

RATI (KG/SI

371 cntrlvar 283

Exi/KGI

372 tempf 123010000

(k)

373 tempf 141010000

ME]

374 tempf 151010000

TMPZERATURE [k]

375 tempf 163010000

TEMPMATURE (ckl

376 tempf 602010000

(k)

377 tempf 655010000

(k)

378 tempf 802010000

[k)

379 tempf 855010000

(k)

380 tempf 902010000

[k)

361 tempf 955010000

(k]

382 tampf 309050000

TEMPBRATURE [k)

383 tempf 409050000

TMPMERTUMR [k)

364 tempt 509050000

TEMPERATRE (k)

385 httemp 131000701

366 httemp 131000601

387 httemp 131000901

NIDDLE TO

366 httemp 131001001

369 httemp 131001101

TAB.1 STR.29/87)

390 httemp 131001201

391 CntrIvar 146

WEc

392 entrlvar 286

[RPM)

393 cntrlvar 287

(RPM)

394 cntrlar 286

[RPM)

*qman32

*qfsgvll

*qmgv12

*qmgb12

*qmzbl2

sg1 PIEMTlR MASS FLOW

sg2 FPRSWATE MASS FLOW

9S3 PEEDWATER MASS FLOW

BREAK MASS FLOW RATE

ag1 STEM LINE MASS FLOW

wg2 STRAN LINr MASS FLOW

sg3 STERN LNE MASS FLOW

ipsa IN c12 MASS FLOW

lpsi IN c13 MASS FLO

395 cntrlvar 289

396 cntrlvar 290

397 cntrlvar 291

396 dt 0

TRANSIENT [S

399 amass 0

* v.02 : CORE (ELEM"TICL,) POMWE

* w~trAc i TRACE RATING [(ll

• zacore SwOLLEN LEV (ME

" dtcalC TIME STEP ALONG

* mor MASS ERROR KGI]

* ttrr tripi

* sebreak s BRIAR SPECIFIC RNTWALPY

501 time 0 qt null 0 300.0 n * break

" tf0l2a

" tf0304

" tf041

" tf042

" tf112

" tf133

" tf212

" tf233

" tf312

" tf333

" tf454c

" tf654c

" tf654c

CORE INLET TEMPERATURE

CORE OUTLET TEMPERATURE

UPPER HEAD (BOTTOM)

UPPER HEAD (TOP)

HOT LM 1 TEMPERATURE

COLD LG 1 TE4PMPETURE

HOT LEG 2 TEMPERATURE

COLD LEG 2 TEMPERATURE

; NOT LBG 3 TEMPERATURE

COLD L2 3 TIMPTRATURE

:OTICH OF gl DOWNCOE

BOTI014 OF s92 DOWNCME

SOTT: OF 9g3

604 -526 or -626 n - 6g pressure control on - before

31. P.

*............................. .......- 

• fii fikairanje zacetnege atanja

............... *•** *•*....................................

*.*•......

Saccuulator vesee2

8330000 accuUm2 accum

8330101 0.0 8.358 0.423 0.0 90.0 0.358 3.96-5 0.0 00

6330200 41.6+5 290. 0.0

• zeta ixtoka je 0.335, zeta kolena je 0.2, upoatevmf 5 kolea

8331101 605000000 0.00114 1.335 1.335 000000

8332200 0.286 0.0 0.119 0.119 0.00927 0 0 0

* accumulator no 2 pipe

8050000 ecel2 angivol

8050101 0.0 21. 0.0239 0.0 20.0 10.005 1.0-4 0.0 00

6050200 2 41.8+S 290.

* accutulator no 2 valve

0060000 accvl2 valve

* zeta kole•a je 0.2. upoatevamo S kolen od 10

8060101 806010000 656000000 0.00114 1.0 1.0 100000

6060201 0 0.00000÷00 0.00000000 0.0000e00

6060300 trpvlv

6060301 669

•8060300 mtrvlv

*8060301 659 656 5.0 0.0

a eccm•mulator vesae13

9330000 accu=3 a*ccu

9330101 0.0 8.356 0.423 0.0 90.0 8.356 3.96-5 0.0 00

9330200 41.$+S 290. 0.0 * zeta iztoka ja 0.335, zeta kolena je 0.2, upoetevemo 4

kolana

, XOt aCCum 833

9331101 905000000 0.00114 1.335 1.335 000000

9332200 0.286 0.0 0.119 0.119 0.00927 0 0 0

* accumulator no 3 pipe

9050000 accZ3 engivol

9050101 0.0 21. 0.0239 0.0 20.0 10.005 1.0-4 0.0 00

9050200 3 41.8+5 290.

