NUREG/IA-0154

, International

Agreement Report

RELAP5/MOD3.2

Post Test Analysis and

Accuracy Quantification of

SPES Test SP-SB-03

Prepared by

F D'Auria

M. Frogheri*

W Giannotti

University of Pisa *University of Genova

Via Diotisalvi 2-56100 DITEC

Pisa, Italy Via all'Opera Pia 15a

16143 Genova, Italy

Office of Nuclear Regulatory Research

U.S. Nuclear Regulatory Commission

Washington, DC 20555-0001

February 1999

Prepared as part of

The Agreement on Research Participation and Technical Exchange

under the International Code Application and Maintenance Program (CAMP)

Published by

U.S. Nuclear Regulatory Commission
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NUREG/IA--0154

International

Agreement Report

RELAP5/MOD3.2

Post Test Analysis and

Accuracy Quantification of

SPES Test SP-SB-03

Prepared by

E D'Auria

M. Frogheri*

W Giannotti

University of Pisa *University of Genova

Via Diotisalvi 2-56100 DITEC

Pisa, Italy Via all'Opera Pia 15a

16143 Genova, Italy

Office of Nuclear Regulatory Research

U.S. Nuclear Regulatory Commission

Washington, DC 20555-0001

February 1999

Prepared as part of

The Agreement on Research Participation and Technical Exchange

under the International Code Application and Maintenance Program (CAMP)

Published by

U.S. Nuclear Regulatory Commission

ACKNOWLEDGMENTS

The authors wish to acknowledge the technical support given to the present research by Dr. P.

Marsili by A1NPA, who also stimulated the same activity.

At DCMN of University of Pisa thanks are due to Dr. G. M. Galassi for storing the needed

data and for the suggestions given for solving some of the encountered problems, and to Prof. F.

Oriolo for managing the activity.

I

CONTENTS

ABSTRACT

LIST OF FIGURES

LIST OF TABLES

5

7

9

1. INTRODUCTION

2. DESCRIPTION OF THE EXPERIMENT

2.1 Spes facility

2.2 Test SP-SB-03

3. ADOPTED CODE AND NODALIZATION

3.1 Relap5/Mod3.2 code

3.2 General criteria adopted for the code models

3.3 SPES nodalization description

3.4 Nodalization qualification

4. ANALYSIS OF POST-TEST CALCULATION RESULTS

4.1 Steady State calculations

4.2 Reference calculation results

4.2.1 Qualitative and quantitative accuracy evaluation

4.3 Sensitivity calculations

5. CONCLUSIONS

REFERENCES

LIST OF ABBREVIATIONS

SUBSCRIPTS

APPENDIX 1: Steady state calculation

APPENDIX 2: Results of the reference calculation (run T03A)

APPENDIX 3: Results of the sensitivity analyses (runs S301, S302, S303, S304, S305)

APPENDIX 4: Reference calculation input deck

11

13

13

16

21

21

21

22

28

33

33

34

43

47

57

59

61

61

3

ABSTRACT

The present document deals with the Relap5/Mod3.2 analysis of the Small Break LOCA

experiment SP-SB-03 performed in SPES facility.

SPES is a PWR simulator (Integral Test Facility) installed at SIET center in Piacenza (I).

Volume scaling and core power scaling factors are 1/427, with respect to the Westinghouse 900

MWe standard reactor.

The experiment is originated by a small break in the cold leg (2" equivalent break area in the

plant) without the actuation of the high pressure injection system. Low pressure injection system

actuation occurs after core dry-out.

The Relap5 code has been extensively used at University of Pisa; the nodalization of SPES

facility has been qualified through the application of the version Relap5/Mod2 to the same

experiment and another test performed in the same facility.

Sensitivity analyses have been addressed to the influence of several parameters (like discharge

break coefficient, time of accumulators start etc.) upon the predicted transient evolution.

Qualitative and quantitative code calculation accuracy evaluation has been performed.

5

LIST OF FIGURES

Fig. 1: Spes facility - sketch of the plant .................................................................................... 14

Fig. 2: Spes facility-flowsheet .................................................................................................. 15

Fig. 3: SP-SB-03 test - measured trends of primary pressure, secondary pressure and rod surface

tem perature ............................................................................................................................. 20

Fig. 4: SP-SB-03 test - measured trends of primary mass and of ECC delivered mass ................ 20

Fig. 5: Relap5/Mod3 nodalization of Spes facility ..................................................................... 23

Fig. 6: Comparison between measured and calculated volume vs. height curve .......................... 31

Fig. 7: Comparison between measured and calculated DP vs. length curve ................ 31

Fig. 8: SPES post test SP-SB-03 (reference caic.) - primary and secondary pressure ................. 38

Fig. 9: SPES post test SP-SB-03 (reference calc.) - integral break flow rate .............................. 38

Fig. 10: SPES post test SP-SB-03 (reference calc.) - ECCS integral flow rate ............................ 39

Fig. 11: SPES post test SP-SB-03 (reference calc.) - pressurizer level ........................................ 39

Fig. 12: SPES post test SP-SB-03 (reference calc.) - core level ................................................. 40

Fig. 13: SPES post test SP-SB-04 (reference calc.) - rod surface temperature (high level) ......... 40

Fig. 14: SPES post test SP-SB-03 (run S301) - PRZ pressure ................................................... 51

Fig. 15: SPES post test SP-SB-03 (run S301) - break integral flow rate ..................................... 51

Fig. 16: SPES post test SP-SB-03 (run S302) - PRZ pressure ................................................... 52

Fig. 17 SPES post test SP-SB-03 (run S302) - rods cladding temperature (high level) ............... 52

Fig. 18: SPES post test SP-SB-03 (run S303) - PRZ pressure ................................................... 53

Fig. 19: SPES post test SP-SB-03 (run S303) - break integral flow rate ..................................... 53

Fig. 20: SPES post test SP-SB-03 (run S304) - PRZ pressure ................................................... 54

Fig. 21: SPES post test SP-SB-03 (run S304) - break integral flow rate ..................................... 54

Fig. 22: SPES post test SP-SB-03 (run S305) - PRZ pressure ................................................... 55

Fig. 23 SPES post test SP-SB-03 (run S305) - rods cladding temperature (high level) ............... 55

7

LIST OF TABLES

Tab. 1: Relevant initial and boundary conditions for Spes test SP-SB-03 in comparison with the

other counterpart tests ....................................................................................................... 18

Tab. 2: Imposed sequence of trips for SPES test SP-SB-03 ....................................................... 18

Tab. 3 - SPES SP-SB-03 experiment: resulting sequence of main events .................................... 19

Tab. 4: Relap5IMod3.2 nodalization - correspondence between code nodes and hydraulic zones .... 24

Tab. 5: Relap5/Mod3 Spes nodalization - overview of code resources ....................................... 26

Tab. 6 - Criteria for nodalization qualification at the steady-state level ................... 30

Tab. 7: Comparison between measured and calculated (Relap5/Mod2 and Relap5/Mod3.2) relevant

initial and boundary conditions ........................................................................................... 41

Tab. 8: Resulting sequence of events, comparison among experimental test and calculated results.. 42

Tab. 9: Judgment of code calculation performance on the basis of phenomena included in the CSNI

m atrix .................................................................................................................................... 44

Tab. 10: Judgment of code calculation on the basis of relevant thermalhydraulic aspects ........... 45

Tab. 11: Summary of results obtained by application of FFT method to the selected parameters for

the reference calculation .................................................................................................... 46

Tab. 12: Sensitivity calculation matrix: varied input parameters and FFT results ........................ 48

Tab. 13: Summary of results obtained by application of FFT method to the selected parameters for

the sensitivity calculations (AA values) ................................................................................ 49

Tab. 14: Summary of results obtained by application of FFT method to the selected parameters for

the sensitivity calculations (WF values) ............................................................................... 50

9

1. INTRODUCTION

The performance assessment and validation of large thermalhydraulic codes and the accuracy

evaluation when calculating the safety margins of Light Water Reactors are among the objectives of

international research programs, such those organized by the committee on the Safety of Nuclear

Installations (CSNI) and the Code Application and Maintenance Program (CAMP).

Solution of these problems would ensure the effectiveness of engineered safety features and,

eventually, lead to cost reductions through better design. This activities could also contribute to the

determination of a uniform basis on which to assess the consequences of reactor system failures in

Nuclear Power Plants, refs. [I] and [2].

The execution of the experiments in Integral Test Facilities simulating the behavior of a nuclear

plant, plays an important role in this connection, both considering the system code assessment and

the possibilities to identify and characterize the relevant phenomena during off-normal conditions.

A special kind of experiments are the so called counterpart tests. These are similar experiments

performed in differently scaled facilities. It is well dear that transient scenarios measured in the

experimental rigs can not be directly extrapolated to the plant conditions. Nevertheless one of the

objectives of a counterpart test is to evaluate the influence of the geometric dimension of the loop

upon the evolution of a given accident.

Counterpart tests have been performed in four PWR simulators: LOBI, SPES, BETHSY and

LSTF, ref. [3], respectively available at the European Community Joint Research Center of Ispra (I),

at SIET in Piacenza (1), at CENG in Grenoble (F) and at JAERI in Tokai-Mura (Q). The selected

experiment is a small break LOCA originated by a rupture in the cold leg, without actuation of high

pressure injection system and with accumulators availability, in particular, starting from low power

conditions (about 10% of the nominal period). Both tests have been performed in the smallest

facilities, SPES and LOBI, starting from full power conditions, all other conditions being the same.

The activity documented in this report is a part of a multipurpose research aiming at the overall

evaluation and exploitation of the counterpart test database. On one hand the Relap5 system code

(Mod2 and, presently, Mod3.2) has been applied to the post test analysis of the four experiments and

to the evaluation of plant scenario during the same transient; on the other hand the experimental data

base have been evaluated to demonstrate the similarity in the behavior of the facilities, ref. [3]. The

two parts of the research have been merged and conclusions have been drawn in relation to the

scaling of phenomena and of the accuracy of thermalhydraulic code calculations.

Previous reports dealt with the evaluation of the experimental data base constituted by the four

counterpart experiments and with the qualification of Relap5/Mod2 nodalization used for the post

test analyses, refs. [4] and [5], as well as with a complete evaluation of the data base leading to the

evaluation of uncertainties (e.g. ref. [6]).

The present document deals with the post test analysis performed by Relap5/Mod3.2 of the

small break LOCA counterpart test carried out in SPES facility (SP-SB-03).

The purpose of this report is to evaluate the performance of the RelapS/Mod3.2 in comparison

with the previous application with the version Mod2. In order to achieve this, a systematic

qualitative and quantitative accuracy evaluation has been performed. The quantitative analysis has

been performed adopting a method (ref. [7]) developed at DCMN, which has capabilities in

quantifying the errors in code predictions related to the measured experimental signal; the Fast

Fourier Transform (FFT) is used aiming at having an integral representation of the code calculation

discrepancies (i.e. error between measured and calculated time trends) in the firequency domain.

The qualitative accuracy evaluation, based on the selection of relevant thermalhydraulic aspects

is a prerequisite to the application of the FFT based method.

11
The comparison of the two experiments, SP-SB-03 and SP-SB-04 (high power test, see also ref

[8]) led to the conclusion that, apart from the first 200 s of the transient, the key phenomena are the

same and occur almost at the same time.

12
2. DESCRIPTION OF THE EXPERIMENT

2.1 Spes facility

The SPES (Simulatore PWR per Esperienze di Sicurezza) Integral Test Facility, ref [9], is

designed to simulate the whole primary circuit, the relevant parts of the secondary circuit (steam

generator secondary sides, main feed water lines up to the isolation valves, main steam lines

upstream the turbine valves), and the most significant auxiliary and emergency systems (charging and

let-down system, safety injection system, including high pressure and low pressure system,

accumulators, emergency feed water system, steam dump and so on) of the Italian Standard Nuclear

power plant (PWR-PUN, Westinghouse 312 type, 3 loops, 2775 MWth core power).

The basic design choices of the facility are the following:

* three active loops to simulate a three loops reactor,

* design pressure 20 MPa, design temperature 910 K; this choice allows the execution of tests with

primary pressure over the reactor design pressure (17.2 MPa);

* electrical heating of the power channel: 97 electrically heated rods, with uniform flux (local hot

spots can be simulated by means of three rods with a peaking factor of 1.19);

Smaximum channel power corresponding to about 140% of the reactor nominal power, this choice

allows the simulation of reactor power excursions;

* volume scaling factor and power scaling factor (nominal power about 6.5 MW) equal to 1:427;

• the height of all the components is the same as in real plant, except for the pressurizer which is

shorter, in order to preserve the volume scaling ratio and to maintain at the same time an

acceptable flow area.

A sketch of the primary and secondary loops is reported in Fig. 1, while Fig. 2 shows a

simplified flowsheet of the facility.

In the SPES rig 375, measurement points are available, providing a large set of both direct

physical quantities (absolute and differential pressure, temperature, voltage, etc.) and derived

physical quantities (void fraction, mass velocity, quality, etc.).

Various kinds of transducers are located in the SPES facility (thermocouples, heated

thermocouples, pressure transmitters, differential pressure transmitters, densitometers, void fraction

probes, Venturi tubes, turbines, catch tank), supplying the following parameters:

" temperature

" pressure

* differential pressure

* liquid level

* density

* void fraction

• velocity

• flow pattern

* fluid mass

13
STEAM

GENERATOR 1

IIGENERATOR 2

tu.

STEAM

GENERATOR 3

PUMP3

PUMP2

DOWN , COMER

POWER

CHANNEL

Fig. 1: Spes facility - sketch of the plant

14
WAlCI ISSEIVOII

Fig. 2: Spes facility - flowsheet

15
2.2 Test SP-SB-03

The counterpart test is essentially a Small Break LOCA originated by a rupture in the cold leg,

between the pump and the vessel. The break is "side oriented" in the pipe and it has an area

equivalent, roughly, to 6 % of the area of the main pipe: the reference break diameter in the

prototype plant is 50 mm (2"). The sequence of the interventions of the various systems is typical of

the kind of transient in a plant: after the break occurrence, scram and pump trip are provided

together with a signal for isolating steam generators (feedwater and steam line closure).

Accumulators intervention is foreseen when primary pressure falls below 4.2 MPa. After

accumulator emptying, the flow rate from the break causes mass depletion in the primary system,

leading unavoidably to core dry out. Low pressure injection system actuation is foreseen after the

occurrence of core dry out and is effective in rewetting the rods.

It should be noted that, owing to the limitation in the maximum power available in Bethsy and

Lstf, the initial conditions of the four counterpart experiments have been established at a core power

around 10 % of the reference reactor nominal power. Few relevant initial condition values are given

in Tab. 1 where, for completeness, the conditions of the remaining three counterpart test are

reported. In Spes and Lobi facilities the counterpart experiments have been repeated utilizing the fMl

power, in order to evaluate whether the transient evolution was affected by the initial conditions; the

data related to the two full power experiments are also reported in Tab. 1.

The data given in Tab. 1 demonstrate that in the four low power experiments, the choice was

made to preserve the initial value of the fluid temperature jump across the core (mass flow rate

reduced of the same amount as power) and to have the same hot leg temperature. In order to achieve

this it was necessary to increase the initial temperature and pressure of steam generators with respect

to the nominal conditions.

The general purpose of the counterpart experiments (including the two full power experiments)

was to be part of the counterpart program. Relevant thermalhydraulic phenomena of potential

interest during the experiments are mass distribution in the primary system, heat transfer with

secondary side with degraded primary conditions including reversal of heat flux, loop seal behavior,

core heat up and rewet, accumulator performance and stratification in horizontal pipes.

The sequence of main imposed and resulting events for Spes test SP-SB-03 is given in Tabs. 2

and 3, respectively. The transient scenario can also be derived from Figs. 3 and 4.

The accident can be subdivided into four main periods from a phenomenological point of view:

a) subcooled blowdown and first core dry-out rewet (time from 0 to 132 s);

b) saturated blowdown and primary to secondary side pressure decoupling (from 132 s up to

accumulators emptying);

c) mass depletion in primary loop (from accumulators emptying to the final core dry-out);

d) intervention of low pressure injection system that quenches the core.

Phase a). Following the break, the primary system pressure is subject to an initial fast decrease (0.1

MPa/s) up to the achievement of saturation conditions upstream the break. The sharp initial pressure

decrease leads to scram, main coolant pump trip and isolation of steam generators in the first 10 s of

the transient. Pressurizer emptying occurs in about 20 s. During the first phase, natural circulation

between core and downcomer through the steam generators develops up to the time when U-tubes

draining occurs in primary side: at this time the saturation temperature in primary loop is still few

degrees higher than saturation temperature in secondary side.

The stop in natural circulation, essentially due to voiding and mass depletion in the upper zones

of the loop, causes manometer type situation in the primary loop piping: the steam produced in the

core partly flows directly to the break through the bypass and partly pushes down the level in the

core to balance the liquid present in loop seals. In this situation core dry-out occurs at about 115 s.

16
The rod temperature excursion ends when loop seal clearing starts (at about 160 s in the broken

loop). Quench occurs simultaneously in the various axial positions of the bundle.

After the occurring of a more or less complete loop seal clearing in the three loops, sufficient

liquid mass is present in the core to cool the rods.

Following the above events (especially broken loop seal clearing) a large amount of steam is

present upstream the break and an important break flow rate decrease takes place.

At the beginning of the transient, the relatively high value of heat losses from the vessel wall to

the environment, made it necessary to increase the initial core power of about 150 kW with respect

to the correctly scaled value. This power surplus was subtracted from core power at time of break

opening and does not appear to have a very important effect upon the transient evolution.

Direct information from pressure drops measurements in loop seal is not available because of the

failure of the installed transducers: this made difficult (and uncertain) to fix the correspondence

between loop seal clearing and core rewet.

Phase b). Continuous core boil off and primary-to-secondary side pressure decoupling characterize

the first part of phase b). The core boil off (the produced steam flows almost entirely to the break)

causes a second smooth level decrease at a pressure higher than the accumulator pressure (4.2 MPa);

liquid old up in the U-tubes of the broken loop steam generator occurs, somewhat limiting steam

flow to the break. In this period the heat transfer from secondary side to primary side is quite small

compared with core power because of the high void fraction in the U-tubes.

The accumulator intervention at 355 s causes the recovery of liquid level in the core and

prevents a second dry out condition.

The isolation of the accumulators occurs at about 1000 s: in the period from 355 s to 1000 s the

primary system mass increases because the liquid flow rate delivered by accumulators is larger than

the break flow rate.

Phase c). The stop of accumulator injection (t = 1058 s) causes another mass depletion period,

leading to the second dry out at about 1300 s into the transient when the primary pressure was

around 1 MPa. No other significant event occurs in this period, excluding the core level depression.

When the rod surface temperature reaches 773 K the low pressure injection system is actuated (1522

s) in the two intact loops cold legs.

It can also be noted that the three steam generators are not connected among each other (this

constitutes a distortion of SP-SB-03 boundary conditions compared with the boundary conditions of

the remaining counterpart experiments) and the SG2 pressure (loop with break) becomes lower than

in the other two loops. This, excluding small leaks from secondary side or higher heat losses in SG2,

is a demonstration that primary flow rate is larger in the broken loop than in the other loop.