* accumlator no 2 valve

9060000 accvl2 valve

- zeta kolena je 0.2 upoatevemo 4 kolea o4 8

9060101 905010000 956000000 0.00114 0.80 0.80 100000

9060201 0 0.00000e+00 0.00000e*00 0.00000e+00

9060300 trpvlv

9060301 669 *9060300 mtrvlv

-9060301 659 656 5.0 0.0

...... 

• ipia pump no 2

6070000 lp42 tmlpjun

6070101 804000000 865010000 0.00599 *.. presek

8070200 1 0 p 203060000

* ai qsb crpelka za abe c1 veji (2.3)

8070201 0.0 0.0 0.0 0.0

6070202 0.6779.5 0.9447 0.0 0.0

6070203 1.041.+5 0.8900 0.0 0.0

6070204 3.8507+5 0.7458 0.0 0.0

807020S 6.767+S 0.4972 0.0 0.0

8070206 6.517+5 0.2486 0.0 0.0

6070207 9.077+S 0.0497 0.0 0.0

6070208 9.100+5 0.0 0.0 0.0

20512600 noname constant 20515200 naoarm constant

20532400 noname conatant

20542400 aoname constant

20662400 noname constant

20621800 noname constant

3290000 noname delete

3300000 noname *elete

4290000 acrmn delete

4300000 nofame delete

5290000 noname delete

5300000 noname delete

7110000 noneme delete

7120000 noname delete

2310000 noname delete

2320000 noname delete

0.648349

0.295703

2.8779*-02

2.9092e-02

2.90886-02

0.0

" ra• love

* 5g recirculation

* prz. beater

" art. feedwater

• ts02091

* t.02151 ;

• t&02191 ROD TEMPERATURE FROM

• ts02201 : TOP CORE ELNVATION 1k)

* t802241 *. ta - ? (LE NEU4RA V

• ta02281 i

* teax MAX. CLAD TOMPERATURE

* pl P PW 1 ROTAXTION SPEED

* vp2 PUMP 2 ROTATION SPEE

• vp3 PUMP 3 ROTATION SPEND

Sart, pressurizer

llp9 l.p.s.i. in akumuuatorji

• trip 659 . trip ventil odpre akumuletorja 2 in 3

3
* ena qab erpalka za vsako c€ vejo

* 8070202 0.6779+5 1.88941 0.0

* 8070203 1.5411.5 1.78996 0.0

* 8070204 3.8507.5 1.49164 0.0

* 8070205 6.767+5 0.99442 0.0

* 8070206 6.517+5 0.49721 0.0

* 8070207 9.077+5 0.09944 0.0

* 8070208 9.100+S 0.0 0.0

(2.3)

0.0

0.0

0.0

0.0

0.0

0.0

0.0

• bpi& tank no 2 - rwst2

8040000 rvst2 tmpv0ol

8040101 0.0 6.1 28.32 0.0 90.0 6.1 1.0-4 0.0 0

8040200 3

8040201 0.0 1.02-S 307.0

* 1pim pump no 3

9070000 lpis3 tnadpjun

9070101 904000000 955010000 0.00599 *÷* prenek

5070200 1 0 p 203060000

9070201 0.0 0.0 0.0 0.0

9070202 0.6779.5 0.9447 0.0 0.0

9070203 1.5411*5 0.8950 0.0 0.0

9070204 3.8507+5 0.7458 0.0 0.0

9070205 6.767*5 0.4972 0.0 0.0

9070206 8.517,5 0.2486 0.0 0.0

9070207 9.077+5 0.0497 0.0 0.0

9070208 8.100*5 0.0 0.0 0.0

3720203 0.0 0.0 0.0 0.0

3720204 1.+5 0.0 0.0078 0.0 * steam discharge

flowrats !