Phase d). The LPIS flow rate (0.4 kg/s) is quite effective in causing the core quench and in

recovering the facility. The quench front velocity is larger than 0.02 m/s and, at about 2000 s, the

core is completely recovered. Core refill occurs in this period. The test was terminated at 2034 s

with pressure around 0.8 MPa.

17
unit Lobi Lobi Spes Spes Bethsy Lstf

BL-34 BL-44 SP-SB-03 SP-SB-04 6.2TC SB-CL-21

core power kW 630 5280 768 5600 2863 7930

pressurizer pressure MPa 15.47 15.46 15.06 15.16 15.38 15.4

hot leg temperature K 589 589 586 589 587 590

average core AT K 27.5 35 28.6 31 31 31

core inlet mass flow kg/s 3.6 28 4.21 31.8 19.5 48.4

rate

bypass DC-UH % 0.83 0.11 0.81 0.97 0.72 0.52

mass flowrate /

core mass flowrate

steam generator MPa il 6.94 il 5.12 6.94 6.7 6.86 7

secondary side bl 6.91 bl 5.11 6.87 6.84

pressure _6.88 6.84

steam generator m il 8.14 il 8.14 11.5 11.5 11.2 11.24

downcomer level bl 4.48 bl 4.48 11.1 11.23

11.1

pressurizer level m 15 5.1 3.23 3.77 7.45 1.7

feedwater mass kg/s il 0.19 il 1.95 0.095 3.4 0.561 2.2

flow rate bl 0.06 bl 0.75 0.093 2.3

0.0965

feed water K il415 473.6 523 523 523

temperature b1409 437.8

1__ _ 1______ 1440.1 1 1 1 J

Tab. 1: Relevant initial and boundary conditions for Spes test SP-SB-03 in comparison with

the other counterpart tests.

EVENT TIME AND/OR SET POINT VALUES

Break opening 0.s

SCRAM signal pressurizer pressure < 13 MPa

Pumps coastdown initiation as above

Steam line closure as above

Feed water closure as above (plus a delay of 8 s)

Accumulators intervention pressurizer pressure < 4.2 MPa

LPIS intervention max. rod temperature >670K

Tab. 2: Imposed sequence of trips for SPES test SP-SB-03.

18
UNIT SPES SB-03

Break opening s 0

Scram power curve enabled s 6.5

Start of main coolant pumps coast down and its duration S(S) 6.5(5)

Main steam line valve closure s 6.5

Feedwater valve closure s 14.5

Upper plenum in saturation condition s 15

Pressurizer emptied s 12

Break two phase flow s 112

First dryout s 112

Loop seal clearing s 110

loop 1-3No

Occurrence of minimum primary side mass s 355.5

1522

Primary-secondary pressure reversal s 115-138

Second dryout s -

Accumulatrs injection start s 355

Accumulators injection stop s 3)903

1) 1058

Final dryout s 1322.5

LPIS start s 1522

Final e s 1569.5

End oftest s 2034

Tab. 3 - SPES SP-SB-03 experiment: resulting sequence of main events.

19
r

Ph.a Pb..b Phe Ph.d

IPhza Ph. b Ph.c Pih. d -. I

20

ak.

0.

15'-

Ioop seal • PRIMARY PRESS.

clearing . SECONDARY PRESS.

--- ROD TEMP.

"p pressurizer

emptied

PU.PD

trip

4-a

800

600.

4oo

400 CLE

200

10o51-

9% .4 -- I U I - L

-100 400

0

900 1400 1900 2400

Time (s)

Fig. 3: SP-SB-03 test - measured trends of primary pressure,

surface temperature

secondary pressure and rod

.d

.PIS

1900 2400

*. 300

O200

Time (s)

Fig. 4: SP-SB-03 test - measured trends of primary mass and of ECC delivered mass

20
3. ADOPTED CODE AND NODALIZATION

3.1 RelapS/Mod3.2 code

The light water reactor transient analysis code, RELAP5, was developed at the Idaho National

Engineering Laboratory (INEL) for the U.S. Nuclear Regulatory Commission (NRC). Specific

applications of the code have included simulations of transients in LWR system such as loss of

coolant, anticipated transients without Scram (ATWS) and operational transients, such as loss of

feed water, loss of offsite power, station blackout and turbine trip.

The Mod3 version of RELAP5 has been still developed by the INEL, but a consortium consisted

of several countries and domestic Organizations that were members of the International Code

Assessment and Application Program (ICAP) and its successor organization, Code Application and

Maintenance Program (CAMP), contributed to the development and the validation process.

RELAP5/Mod3.2 code, refs. [10] and [11], is based on a non-homogeneous, non-equilibrium

set of six partial derivative balance equations for the steam and the liquid phase. A non-condensable

component in the steam phase and a non-volatile component (boron) in the liquid phase can be

treated by the code. A fast, partially implicit numeric scheme is used to solve the equations inside

control volumes connected by junctions.

In particular, the control volume has a direction associated with it that is positive from the inlet

to the outlet. The fluid scalar properties, such as pressure, energy, density and void fraction, are

represented by the average fluid condition and are viewed as being located at the control volume

center. The fluid vector properties, Le. velocities, are located at the junctions and are associated with

mass and energy flow between control volumes. Control volumes are connected in series using

junctions to represents flow paths.

Heat flow paths are also modeled in a one-dimensional sense, using a staggered mesh to

calculate temperatures and heat flux vectors. The heat structure is thermally connected to the

hydrodynamic control volumes through heat flux that is calculated using a boiling heat transfer

formulation. The heat structures are used to simulate pipe walls, heater elements, nuclear fuel pills

and heat exchanger surfaces.

Several new models, improvements to existing models and user conveniences have been added.

The new models include:

" the Bankoff counter-current flow limiting correlation;

" the ECCMIX component for modeling of the mixing of the subcooled emergency core cooling

system liquid and resulting interfacial condensation,

" a zirconium-water reaction model to model the exothermic energy production on the surface of

zirconium cladding material at high temperature;

* a surface to surface radiation heat transfer model with multiple radiation enclosures defined

through user input;

" a thermal stratification model.

3.2 General criteria adopted for the code models

A detailed nodalization reproducing each geometrical zone of the loop has been developed: in

principle it is suitable for different types of transients.

The general methodology followed is described in refs. [11] and [12]. Being used, in this case,

the Relap5/Mod3 code, great care is given to the information contained in the specific user manual.

21
Nevertheless, it should be noted that this information alone is generally not exhaustive for the

development of an adequate set of input data. So, few supplementary criteria, to those reported in

the manual, have been fixed, as result of experience, in the attempt to set up a "homogeneous"

nodalization, that is to avoid imbalance in the distribution of hydraulic and thermal meshes. Of

course, the achievement of this objective, requires a good user knowledge of the reference facility

characteristics. Moreover, the prevision of the phenomena to be simulated in the calculation can also

have a role in this context. Compromises apply in the choice of number of nodes: on the one hand

there is the need to develop a model adherent to the geometric and material particularities of the

physical system, on the other hand computer capabilities (essentially CPU time) limit the maximum

number of nodes.

Two limits have been fixed for the linear dimension of nodes: all'the volumes should have their

flow lengths comprised between 0.5 and 1.0 m (with the exception of core stack, much more

detailed, of the descending zone of the SG U-tubes and of the pressurizer and accumulator surge

lines, nodalized by 2.0 m length nodes). With regard to conduction heat transfer, the distance

between neighboring mesh points inside structures must be less than 5 mm in each case, up to the

lower limit of few tenths of mm used for heated rods and steam generator U-tubes. In the subdivision

of volumes and slabs the position of instrumentation has been considered.

The following choices have been made with regard to code options:

* thermodynamic non-equilibrium is allowed in all control volumes;

* the smooth area change for all the junctions where it is allowed (i.e. excluding the motor valves);

" the stratification option is used in the junctions of the hot legs and cold legs horizontal parts.

3.3 SPES nodalization description

The Relap5/Mod3 nodalization for the SPES facility is shown in Fig. 5. The correspondence

between the zones of the facility and the nodes of the code model is presented in Tab. 4. In this table

the facility is divided in zones, composed by various hydraulic elements. These components are

reported in the table according to flow paths in nominal conditions. Number and type of the

hydraulic nodes are indicated in the table itself.

The utilized code resources for the SPES nodalization are summarized in Tab. 5. In particular,

the number of hydraulic components and of heat structure are reported.

Hereafter some significant aspects of the developed nodalization are summarized.

The vessel model consists of 45 hydraulic components which are connected through 48

junctions.

The heat structures used in the vessel model are made up of 78 heat slabs subdivided in:

* 24 active structures for the heaters exchanging heat with the pipe component 130 (composed by

12 volumes), where the overall power is dissipated: two stacks of 12 slabs simulate the three hot

rods and the remaining 94 rods of the core bundle;

* 4 internal non-active structures simulate the connection zones (in the lower part and in the upper

part of the bundle) exchanging heat with the branch components 100-01, 110-01, 120-01 and

140-01, where no power is assumed to be dissipated;

* 50 heat slabs simulate the vessel structures; in 19 over 50 slabs the heat exchange with the

environment is imposed.