3720205 70.+5 0.0 0.5460 0.0

3720206 100.*5 0.0 0.7800 0.0

*.. ni upostevan zacetni odstopek tlaka: 60.7 bar - 68.4 bar -

0.3 bar

-... p-kav msanem toku do 0.00234 kg/a ... 0.8% (pri 70

bar)

*,, pri prenosu na NO3 se je zacetni odstopek povecal na 0.5

bar

* steam dump no. 1

3670000 -dump2 tdpvol

3670101 0.0 6.1 28.32 0.0 90.0 6.1 1.0-4 0.0 0

3670200 2

3670201 0.0 1.02+5 1.0

• fikairanje prostib cv

20530000 nonam constant 1.0

20534400 noname constant 1.0

4670201 0.0 1.02+5 1.0

20540000 noname constant 1.0

20544400 nosame constant 1.0

.......... *.........*. 

* regulacija tlaka pare: sg3

.............................................. t**...........

5440000

5440101

5440200

5440201

(si) ++

5440202

S440203

1.2 bar

5150000

5150101

5150201

5150300

5150301

* stems

5720000

5720101

5720200

5720201

5720202

5720203

5720204

koVd3 tOdpvol

10.0 0.0 1000.0 0 0.0 0 0.20-03 0 0

2 505 * s1

-1.0 68.0614e+05 1.0 * before turbine bypass

0.0 68.06148*05 1.0

4.0 69.2614e.05 1.0 * after turbine bypass: *

vrgvl3 valve

520010000 544000000 0.0 0.0 0.0 100000

0 6.99040e*00 6.954300*00 0.00000+00

trpvlv

604 - after ultimate orocedur,e

b hpi* tank no 3 - rwot3

9040000 rwmt3 tmdpvol

9040101 0.0 6.1 28.32 0.0 90.0

9040200 3

9040201 0.0 1.02*5 307.0

regulacija tlaka pare: sg2

6.1 1.0-4 0.0 0

dump no. 3

ed& 3 todpjun

520010000 567000000 0.00

1 526 p 510020000

-1.0 0.0 0.0 0.0

-0.5 0.0 0.0 0.0

0.0 0.0 0.0 0.0

1.+5 0.0 0.0078 0.0

2

* Jregulacija tlaka pare: sg1

4440000

4440101

4440200

4440201

(si) #+

4440202

4440203

1.2 bar

4150000

4150101

4150201

4150300

4150301

kozd2 tmdpvol

10.0 0.0 1000.0 0 0.0 0 0.20-03 0 0

2 505 •si

-1.0 68.0613e,05 1.0 * before turbine bypass

0.0 68.0613e.05 1.0

4.0 69.2613e-0S 1.0 * after turbine bypass: +

vrgvl2 valve

420010000 444000000 0.0 0.0 0.0 100000

0 6.990400*00 6.954300*-00 0.00000e+00

trpvlv

604 * after ultimate procedur

16475

- steam discharge

6.1 1.0-4 0.0 0

3440000

3440101

3440200

3440201

(si) ++

3440202

3440203

1.2 bar 0,,

3150000

3150101

3150201

3150300

3150301

koand tdApvol

10.0 0.0 1000.0 0 0.0 0 0.20-03 0 0

2 505 * si

-1.0 68.0571e+05 1.0 * before turbine bypass

0.0 68.0571*+05 1.0

4.0 69.25710+05 1.0 * after turbine bypass +

4.0 a ... dejanako tlak naraSte v 3 a

vrgvll valve

320010000 344000000 0.0 0.0 0.0 100000

0 6.59040e*00 6.95430e.00 0.00000*+00

trpvlv

604 • after ultimate procedur.

flowrate I

5720205 70.+5 0.0 0.5460 0.0

5720206 100.,5 0.0 0.7800 0.0

* tam dupno. 3

5670OO sdump3 tmdpvol

5670101 0.0 6.1 28.32 0.0 90.0

5670200 2

5670201 0.0 1.02+S 1.0

20550000 nonsma Constant 1.0

20554400 nOona. Constant 1.0

5

• steam dump no. 2

4720000 sdump2 tadpjun

4720101 420010000 467000000 0.00216475

4730200 1 526 p 410020000

4720201 -1.0 0.0 0.0 0.0

4720202 -0.5 0.0 0.0 0.0

4720203 0.0 0.0 0.0 0.0

4720204 1.+5 0.0 0.0078 0.0 * 51

flomrate t

4720205 70.+S 0.0 0.5460 0.0

4720206 100.+5 0.0 0.7800 0.0

team discharge

* 0af9w pomosne napajanje

* cv 320 ps s8gl or level (pa/g]

* 0.0197 1/2 1/9.8067

20532000 dplr2 sum 1.0 0.0 1

20532001 0.0 0.10197 p 308010000 -0.10197 p 310010000

20532002 0.121 rho 308010000 0.440 rho 310010000

* stea dump no. 1

3720000 sdumpi tmapjun

3720101 320010000 367000000 0.00216475

3720200 1 526 p 310020000

3720201 -1.0 0.0 0.0 0.0

3720202 -0.5 0.0 0.0 0.0

* stem dump no. 2

4670000 Sdu•p2 tmdpvol

4670101 0.0 6.1 28.32 0.0 90.0 6.1 1.0-4 0.0 0

4670200 2

4
* cv 321 narrow range sgi level (m]

20532100 ztlr2 div 1.0 0.0 1

20532101 rho 308010000 cntrlvar 320

* cv 322 ± wide range sg8 level [m]

20532200 otsgl sum 1.0 0.0 1

20532201 11.255 1.0 cntrlvar 321

* afw pump no. 1 - before ultimate procedure

3700000 afuli tmdpjun

3700101 368000000 332000000 0.0006786

3700200 1 626 cntrlvar 322

3700201 -1.0 0.0 0.0 0.0

3700202 0.0 0.30329 0.0 0.0

3700203 13.32 0.30329 0.0 0.0

* 3700204 13.4 0.24263 0.0 0.0

* 3700205 13.5 0.16726 0.0 0.0

* 3700206 13.6 0.09169 0.0 0.0

* 3700207 13.7 0.01611 0.0 0.0

* 3700208 13.71 0.00855 0.0 0.0

* 3700209 13.715 0.00477 0.0 0.0

3700210 13.72 0.0 0.0 0.0

* afw pump no. 1 - after ultimate procedure

3710000 afwlii tedpjun

3710101 369000000 332000000 0.0006786

3710200 1 526 cntrlvar 322

3710201 -1.0 0.0 0.0 0.0

3710202 0.0 0.30329 0.0 0.0

3710203 13.14 0.30329 0.0 0.0

* 3710204 13.20 0.24263 0.0 0.0

* 3710205 13.25 0.16726 0.0 0.0

* 3710206 13.30 0.09169 0.0 0.0

* 3710207 13.325 0.01611 0.0 0.0 * 3710208 13.34 0.00855 0.0 0.0

3710209 13.35 0.00477 0.0 0.0

* afw tank-i no. 1

3680000 afwtli tmdpvol

3680101 0.0 6.1 28.32 0.0 90.0 6.1 1.0-4 0.0 0

3680200 003

3680201 0.0 1.02+5 307.0

* afw tank-li no. I

3690000 afwtlii tmdpvol

3690101 0.0 6.1 28.32 0.0 90.0 6.1 1.0-4 0.0 0

3690200 003

3690201 0.0 1.02.5 307.0

* cv420 dp eg2 nr level [pa/gI

* 0.0197 - 1/9.8067

20542000 dp2r2 aum 1.0 0.0 1

20542001 0.0 0.10197 p 408010000 -0.10197 p 410010000

20542002 0.121 rho 408010000 0.440 rho 410010000

* c 421 narrow range ag2 level (m)

20542100 at2r2 div 1.0 0.0 1

20542101 rho 408010000 cntrliar 420

* cv 422 wide range eg2 level (m)