22
! : -0.4- TKDFJU*SNGLJM vwrrmptvlvTyi'&VJu*:ý]

Fig. 5: RelapS/Mod3 nodalization of Spes facility

23
GENERAL ZONE NAME NUMBER TYPE

135 BRANCH

DOWNCOMER 125 BRANCH

REGION 115 PIPE

105 BRANCH

100 BRANCH

PRESSURE LOWER PLENUM 110 BRANCH

VESSEL 120 BRANCH

112 PIPE

LP-UP BYPASS 113 SNGLJUN

114 PIPE

CORE 130 PIPE

REGION 140 BRANCH

UPPER 150 BRANCH

PLENUM 160 BRANCH

170 BRANCH

UPPER HEAD 180 BRANCH

190 PIPE

DC - UH 155 SNGLJUN

BYPASS 145 PIPE

VESSEL NOZZLE 200(300) [4001 BRANCH

HOTLEG 210(310) [4101 BRANCH

LOOP 1 SG INLET PIPE 220 (320) [4201 PIPE

(LOOP 2) [LOOP 31 SG INLET JUNCTION 225 (325) (4251 SNGLJUN

PIPING SG OUTLET JUNCTION 235 (335) [4351 SNGLJUN

SG OUTLET PIPE 240 (340) [4401 PIPE

LOOP 250 (350) [4501 BRANCH

SEAL 260 (360) [460] PIPE

PRIM. COOLANT 270 (370) [470] PUMP

PUMP

COLD LEG 280 (380) [480] BRANCH

290 (390) [4901 BRANCH

SURGE LINE 010 PIPE

015 BRANCH

020 BRANCH

PRESSURIZER PRESSURIZER VESSEL 025 PIPE

030 BRANCH

035 BRANCH

PRZ LEVEL 045 TMDPJUN

CONTROLSYSTEM 040 TMDPVOL

PRZ PRESSURE 065 TRPVLV

CONTROLSYSTEM 060 TMDPVOL

PORV 075 MTRVLV

070 TMDPVOL

PRESSURIZER 085 TMDPJUN

LEAK 080 TMDPVOL

Tab. 4 (part 1): Relap5/Mod3.2 nodalization - correspondence between code nodes and

hydraulic zones

24
GENERAL ZONE NAME T mNmBER I TYPE

U -TUBE 230 (330) r4301 PIPE

SG1 (2) (31

SECONDARY SIDE

RISER 500 (600) [7001 PIPE

UPPER PLENUM 505 (605) (705] BRANCH

SEPARATORS 510 (610) [7101 SEPARATR

STEAM DOME 520 (620) [700 BRANCH

530 (630) [7301 BRANCH

DOWNCOMER 540 (640) [7001 BRANCH

560 (660) [7601 BRANCH

570 (670) [7701 PIPE

DC-RISER 575 (675) [7751 SNGLJUN

CONNECTION

590 (690) [7901 TMDPVOL

FEEDWATER LINE 591 (691) [7911 TMDPJUN

565 (665) [765] PIPE

EFW 592 (692) [792] TMDPVOL

SYSTEM 593 (693) [7931 TMDPJUN

TRANSIENT STEAM 581 (681) [781] TMDPVOL

LINE

(PRE. CONTR. SYSTEM) 580 (680) [7801 MTRVLV

525 (625) [7251 PIPE

STEADY - STATE 582 (682) [7821 TMDPJUN

STEAM LINE 583 (683) [7831 TMDPVOL

594 (694) [7941 TMDPVOL

LEVEL 595 (695) [7951 TMDPJUN

CONTROL SYSTEM 596 (696) [7961 TMDPVOL

597 (697) [7971 TMDPJUN

SAFETY 585 (685) [7851 TMDPVOL

RELIEF VALVE 584 (684) [7841 MTRVLV

SG LEAK 586 (686) [786] TMDPVOL

587 (687) [7871 MTRVLV

BREAK BREAKVALVE (383) TRPVLV

BREAK VOLUME (384) TMDPVOL

LPIS LPIS JUNCTION 278 [478] TMDPJUN

LPIS TANK 277 [4771 TMDPVOL

ACCUMULATOR 281 [4811 MTRVLV

VALVE

ACCUMULATOR ACCUMULATOR INJ 282 [482] PIPE

SA ACCUUTOR C C MLAN E 1 284 [4841 ACC

Tab. 4 (part 2): RelapS/Mod3.2 nodalization - correspondence between code nodes and

hydraulic zones

25
PARAMETER VALUE

1. NUMBER OF NODES

- primary side 165

- secondary side 99

- total 264

2. NUMBER OF JUNCTIONS

- primary side 169

- secondary side 102

- total 271

3. NUMBER OF SLABS

- primary side 224

- secondary side 75

- total 299

4. OVERALL NUMBER OF MESH POINTS 1615

5. NUMBER OF CORE ACTIVE STRUCTURES 24

6. HEAT TRANSFER AREA (m2)

- core region 10.596

- steam generator U-tubes 35.417

7. NUMBER OF MESH POINTS

- core slabs 240

- stem generator slabs 351

8. BYPASS FLOW PATHS

LOWER PLENUM - UPPER PLENUM

- area (m) 1.441-10"3

- total energy loss coefficient [11C (forward)/yl (reverse)] 82/13.5

DOWNCOMER - UPPER HEAD

- area (m2) 4.638.104

- total energ loss coefficient [I&. (forward)/iKI (reverse)] 3.5/3.5

9. OVERALL VOLUME (M3) 0.622

Tab. 5: RelapS/Mod3 Spes nodalization - overview of code resources

26
In the vessel model all the bypass flow paths reported in the facility description have been

modeled:

" bypass from lower plenum rto upper plenum simulated by the pipe components 112 and 114

connected through the single junction 113;

* bypass from downcomer top to upper head simulated by the pipe component 145 and the single

junction 155.

The three loops are almost equal in the nodalization (33 volumes, 32 junctions and 42 slabs) and

are differentiated for the pressurizer (placed in loop 2). For simplicity the loop 3 is not shown in Fig.

5; it has the same features of the loop 1.

The steam generator U-tubes are modeled asymmetrically, assuming that the largest portion of

the exchanged power between primary and secondary side occurs across the slabs of the rising part

of the package.

The pumps in the three loops are considered equal; different working conditions are achieved by

changing the shaft velocity. The related input two phase curve differences, which for completeness

have been considered in the nodalization, have been set equal to ones related to the LOBIIMod2

pumps.

Two additional systems can be noted in the pressurizer nodalization:

• a time dependent volume and related trip valve (component 60-01 and 65-01 respectively);

" a time dependent junction and related time dependent volume (components 45-01 and 40-01

respectively).

Both are control systems. The former system allows the primary side pressure to remain

constant in the steady-state period. The latter system maintains at an assigned value the liquid level

inside the pressurizer. The temperature of the fluid possibly injected by this system corresponds to

the saturation conditions inside the pressurizer..

Still, the black structures inside the pressurizer model represent the internal heaters; they

simulate in the code model also the external heaters installed in the facility.

The motor valve 75 and the related time dependent volume 70-01, connected to the top of the

pressurizer, simulate the PORV system, while the time dependent volume 80 and the time dependent

junction 85 simulate the leak detected in the pressurizer in a previous SPES test.

The slabs with an asterisk represent the zones where the heat losses to environment are

considered.

Accumulators and LPIS simulator are connected with the cold legs of the two intact loops.

The secondary side nodalization of the three steam generators are equal both concerning the

hardware of the facility and the control system (33 nodes, 34 junctions and 25 head slabs): in

particular the volume identification number can be obtained by changing the first digit in the loop I

related one (6 in place of 5 for loop 2 and 7 for loop 3). So only one nodalization will be described

hereafter.

Five zones can be recognized in each steam generator:

1. the downcomer, consisting of a single stack of nodes (the two external downcomers are gathered

in a simple pipe component);

2. the riser zone, essentially including the U-tubes;

3. the top of the vessel, including the separator, the dryer and the steam done regions;

4. the steam line downstream the dome of each SG, simulated with the pipe component 525-01, the

motor valve 580 and time dependent volume 581. This last component is also utilized like a

pressure control volume imposing constant pressure in the volume itself

5. the feedwater line connected to the top of the downcomer, simulated with the pipe component

565-01, time dependent junction 591 and the time dependent volume 590.

The degree of detail of the nodalization is commensurate to what considered-in the primary

loop. In particular, the heights of the riser volumes are the same as the minimum between the heights

of the rising and descending corresponding nodes of the primary side U-tubes.

27
The components 510-01 simulates the separator that is necessary in the code model in order to

achieve quality equal to one in the steam dome.

The pre-heaters are not simulated in the code model

A relatively large number of control volumes are connected with the steam generators; the

following functions are accomplished:

* feedwater injection and steam line previously described;

" EFW injection: simulated with the time dependent volume 592 and with the time dependent

junction 593 (used only in the steam generator of the loop 1);

" SRV safety system: simulated with the time dependent volume 585 (safety tank) and with the

motor valve 584 (safety valve);

" liquid level control system: realized through two time dependent volume components (596 and

594), each one connected with one time dependent junction (597 and 595 respectively). This

system assures constant value for steam generator downcomer liquid level during the steady-state

period.

3.4 Nodalization qualification

A nodalization representing an actual system (Integral Test Facility or plant) can be considered

qualified when:

- it has a geometrical fidelity with the involved system;

- it reproduces the measured nominal steady state condition of the system;

- it shows a satisfactory behavior in time dependent conditions.

Taking into account these statements, a standard procedure to obtain a "qualified nodalization"

has been defined, ref. [13].

The qualification process consists of two main phases:

1) steady state level: the nodalization is qualified against data available from nominal stationary

conditions measured in the simulated system. To this aim:

a) relevant geometrical parameters of the facility (e.g. volume, heat transfer area, elevations,

pressure drops distribution etc.) are compared with the input data and the differences among

them must be acceptably small. The adopted acceptability criteria are reported in the first part

of Tab. 6; the accomplishment of criteria, as far as volume versus height curve is concerned,

results from Fig 6.

b) the nominal steady state conditions are simulated with a code running (a hundred seconds

time interval is considered acceptable to reach correct steady state values); significant

parameters are selected and compared with the measured results. A parameter is considered

as significant when it is of major relevance in determining the plant behavior and can be

reliably measured. The adopted acceptability criteria for this step are reported in the second

part of Tab. 6; the accomplishment of criteria, as far as the distribution of pressure (or

pressure drops), in the primary loop is concerned, results from Fig. 7: criterion 19 of Tab. 6 is

fafilledi i

* pressure at SG inlet location is taken as reference

* errors (not discussed in the present frame) in pressure drops measurement are

considered.

2) transient level: the nodalization is tested in time-dependent conditions reproducing the available

experimental transients. This phase also includes the procedure for the qualitative and the

quantitative (through the application of the FFT based method) evaluation of the code accuracy,

necessary to demonstrate the acceptability of the code transient performance. The demonstration

of the quality of the nodalization at the transient level, before application to the reference

calculation (SP-SB-03 in this case), involves at least one among the following steps:

28
a) perform a "K, scaled" calculation aiming at the comparison between the nodalization

performance and experimental data in another facility (proper scaling factors must be

adopted to fix initial and boundary conditions);

b) compare results of the nodalization with experimental data different than those object of the

reference calculations (these can be operational transient data in the case of a Nuclear

Power Plant);

c) compare the results of the nodalization with calculations data coming from a previously

qualified nodalizatioa

The idea of the "Kv-scaled calculation" (item a) comes from the objective to comparing

calculated data with experimental data before adopting any nodalizations (i.e. including NPP

nodalization) for any kind of calculation (code assessment, licensing, etc.). In this frame, adopting

proper scaling criteria (time preventing, volume/power scaling)a comparison can be made between

predicted and experimental data in the area of PWR and BWR. This must be used to detect

nodalizations and user choice inadequacies. Correction of errors or deficiencies leads to a "on

transient" qualified nodalization ready to be used for other purposes.

The acceptability constraints for the FFT (i. e. 0.4 for Average Accuracy and 0.1 for the primary

pressure) must be fulfilled in any case.

The qualification process, summarized above, has been applied to the nodalization of Spes

facility.

As concerns the first phase (steady state level), the steady state acceptability criteria previously

defined (reported in Tab. 6) have been verified; in particular, the comparison between the calculated

and the measured volume vs. height curve and the distribution of pressure drops along the length are

reported in Figs. 6 and 7, respectively.

The second part of the qualification process (transient level) has been conducted through the

step b) and c) described above: in the first case the International Standard Problem 22, refs. [14] and

[15], has been in considered, while in the second case the previous simulation with the version

RelapSIMod2, refs. [5] and [16], has been utilized (see also below).

It is to be mentioned that the application of the FFT based methodology has been exhaustively

performed in the RelapS/Mod2 simulation of SP-SB-03 [16] and it was not repeated in a systematic

way for the Relap5/Mod3.2 simulation. No important differences related to any of the finding of the

Relap5/Mod2 analyses are expected.

29
QUANTITY ACCETPTABLE ERROR

1 Primary circuit volume 1%

2 Secondary circuit volume 2%

3 Non-active structures heat transfer area (overall) 10 %

4 Active structures heat transfer area (overall) 0.1%

5 Non-active structures heat transfer volume (overall) 14 %

6 Active structures heat transfer volume (overall) 0.2 %

7 Volume vs. height curve (i.e. "local" primary and 10 %

secondary circuit volume)

8 Component relative elevation 0.01 m

9 Axial and radial power distribution (o) 1%

10 Flow area of components like valves, pumps orifices 1 %

S11 Generic flow area 10%

12 Primary circuit power balance 2%

13 Secondary circuit power balance 2%

14 Absolute pressure (PRZ, SG, ACC) 0.1%

15 Fluid temperature 0.5 % (**)

16 Rod surface temperature 10 K

17 Pump velocity 1%

18 Heat losses 10%

19 Local pressure drops 10 % (A)

20 Mass inventory in primary circuit 2 % (AA)

21 Mass inventory in secondary circuit 5 % (ýA)

22 Flow rates (primary and secondary circuit) 2 %

23 Bypass mass flow rates 10%

24 Pressurizer level (collapsed) 0.05 m

25 Secondary side or downcomer level 0.1 m(M)

(0) The % error is defined as the ratio Ireference or measured value - calculated valuel

I reference or measured value

The "dimensional error" is the numerator of the above expression

(00) Additional consideration needed

(*) With reference to each of the quantities below, following a one hundred s "transient-steadystate" calculation, the solution must be stable with an inherent drift < 1% / 100 s.

(**) And consistent with power error

(A) Of the difference between maximum and minimum pressure in the loop.

(AA) And consistent with other errors.

Tab. 6 - Criteria for nodalization qualification at the steady-state leveL

30
.0-

100

90

80

70

60

50

40

30

20

10

0

0 20 40 60 80

Height (%)

100

Fig. 6: Comparison between measured and calculated volume vs. height curve

CC

k.

C

C

0.

15.34

15.32

15.30

15.26

15.26

15.24

15.22

15.20

15.18

15.16

0 5000 10000 15000 20000 25000 30000 35000 40000 45000

Length (mm)

Fig. 7: Comparison between measured and calculated DP vs. length curve

31

4. ANALYSIS OF POST-TEST CALCULATION RESULTS

Three main calculation types can be distinguished in a meaningful code assessment process:

a) 100 s steady state;

b) reference calculation results;

c) results from sensitivity studies.

It may be noted that item a) may constitute a part of the nodalization qualification process,

described in the previous chapter, however, the fulfillment of criteria reported in Tab. 6 is necessary

each time a new experiment is considered and before starting transient calculations by using the

previously qualified nodalization.

The reference calculation results, item b), must outcome from the qualified nodalization and

satisfy qualitative and quantitative accuracy related criteria. The reference calculation is not "the

best" calculation achievable by the code. In order to get the reference calculation, boundary and

initial conditions of the considered experiment (ie. input data for the reference calculation) may be

changed within their uncertainty ranges; if a user choice is introduced (e.g. changes in noding detail),

its validity and acceptability must be checked by repeating the nodalization qualification process.

Sensitivity analyses, item c), must be carried out to demonstrate the robustness of the

calculation, to characterize the reasons for possible discrepancies between measured and calculated

trends that appear in the reference calculation, to optimize code results and user option choices, to

improve the knowledge of the code by the user.

The attention is focused hereafter toward the analysis of the reference calculation results, item

b), considering that steady state calculation, item a), is part of the nodalization qualification process

and sensitivity analyses, item c), can be designed following the analyses at the previous step. Typical

results are provided in relation to the three steps.

When calculating the quantitative accuracy, twenty-three time trends have been selected in

relation to which experimental data exist: these are assumed to be the minimum number of measured

quantities that fully describe the experimental scenario. The related list is given in the first column of

Tabs. 11, 13 and 14.

When calculating qualitative accuracy, including the comparison between time trends, reference

is made to the same list (e.g. Apps. 1 and 2) of Tab. 13 with the following changes:

* quantities 04 and 03 in Tab. 13 are both reported in Fig. 3; so quantities from 05 to 23 are shown

in Figs. 4 to 22, respectively;

* the following quantities have been added to the comparison: pressure drop across DC-UH bypass,

pressure drop in the U-tubes ascending leg (also a measure of liquid hold-up in the U-tubes), core

inlet flow rate, pressure drop in cold leg, mass flow rate in SG downcomer, hot leg mass flow

rate; these are reported in Figs. from 23 to 28, respectively. Fig. 29 has been added to give an

overall view of the system performance (primary and secondary pressure together).

4.1 Steady State calculations

A steady state calculation, by running the code with the TRANSNT (transient) option for 100 s

has been completed. This constitutes the final step of the nodalization qualification process at steady

state level.

The related results are shown in Tab. 7 and in App. 1. In both cases, resulting values are

compared with experimental data. In the case of Tab. 7, for completeness, the data calculated by

RelapS/mod2 are included as taken from ref. [5].

It may be noted that the data in Tab. 7 deal with most of the parameters imposed for the

nodalization qualification process (Tab. 6): the values in the table have been taken from the code

33
output at 100. s. The time trends above identified are part of the App. 1, numbering of figures is

different owing to the obvious lack of time trends dealing with ECC and break flow rates.

The analysis of data brings to the following conclusions:

- the criteria for nodalization qualification are fulfilled, though the complete comparison between

data in Tab. 7 and in App. 1 with acceptability criteria has not been done owing to the lack of

experimental data; in addition, some of the criteria can be matched by considering sums or

combinations of values from Tab. 7 (e.g. the primary circuit power balance can be obtained by

considering data at items 1, 4, 14, 16 and 17); still, the error on bypass flow rate, can be better seen

by considering the errors in fluid temperatures owing to the fact that the direct experimental

information about bypass flow rate is uncertain (measurement error not available);

- the calculated values are stable as it results from Figs. I to 26;

- differences between Relap5/mod2 and Relap5/mod3.2 codes results are negligible;

- discrepancies between measured and calculated values of heater rod temperatures, Figs. 8 to 10 in

App. 1, come from the position of thermocouples and from generic ekperimental error (the

calculation result refer to the surface, the experimental data are taken slightly inside the surface, the

error almost disappears at low linear rod power, during the transient);

- the discrepancy in Fig. 14 (pressure drop across steam generator) is attributed to the experimental

error and to the position of the measurement pressure taps not accounted for by the calculated

results;

- the last explanation is also valid in the cases of pressure drops in Figs. 16, 17, 19, 20 and 21; the

unknown position of pressure taps is specifically valid in the case of Fig. 20;

- the discrepancy in Fig. 23, related to the recirculation mass flow rate in the steam generator, can

also be originated by a measurement error, however, in this case tuning or adjustments of steady

state code results was considered unnecessary owing to the low influence that this parameter has in

the selected transient (early main coolant pump and feedwater trips occur).