20542200 ztsg2 aum 1.0 0.0 1

20542201 11.255 1.0 cntrlver 421

* ate pump no. 2 - before ultimate procedure

4700000 afw2i tedpjun

4700101 468000000 432000000 0.0006786

4700200 1 626 cntrlvar 422

4700201 -1.0 0.0 0.0 0.0

4700202 0.0 0.30329 0,0 0.0

4700203 13.32 0.30329 0.0 0.0

* 4700204 13.4 0.24263 0.0 0.0

* 4700205 13.5 0.16726 0.0 0.0

* 4700206 13.6 0.09169 0.0 0.0

* 4700207 13.7 0.01611 0.0 0.0

* 4700208 13.71 0.00855 0.0 0.0

* 4700209 13.715 0.00477 0.0 0.0

4700210 13.72 0.0 0.0 0.0

* afv pump no. 2 - after ultimate procedure

4710000 afw2ii tedpjun

4710101 469000000 432000000 0.0006786

4710200 1 S26 cntrlvar 422

4710201 -1.0 0.0 0.0 0.0

4710202 0.0 0.30329 0.0 0.0

4710203 13.14 0.30329 0.0 0.0

* 4710204 13.20 0.24263 0.0 0.0

* 4710205 13.25 0.16726 0.0 0.0

* 4710206 13.30 0.09169 0.0 0.0

* 4710207 13.325 0.01611 0.0 0.0

* 4710208 13.34 0.00855 0.0 0.0

4710209 13.35 0.00477 0.0 0.0

* afw tank-i no. 2

4680000 afwt2i tmdpvol

4680101 0.0 6.1 28.32 0.0 90.0 6.1 1.0-4 0.0 0

4680200 003

4680201 0.0 1.02+5 307.0

* afw tank-ii no. 2

4690000 afvt2ii tedpvol

4690101 0.0 6.1 28.32 0.0 90.0 6.1 1.0-4 0.0 0

4690200 003

4690201 0.0 1.02.5 307.0

* cv 520 dp eg3 nr level (pa/gI

* 0.0197 - 1/9.8067

20552000 dp3r2 eum 1.0 0.0 1

20552001 0.0 0.10197 p 508010000 -0.10197 p 510010000

20552002 0.121 rho 508010000 0.440 rho 510010000

• cv 521 narrow range eg3 level [ma

20552100 at3r2 div 1.0 0.0 1

20552101 rho 508010000 cntrlvar 520

• cv 522 wide range e93 level (m]

20552200 zte93 gum 1.0 0.0 1

20552201 11.255 1.0 sntrlvar 521

* afw pump no. 3 - before ultimate procedure

5700000 afv3i tudpjun

5700101 568000000 532000000 0.0006786

5700200 1 626 cntrlvar 522

5700201 -1.0 0.0 0.0 0.0

5

5700202 0.0 0.30329 0.0 0.0

5700203 13.32 0.30329 0.0 0.0 * 5700204 13.4 0.24263 0.0 0.0

* 5700205 13.5 0.16726 0.0 0.0

* 5700206 13.6 0.09169 0.0 0.0

* 5700207 13.7 0.01611 0.0 0.0

* 5700208 13.71 0.00855 0.0 O0S

: 5700209 13.715 0.00477 0.0 0.0

5700210 13.72 0.0 0.0 0.0

* aft pump no. 3 - after ultimate procedure

5710000 afW3ii tmdpjun

5710101 569000000 532000000 0.0006786

5710200 1 526 ontrivar 522

5710201 -1.0 0.0 0.0 0.0

5710202 0.0 0.30329 0.0 0.0

5710203 13.14 0.30329 0.0 0.0 • 5710204 13.20 0.24263 0.0 0.0

" 5710205 13.25 0.16726 0.0 0.0

• 5710206 13.30 0.09169 0.0 0.0

* 5710207 13.325 0.01611 0.0 0.0

• 5710208 13.34 0.00855 0.0 0.0

5710209 13.35 0.00477 0.0 0.0

* afw tank-i no 3

5680000 afwt3i twdpvol

5680101 0.0 6.1 28.32 0.0

5680200 003

5680201 0.0 1.02.5 307.0

• ate tank-ii no 3

5690000 afwt3ii tsdpvol

5690101 0.0 6.1 28.32 0.0

5690200 003

5690201 0.0 1.02.5 307.0

90.0 6.1 1.0-4 0.0 0

90.0 6.1 1.0-4 0.0 0

* all alom : cli

............ ***........

1800000 break k ngijun

* e*t. 1800101 655010000 182000000 2.091e-05 1.0 1.0

130102 0.564 0.92

* * 1800101 655010000 182000000 2.091e-05 1.0 1.0 130102

0.85 0.92

* 1800101 655010000 182000000 2.0911-09 1.0 1.0 130100

0.85 1.20

1800201 0 0.0 0.0 0.0

• zlom-spoj is btestm3n2.dat

1800000 break engljun

* 1800101 655010000 182000000 2.091e-0S 1.0 1.0 -130100

0.85 1.0 1.1

1800101 655010000 182000000 2.0918-05 1.0 1.0 130100

0.80 1.0 1.1

1800201 0 0.0 0.0 0.0

1020000 bline englvol

1820101 1.6619-3 10.0 0.0 0.0 0.0 0.0 1.0e-04 0.0 00

1820200 3 5SS.Oe0OS 533.0

1830000 bvent valve
1530101 152010000 156000000 1.66000-03 0.0 0.0 100100

1530201 0 0.0 0.0 0.0

1530300 strvlv

1530301 501 £03 20. 0.0

1560000 tank tmd6 vol

1560101 1.0 0.0 5.02 0.0 0.0 0.0 1.00-04 0.0 00

1560200 2

1560201 0.0 1.00+05 1.0

* blowdown tan• keep the preslure at a level which is

not likely

* to influence the break flow rate (str.25/S0)