4.2 Reference calculation results

The post-test calculation was performed starting from the input deck suitable for Relap5/Mod2.

A 'blind6 post test was performed by Relap5/Mod3.2 constituting the reference calculation for this

study (label S3RO); the related time trends and significant single valued parameters are reported,

together with experimental data, in App. 2 and in Tab. 8, respectively. For clarity reasons, selected

time trends from App. 2 are shown in Figs. 8 to 13 below.

The comparison of SP-SB-03 test with the high power experiment SP-SB-04, showed that,

notwithstanding the different boundary conditions, the same key phenomena characterize the two

tests. The results of the related Relap5/Mod3.2 calculations are very similar and the considerations

reported in ref. [20] are almost completely valid also for the SP-SB-03 test simulation.

A comprehensive comparison between measured and calculated trends or values was performed,

including the following steps:

a) comparison between experimental and calculated time trends on the basis of the 29 variables

introduced above (App. 2);

b) comparison between values of quantities characterizing the sequence of resulting events, Tab. 8;

c) qualitative evaluation of calculation accuracy on the basis of the phenomena included in the CSNI

matrix, ref. [17], as given in Tab. 9;

d) qualitative evaluation of calculation accuracy on the basis of the Relevant Thermalhydraulic

Aspects (RTA, also used for code uncertainty derivation, e.g. ref [6]), as given in Tab. 10;

e) quantitative evaluation of calculation accuracy, utilizing the FFT based method (FFIBM),

described in refs. [7] and [18], see also App. I in ref [20], as given in Tab. 11.

34
Comments related to items a) and b) are given below, distinguishing groups of homogeneous

variables, while the discussion about items c), d) and e) is given in sect. 4.2.1. An asterisk (*)

identifies the items that are subject to sensitivity analyses.

Absolute Pressures

The primary system pressure is well predicted by the code (Fig. 8 below and Fig. 1 in App. 2),

apart from the saturated blowdown phase where it is slightly underestimated. The phenomenological

phases (e.g. subcooled blowdown, saturated blowdown and steam flow from the break) can be easily

recognized from the calculated time trend.

The steam generator pressure is slightly underpredicted as shown in Fig. 2 of App. 2; reasons for

this appear connected with the overestimation of heat transfer between primary and secondary sides

and, eventually, with overestimation of heat losses from secondary side to the environment; a role

could be held in this connection, by minor discrepancies (undetected, so far) between measured and

calculated closure times of feedwater and steam lines valves.

The accumulators pressure is well predicted, starting form the accumulator injection time. The

final pressure measured for one of the accumulators is lower than the calculated value, as results

from Fig. 3 in App. 2. Reason for this cannot be understood from the experimental data base;

apparently, the isolation valve closed with some delay.

Fluid temperatures

Measured and calculated fluid temperatures are compared in Figs. 4, 5, 6, and 8 of App. 2, the

last one related to the steam generator and the other ones related to the primary circuit.

Core inlet fluid temperature is qualitatively well predicted (Fig. 4); the underprediction of

temperature values is connected to the underestimation of the primary pressure and probably (this

has not been controlled) to the experimental procedure adopted to reach the initial conditions. The

predicted core outlet fluid temperature presents two peaks in correspondence to the two core level

depressions, early predicted by the code (see also below). The superheating is larger than in the

experiment and the position of the thermocouple strongly affects this time trend. This is specifically

true for the upper head fluid temperature where a very high superheating is measured; in this case, it

seems evident that the thermocouple gives a measure of the structural mass temperature starting

from about 200 s into the transient, i.e. following the emptying of the upper head.

The underprediction of the fluid temperature in the bottom of the steam generator downcomer

(Fig. 8 in App. 2) derives from the same reasons discussed for the pressure.

Mass flowrates

The measured values of break flowrate (Fig. 9 below and Figs. 7 and 9 in App. 2), the ECCS

flowrate (Fig. 10 below and Fig. 10 in App. 2), core inlet (Fig. 25 in App. 2), hot leg mass flowrate

(Fig. 28 in App. 2) and the steam generator downcomer flowrate (Fig. 27 in App. 2) are compared

with the respective calculated trends.

Break flow rate is well predicted up to 500 into the transient, after that is overpredicted (*);

however, the related error can be considered within the uncertainty bands.

ECCS flowrates are clearly overpredicted; the reason for this seems connected with the

experimental error" (*).

+ A data base for an oqaiment typically oonsists of seve hundreds time trends (up to 2000s) and hundreds of point

values or time functions for boundary and initial conditions, plus indications about status of valves, pumps and of

various systems; the data base, as in the present case, is judged as qualified in a global sense, and it is certainly

suitable for code assessment purposes. However this does not imply that all the supplied values are unaffected by more

or less large errors. Typical examples, in the present data base are constituted by the core mass flowrate that is

inconsistent with data for hot legs flowrate , and by accumulators integral mass flowrate that is inconsistent with the

supplied data for accumulators injected mass and primary system mass inventory.

35
The LPIS intervention is slightly anticipated, because the early prediction of the heater rods

temperature excursion.

The error in core inlet flowrate appears a consequence of instrumentation inadequacy as also

results from observing the good agreement between measured and calculated trends of hot leg

flowrates. Oscillations appear in the calculated trends (mostly one of the loops) of hot leg flow rates,

starting from about 400 s into the transient; these could be explained with the "siphon condensation

mechanism": the siphon condensation is a natural circulation mode that appears in the primary side

loop of a PWR when mass inventory value is about 70% of the initial mass. In this condition steam

coming from the core, condenses in the rising part of U-tubes; however due to CCFL (counter

current flow limitation) at U-tubes inlet, the condensate does not drain back to the core, and liquid

level formation occurs in the ascending side of U-tubes (m this phase zero flow cold leg occurs).

This situation is valid until the liquid level reaches the top of the U-tubes, when the siphon effect

occurs, causes liquid draining to cold legs ant to the core. The cycle may repeat several time in a real

siphon. Liquid accumulation may be due either to condensation or de-entrainment of droplets carried

by the two phases mixture.

Following the steady state misprediction (already discussed), steam generator downcomer

flowrates (experimental and calculated values) substantially agree and achieve a value close to zero.

Residual Mass

A good agreement between measured and calculated trends can be observed from Fig. 14 of

App. 2, apart from the last part of the transient, where the residual mass is overpredicted owing to

the early intervention of the LPIS. The good prediction of the primary side mass is at the origin of

the conclusions previously drawn, connected with reliability of ECC related instrumentation.

Pressure drops

Pressure drops between different points of the primary circuit are considered in the comparison,

e.g. Figs. 17, 19, 20, 22, 23, 24 and 26 in App. 2. All of the comparisons, with different extent,

suffer of the limitation already explained in sect. 4.1 (pressure taps not coincident with the center of

the volumes of the nodalization).

The transient comparison is acceptable in relation to all the considered trends also having in

mind the above limit. Deep studies of local phenomena could be carried out, starting from those

trends, to improve the comparison leading to a tuned input deckl. This has not been among the

purposes of the present activity.

Levels

The pressurizer level (Fig. II below and Fig. 21 in App. 2) is very well predicted in the

calculation, testifying of the good prediction of the subcooled blowdown flow rate.

Core collapsed level constitutes a critical quantity during this experiment, as the level variations

are directly connected with the occurrence of core dryout. The experimental trend (e.g. Fig. 12) is

characterized by a peak at the transient beginning, when a short duration dryout is also observed;

another core level depression occurs starting from about 1600 s into the transient leading to the final

dryout, quenched by LPIS injection. The trend of this variable is strongly affected by the distribution

of pressure drops along the loop that also influence the occurrence of threshold phenomena like loop

seal clearing.

Core level is quite well predicted (Fig. 12 below and Fig. 15 in App. 2); however, two main

discrepancies can be identified (*): the first core level depression is underpredicted by the code,

although at the right time; the early stop of the accumulator intervention shifts of about 100 s the

appearance of the level depression at the end of the transient.

36
Rod Surface Temperatures

When analyzing the rod surface temperature trends, the three-dimensional situation in the core

must be considered, as described into detail in ref. [8].

Representative experimental data at three core levels have been selected for the present

comparison, distinguishing in the axial sense, the core bottom, the core middle and the core top

regions (Figs. 11 to 13, respectively in App. 2, and Fig. 13 below related to the top region).

Predicted rod surface temperature trends follow qualitatively well the measured values. The first

dryout, appearing in the middle and high core regions (Figs. 12 and 13 in App. 2), is predicted by the

calculation only in the high level, with a delay of about 70 s and the underestimation of the peak

cladding temperature. The last dryout situation is quite well predicted by the calculation, although

the dryout occurrence is anticipated and the temperature excursion is 50 K lower than in the

experiment (at the high level); this dryout does not appear in the bottom core region neither in the

experiment nor in the calculated results.

37
18.0

14L0 000 SSo3P-2045

MA OMP-3043

10.0

8.0

4.0

2.0

0.0 " I IL ..

-200 0 200 400 600 800 1000 1200 1400 1600 1800 2000 ,2200

limo(s)

Fig. 8: SPES post test SP-SB-03 (reference calc.) - primary and secondary pressure

1200

1000

SPES

COLD LEG BREAK LOCA

RELAPSMOM3.2

.-:T30ABREAJGNTFLOW

YYY SS0381F

,

600

400

200

0

-200

I-x

0 250 500 750 1000 1250 1500 1750 2000 2250 2500 2750

"nin. (s)

Fig. 9: SPES post test SP-SB-03 (reference calc.) - integral break flow rate

38
400.