* separator pare ---. branch

oak. osatem, seaprator pare

3070000 separ branch

3070001 3 0

3070101 0.0 1.9430 0.09467 0 90.0 1.9430 0.19-04 0.249

00

3070200 100 6.547200+06 1.24232e.06 2.55325e+06 1.51410e01

3071101 307010000 310000000 4.26954-02 0.52 0.14 00000

3072101 307000000 305000000 44.9150*-02 0.26 0.23 00000

3073101 303010000 307000000 4.5695a-02 0.0 0.0 00000

3071201 3.70160e-01 3.95960e-0l 0.00000e+00

3072201 *3.15359e-03 -4.578620-03 0.O0000oe00

3073201 3.41760*-Cl 3.737800-01 0.O0000e*00

: ex. sistem:,separator pare

4070000 separ branch

4070001 3 0

4070101 0.0 1.9430 0.09467 0 90.0 1.9430 0.10-04 0.249

00

4070200 100 6.847520,06 1.24169**06 2.58326e+06 1.34150.-

01

4071201 407010000 410000000 4.86950-02 0.52 0.14 00000

4072101 407000000 405000000 44.91500-02 0.26 0.23 00000

4073101 403010000 407000000 4.56955-02 0.0 0.0 00000

4071201 2.511900-01 3.107300-01 0.OO000e+00

4072201 6.343190-03 4.914650-03 0.00000e+00

4073201 3.39400*-01 3.73250s-01 0.00000e#00

* oAk. mistent separator pare

5070000 separ branch

5070001 3 0

S070101 0.0 1.9430 0.09467 0 90.0 1.9430 0.le-04 0.249

00

5070200 100 6.84752e+06 1.24169o+06 2.583260+06 1.341500-

01

5071101 S07010000 510000000 4.85695e-02 0.52 0.14 00000

5072101 507000000 505000000 44.91500-02 0.26 0.23 00000

5073101 503020000 507000000 4.8695e-02 0.0 0.0 00000

5071201 2.512100-01 3.10750*-01 0.000000+00

5072201 6.34016e-03 4.912565-03 0.00000e+00

5073201 3.394000-01 3.73250*-01 0.O0000e+00

............. .............. .................

• hesl beat structure thermal property data

.................. *••l/tt***** ..................... •*

..... .. . .. l+. . *

* composition type and data format

20100100 thl/fctn 1 -1 * stainless steel

20100200 tbl/fctA 2 2 * boron nitride (heater rods)

20100300 tbl/fctn 1 -1 - inconel 600

• thermal conductivity data

* stainless steel

20100101 293. 13.9, 373. 15.1. 473. 16.7, 573. 10.3, 673.

19.8. 873. 23.0,

-1 20100102 1073. 26.1

20100102 1073. 26.1 1473. 26.1

- boron nitride

*! 20100201 473. 1073. 2. 0. 0. 0. 0. 0. 0.

20100201 293. 1473. 2. 0. 0. 0. 0. 0. 0.

* inconel 600

20100301 293. 14.9, 373. 15.6. 473. 17.2, 673. 20.4, 573.

23.7. 1073. 27.4

volumetric heat capacity data

• stainless steel

20100151 3.57870+6, 3.5577866. 4.0976586, 4.20598.6,

4.26474+6, 4.41405.5,

*1 20100152 4.65555+6

20100152 4.65555+6 4,65555+6

• boron nitride

-1 20100251 473. 1073. 1.46+6 1.62+3 0. 0. 0. 0. 0.

20100251 293. 1473. 1.46+6 1.62+3 0. 0. 0. 0. 0.