350.

300.

250.

S

U;

200.

160.

50.

-200 0 200 400 600' 800 1000 1200 1400 i160 uoo 2000

TFpBe (a)

Fig. 10: SPES post test SP-SB-03 (reference calc.) - ECCS integral flow rate

2200

I

450

4.000

3.500

3.000

2.OOO

2.500

2.000

1.500

1.000

0.000 -- -

4.500-200 0

SPES

COLD LEG BREAK LOCA

RELAPSJMOD3.2

J i --

XX: T30ACNTRIYAFH

YYY SS03L-M OP

I I I * I

. I I I I I I

200 400 600 800 1000 1200 1400

Tma (S)

1600 1800 2000 2200

Fig. 11: SPES post test SP-SB-03 (reference caic.) - pressurizer level

39
I

4.500 4.000

4.500

4.5OO0

2.5W0

2.000

1500

1.000

0.500

0.000-200

COLD LEG BREAK LOCA

RELAP5jIAOM32

)OCTWACNTRLVAR155*

YYY SB0*L.CL*

I

0 200 400 60 00 1000 1200 1400 1600 1800 2000 2200

7ime (S)

Fig. 12: SPES post test SP-SB-03 (reference calc.) - core level

7SO.

70a.

g6M0

55M

-200 0 200 400 600 800 1000 12W 1400 1600 18W 2000 2200

lMeO (S)

Fig. 13: SPES post test SP-SB-03 (reference calc.) - rod surface temperature (high level)

40
QUANTIY UNIT EXP CALC R5/M2 CALC RS/M3.2

_(ost-test)

1) Core power kW 768 766 769

2) Pressurizer pressure MPa 15.06 15.1 15.1

3) Pressurizer level m 3.23 3.23 3.16

4) Core mass flow rate kg!s 4.21 4.2 4.52

5) Core bypass mass flow rate kgs 0.099 0.096 0.11

6) DC-UH bypass mass flow rate [kgs 0.034 0.05 0.06

7) Primary pumps speed rad/s 38.6 40.2 40.1

36.7 40.2

- 40.2

8) Core inlet temperature K 558.1 554.5 557.9

9) Core outlet temperature K 586.7 587.1 585.6

10) Core AT K 28.6 32.6 30.7

11) Upper head temperature K 543 543 547

12) Primary mass k9 423 425 425

13) Acc. liquid temperature K 319.7 321 322

320.8

14) Secondary pressure SG MPa 6.94 6.94 6.94

6.87

6.88

15) SG downcomer level m 11.5 11.3 12.2

11.3

11.3

16) Feedwater temperature K 437.6 436 434

437.8 436 441

440.1 436 433

17) Feedwater flow rate kg/s 0.095 0.097 0.097

0.093 0.097

1__ 0.0965 0.097

18) Total primary side heat losses kW 150. 180 155

19) Secondary side heat losses kW 61.4 71 71

Tab. 7: Comparison between measured and calculated (RelapS/Mod2

relevant initial and boundary conditions

and RelapS/Mod3.2)

41
*,

CS

.o

*0

CS

goa

EXP "T30A S302 S303 S304 305 -301 

(base) ,,,

Break opening 0 0 0 0 0 0 

0

Scram power curve enabled 6.5 0 0 0 0) 0 

0

Start of main coolant pumps coast down and 0(5) 6 6 6 6 6 

6

its duration

Main steam line valve closure 6.5 5 5 5 5 4 

5

Feedwater valve closure 14.5 5 5 5 5 4 

5

Upper plenum in saturation condition 15 12 11 12 12 10 10

Pressurizer emptied* 12 18 18 18 19 17 19

Break two phase flow 112 92 94 95 98 90 105

First dryout 112 167 167 

-

-

Loop seal clearing 110 485 482 No No 501 545

loop' 1-3 no no No No no no

No no no 609 509 no no

Occurrence of minimum primary side mass 355.5 345 362 362 360 351 338

1522 1278 1277 1397 1577 1256 1328

PrImary-secondary pressure reversal 115-138 162 161 158 164 140 185

Second dryout 

-

-

-

-

- 310

Accumulators injection start 335.5 339 340 338 356 304 337

Accumulators injection stop 3)903 757 752 868 909 781 821

M1)1058

Final dryout 1322.5 1184 1182 1214 1369 1142 1218

LPIS start 1522.5 1277 1276 1401 1579 1256 1327

Final rewetting 1569.5 1353 1354 1461 1630 1331 1393

End of test 2034 2000 2000 2000 2000 2000 2000

* level equal to 0.2 

m
4.2.1 Qualitative and quantitative accuracy evaluation

Qualitative accuracy

A part of the qualitative accuracy evaluation has already been completed, consisting of the

consideration in sect. 4.2, leading to starred items that are at the basis of the design of sensitivity

calculations.

The qualitative accuracy evaluation here discussed is based upon a systematic procedure

consisting in the identification of phenomena (CSNI list) and of RTA. In both cases five levels of

judgment are introduced (E, R, MK U, and -) whose meaning is detailed in the notes of Tab. 9 and in

App. 1 of ref. [20]. The related results are reported in Tabs. 9 and 10, where for completeness the

information related to Relap5/mod2 results are given.

A positive overall qualitative judgment is achieved if 'U' is not present; in addition, the

parameters characterizing the RTA (i.e., SVP = Single Valued Parameter, TSE = parameter

belonging to the Time Sequence of Events, IPA= Integral Parameter and NDP = Non Dimensional

Parameter) give an idea of the amount of the discrepancy.

In the present case the following conclusions could be reached:

a) no 'U' mark is present;

b) all RTA of the experiment are present in the calculated data

c) the accuracy evaluation by adopting RTA and Key Phenomena, supports the conclusion that

the calculation is qualitatively correct.

Quantitative Acacy

The positive conclusion of the qualitative accuracy evaluation, makes it possible addressing the

quantitative accuracy evaluation. To this aim a special methodology, developed at University of Pisa,

and widely used has been adopted.

The methodology is based upon the use of the Fast Fourier Transform (e.g. ref [19]); its main

features are detailed in App. 1 of ref. [20].

The results of the application of the method are given in Tab. 11, where again the information

related to Relap5/mod2 calculation is given too. The conclusions from the quantitative accuracy

evaluation analysis are as follows:

a) the achieved results are well below the acceptability threshold both in relation to the overall

accuracy (AA = 0.29 compared with the acceptability limit of 0.4) and the primary system

pressure accuracy (AA = 0.065 compared with the acceptability limit of 0.1);

b) the achieved results appear slightly better than those obtained by Relap5/mod2.

Definitely, the documented reference calculation is acceptable from the code assessment point of

view; i.e. the code is positively assessed in relation to its capabilities to predict this kind of transient.

Design of sensitivity calculation

Following the performed qualitative and quantitative accuracy evaluation there is no need to

perform additional calculations.

Therefore, the planned sensitivity analyses are carried out with the main purpose of

understanding the code behavior (including the robustness of the present solution) rather than

following needs from accuracy evaluation. Nevertheless, emphasis is given to the findings of sect. 4.2

and the following objectives for the analyses are established:

1) prediction of break flow rate;

2) prediction of the core level.

43
PHENOMENA FACILITY EXPERIMENT JUDGEMENT JUDGEMENT

OF CALC. OF CALC.

SPES SP-SB-03 RELAPS/M2 RELAPIM3.2

Natural circulation in one-phase 0 + R R

flow

Natural circulation in two-phase 0 + R R

flow

Rflux odenser mode and + - M M

CCFL

Asymmetric loop behavior o + M M

Leakflow + + M M

Phase separation without mixture o -

level formation

Mixture Level and entrainment in + -

SG secondary sZide_____ ____

Mure level and entrainment in + + M M

the core

Stratification in horizontal pipes + -

Emer ycore cooling m g+ + R R

and condensation

Loop seal clearing 0o M M

Pool formation in upper plenum - + - CCFL

Core wide void and flow - distribution

Heat transfer in covered core 0 o R R

Heat transfer in partially + o R R

uncovered core

Heat transfer in SG primaryside 0 0 R R

Heat transfer in SG secondary o - /R. M/R

side

Pressurizer temaihdrulic + + E E

Surge line hydraulics (CCFL + -

choking)

One and two phase pump + -

behavior

Structural heat and heat losses + + R R

Non condensable gas effect on + -

leak flow

Phase separation in T-junctions + + M M

Separator behavior ....