- inocoel 600

20100351 3.76320+6. 3.55526+6., 4.02919+6, 4.26422+6,

4.61003+6. 4.98467+6

.comparison report dodatki

20516000 avgrhof sma 0.0533 0.0 1

20516001 0.0 1.0 rbof 131010000 1.0 rho! 131020000 1.0

rho! 131030000

20516002 1.0 rho! 131040000 1.0 rho! 131050000 1.0

rhof 131010000

20516003 1.0 rho! 131070000 1.0 rho! 131050000 1.0

rbof 131090000

20516004 1.0 rho! 131100000 1.0 rho! 131110000 1.0

rho! 131120000

20516100 clevl sum 1.0 0.0 1 - 101.94 . 1000-1/9.81

20516101 0.0 101.94 cntrlvar 240 -5.61 rhog 131060000

20516200 clov2 sum 1.0 0.01 1

6

20516201 0.0 1.0 catrlvar 160 -1.0 rhog 131060000

ctv 163: collapsed liquid core level (a)

20516300 corelevi div 1.0 o. 1 3 0.0 9.5

20516301 catrlvar 162 catrivar 161

. .* 

ctV 1461 maximam bttese rx core, right-wall surface

20514600 maxrxt stdfnctn 1.0 600. 1

20514601 max httemp 131000106 httemp 131000206

20514602 Uttemp 131000306 httemp 131000406

20514603 httep 131000506 httemp 131000606

20514604 httemp 131000706 httemp 131000506

20514605 httomp 131000506 httmlp 131001006

20514606 httemp 131000906 httemp 131001206

aacetno stanjo. mcp(O) + 0=2(0) + 5m3(0)

1949 0Y + 286 +G + 256 XG . 2521 XG

20517000 mcp sm 1.0 1949.0 0

20517001 2521.0 -1.0 cntrlvar 271 -1.0 cntrlvar 275

20517002 -1.0 cntrlvar 276 +1.0 cntrlvar 274

+. .. .**f**+****............. 

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

(2-M (Assned by NRC, Add Vol. Supp., Rev., NRCM 110Z, mWc Addendum Numbers, If wm.)

3M. 3= BIBUOGRAPHIC DATA SHEET

2. TITLE AND SUBTITLE NUREGAA-0141

Result of BETHSY Test 9.1.b Using RELAPM/MOD3 3. DATE REPORT PUBUSHED

MONTHYEAR

August 1998

4. FIN OR GRANT NUMBER

W6238

5. AUTHOR(S) 6. TYPE OF REPORT

S. Petelin, B. Mavko, 0. Gortnar, I. Ravnikar, G. Ceme

7. PERIOD COVERED (OncushA vDi)

8. PERFORMAING ORGANIZATION - NAME AND ADDRESS (FNRC, provide Dkikvi€• Oft& orfRtibm U.S. Mc wrReguisfry Gonmr.kts~i &W mf • •wus d ffoo

provide nome and mlng oedhsj

University of Ljubljana

"Jozef Stefan" Institute

Ljubljana, Slovenia

O. SPONSORING ORGANIZATION. -NM ANDADDRSS PrK ,&w yp Same as •xow'1, =•¢'. r pwoid& RDkve, Oftarft,'n U.S.&xe N~bRWA•=y Conmmsw,

ardmefaft eddies.

Office of Nulear Regulatory Research

U.S. Nuclear Regulatory Commission

Washington, DC 20555-0001

10. SUPPLEMENTARY NOTES

S. Smith. NRC Proeect Manaaer

11. ABSTRACT (" wordsor issa)

RELAP5 computer code was used to simulate an experiment designated 9.1.b, (2" Cold Leg Break without HPSI and with Delayed

Ultimate Procedure) performed on BETHSY integral test faclTity. This test is characterized as beyond design transients scenarios

with unavailabiflty of some safety and protection systems. The calculations which have been completed using the computer Sun

Sparcstation 20 aim to evidence the difference between experimental and computed data. Generally, an agreement of major

transient trends is shown to be obtained In the simulation.

12. KEY WORDS/DESCRIPTORS gm wads ao.rphse owt we assistmaewcls in jkatog report) 1. AVAILABI" STATEMENT

RELAP5, BETHSY, Beyond Design Basis Accidents (BDBA) unlimited

14. SECUMn'Y CLASSIFICATION

unclassified

gtaM Rep"t

unclassified

15. NUMBER OF PAGES

16. PRICE

NRC FORM 335 (2419 This lorm *= ewctonkaffy produosd by Elft Fed" Rx., , kc


Federal Recycling Program

NUREG/IA-0141 RESULT OF BETHSY TEST 9.1.B USING RELAP5IMOD3 AUGUST 1998

UNITED STATES

NUCLEAR REGULATORY COMMISSION

WASHINGTON, DC 20555-0001

SPECIAL STANDARD MAIL

POSTAGE AND FEES PAID

USNRC

PERMIT NO. G-67

OFFICIAL BUSINESS

PENALTY FOR PRIVATE USE, $300