Thrmaihydraulic nuclear ...

feedback

Boron mixing and transport - - -

For the test facility vs.

phenomenon:

o suitable for code assessment

+ limited suitability

- not suitable

For phenomenon vs. test:

o expimentally well defined

+ occurring but not well characterized

. not occurring or not measured

For phenomenon vs.

calculation:

E = Excellent

R = Reasonable

M = Minimal

U = Unqualified

- = Not applicable

Tab. 9: Judgment of code calculation performance on the basis of phenomena included in the

CSNI matrix

44
UMNIT M I CALC CALC Judgment

RTAM Pressurizer eptying

TE I emptyingtime* s 12 116 11 /BE

!scram time s 6.5 6.5 0 E/R

RTAM Steam generators secondary side behavior

TSE main steam line valve closure s 6.5 3.8 5 R/R

feed water valve closure s 14.5 3.8 5 R/R

SVP difference between PS and SS MPa 0.16 0.15 0.36 R/R

pressure at 100 s

RTA., Subcoolcd blowdown

TSE upper plenum in sat. conditions 15 12 12 FE/

break two phase flow 1 112 67 92 R/R

IPA break flow up to 30 s kg 89 123 85 [ R/E

RTA First dryout occurrence

TSE time of dry out s 112 157 167 R/R

peak cladding temperature K 658 645 589 E/R

SVP average linear power kW/m 1.11 0.8 0.8 V/E

maximm linear power kW/m 1.41 0.92 - R/

core power / primary mass kW/kg 1.92 2.22 1.76 R/E

NDP prima rmass / initial mass % 47 30 38 RIR

RTAM Rewet by loop seal clearing

TSE lime of loop seal clearing s no no no E/E

110 150 no E/M

no no no ,/E

time when rewet is completed s1 1175 180 R/R

RTAZ Saturated blowdown

TSE PS pressure equal to SS pressure s 115-138 140 1162 E/R

SVP break flow at 200 s kg/s 0.39 0.27 0.32 R/E

break flow at 1000 s 10.0 10.06 10.12 RIE

RTA: Mass distribution in primary side"

TSE time of minimum mass occurrence s 355.5 347 345 W/E

1522 1866 1278 R/R

SVP minimum primary side mass kg 110 73 108 RIE

95 71 101 RAE

av linear power at mm. mass kW/m 0.38 0.44 0.43 B/E

mininmm mass/ITrF Volume kgW 176.2 115 161.8 R/R

RT A: Accumulators behavior

TSE accumulators injection starts s 355.5 347 339 E/R

accumulators injection stops s 3) 903 903 757 E/R

1) 1058 1058 757 E/R

INDP mll~mmasslinitial Mas % 26 17 25 RAE primary massinit_ __ mass % 30 21 25 PIE

RTAM Final dr-yout occurrence

TSE time of dryout s 1322.5 1728 1184 R/R

peak cladding temperature K 706 703 714 EBE

SVP average linear power kW/m 0.29 0.26 0.29 E/E

core power/primary mass kW/kg 0.78 1.25 0.89 R/E

rate of rod temperature increase K/s 1.08 1.1 1.22 B/E

NDP primary mass/initial mass % 25 17 27 R/E

RTA: LPIS intervention

TSE LPIS start is 1522.5 1866 1277 R/R

final rewetting s 1569.5 1904 1353 R/R

NDP primary mass/initial mass % 22 17.8 126 R/E

* level equal to 0.2 m

Tab. 10: Judgment of code calculation on the basis of relevant thermalhydraulic aspects

45
PARAMTER RM_ R_3

AA WF AA WF

01 - PRZ pressure 0.07 0.06 0.065 0.072

02 - SG pressure - secondary side 0.13 0.05 0.168 0.042

03 - ACC pressure 0.16 0.05 0.097 0.060

04 - ACC pressure 0.078 0.073

05 - Core inlet fluid temperature 0.05 0.05 0.038 0.050

06 - Core outlet fluid temperature 0.06 0.03 0.052 0.034

07 - Upper head fluid temperature 0.69 0.07 0.709 0.054

08 - Integral break flow rate 0.08 0.03 0.122 0.053

09 - SG DC bottom fluid temperature 0.06 0.05 0.157 0.059

10 -Break flow rate 1.07 0.09 0.826 0.097

11 - ECCS integral flow rate 0.52 0.07 0.246 0.045

12 - Heater rod temp. (bottom level) 0.07 0.04 0.057 0.036

13 - Heater rod temp. (middle level) 0.3 0.04 0.297 0.036

14 - Heater rod temp. (high level) 0.59 0.04 0.530 0.031

15 - Primary side total mass 0.52 0.07 0.134 0.042

16 - Core level 1.13 0.06 0.964 0.083

17 - SGDC level 0.29 0.07 0.192 0.063

18 - DP inlet-outlet SG QL) 1.16 0.05 1.489 0.083

19 - Core power 0.29 0.11 0.187 0.107

20 - DP loop seal BL - ascending side 1.12 0.07 3.309 0.124

21 - DP loop seal BL - descending side 0.6 0.04 0.414 0.089

22 - PRZ level 0.14 0.12 0.235 0.070

23 - DP SG inlet plenum U tubes top IL 0.52 0.06 0.432 0.069

TOTAL 0.32 0.05 0.29 0.054

(*) Experimental or calculated variable trend missing from available data

Tab. 11: Summary of results obtained by application of FFT method to the selected

parameters for the reference calculation

46
4.3 Sensitivity calculations

Considering the reference calculation, a series of sensitivity analyses have been carried out,

addressing the items 1) and 2), reported in section 4.2. 1, and additional input parameters; these are

essentially user's choices that may have some effect in solving discrepancies leading to the same

items.

The characteristics of the performed calculations can be drawn from Tab. 12, together with the

results of the FFT methodology application (overall calculation and primary pressure). The summary

of the EFT results related to all the parameters for all the performed sensitivity calculations are given

in Tab. 13 and 14.

The comparison between calculated and measured trends for each sensitivity analysis is reported

in Appendix 3. In Figs. 14 to 23 the comparison of the sensitive analyses with the reference

calculation is shown for some parameters of interest (primary pressure, break flow rate, heater rods

temperature); more details are given hereafter.

a) Break flow rate

In order to obtain a better prediction of the break mass flow rate, the discharge coefficient at the

break junction has been decreased and set to 0.9, 0.8 and 0.75 (runs S304, S301 and S303,

respectively).

In the first case (discharge coefficient equal to, 0.9), the flow rate is overestimated starting from

100 s and the discrepancy with the experimental data is larger than in the reference case (see also the

AA value related to the break flow rate in Tab. 13) The discrepancy in the break flow rate

corresponds to a worst prediction of the primary pressure trend and of the primary total mass with

the consequent early prediction of the Last dryout occurrence. From a quantitative point of view, the

global accuracy is worse than in the reference case.

A fiirther decrease of the discharge coefficient (equal to 0.8) does not affect the transient up to

about 800 s; afterwards, the break flow rate calculation is slightly improved, but the apparent better

prediction of the ECCS flow rate (in terms of delivered mass) corresponds to a worst prediction of

the primary mass and of the dry out occurrence, that is anticipated. The results obtained with the

FFT application appear not consistent with the above analysis, but give an "objective"* evaluation to

the calculation performance.

The discharge coefficient equal to 0.75 gives the best results in the prediction of break flow rate,

intervention of ECCS and time of last dryout occurrence, as also testified by the accuracy evaluation

of these parameters. The obtained global accuracy is the best of all the performed calculations.

It can be noted that the importance of the discharge coefficients is confirmed, in addition, the

total accuracy shows a non monotone trend as a function of the break discharge coefficient.

c) Core level

Aimning at the improvement of the core level, the following analyses have been performed:

- reduction of the hydraulic diameter of the steam generators riser (run S302), so to improve the

prediction of the primary to secondary side heat exchange: small effects on the core level

prediction and on the dry out occurrence, slightly anticipated, with a small worsening of the

overall accuracy;

- reduction of the form loss coefficients (reverse) in the core by-pass (rnm S305): the core level is

underpredicted in the first part of transient and this causes a dry out occurrence, both at the

middle and high level of heater rods.

47
ED Calculation Variations from FFT application results Notes

reference case (AAtw / WF /AAp)

S301 CD Break set to 0.8 0.61 / 0.053 I 0.07 Improve primary side

pressure trend and

core rod superficial

temperature

S302 SG riser hydraulic 0.33 / 0.052 /0.066 Improve primary to

diameter reduced to secondary side

60% response

S303 CD Break set to 0.75 0.26 /0.051/ 0.069 Improve primary side

pressure trend and

core rod superficial

temperature

S304 CD Break set to 0.9 0.38 / 0.048 / 0.074 Improve primary side

pressure trend and

core rod superficial

temperature

S305 Kv reverse in vessel 0.35 / 0.049 / 0.076 Improve primary side

DC-UH by-pass as in pressure trend and

SBO4 calculation core rod superficial

temperature

Tab. 12: Sensitivity calculation matrix: varied input parameters and FFT results

48
Calculation ID T30A S301 S302 S303 S304 S305

1) Primary side pressure 0.065 0.070 0.066 0.069 0.074 0.076

2) Secondary side pressure 0.168 0.164 0.170 0.175 0.155 0.186

3) Accumulator 1 pressure 0.097 0.137 0.100 0.098 0.128 0.112

4) Accumulator 2 pressure 0.078 0.097 0.083 0.091 0.124 0.100

5) Fluid core inlet temperature 0.038 0.049 0.042 0.037 0.069 0.051

6) Fluid core outlet temperature 0.052 0.061 0.053 0.044 0.059 0.056

7) Upper plenum fluid temperature 0.709 0.774 0.737 0.751 0.765 0.745

8) Integral break mass flowrates 0.122 0.235 0.139 0.042 0.206 0.194

9) SGbottom downcomerfluid 0.157 0.177 0.161 0.110 0.195 0.055

temperature I

10) Break mass flowrate 0.826 1.031 0.842 0.671 0.945 0.906

11) ECCS integral mass flowrate 0.246 0.433 0.320 0.079 0.557 0.442

12) Rod clad temperature (bottom 0.057 0.068 0.057 0.051 0.071 0.062

level)

13) Rod clad temperature (middle level) 0.297 0.368 0.301 0.273 0.311 0.361

14) Rod clad temperature (high level) 0.530 0.599 0.549 0.437 0.573 0.625

15) Primary side mass inventory 0.134 0.225 0.132 0.078 0.183 0.180

16) Core level 0.964 1.087 0.910 0.790 1.100 0.959

17) SG downcomer level 0.192 0.196 0.195 0.181 0.206 0.174

18) Pressure drop SG inlet-outlet 1.489 1.499 1.938 1.619 1.268 1.275

19) Core power 0.187 0.260 0.165 0.154 0.185 0.251

20) Pressure drop loop seal (ascending 3.309 9.654 4.728 1.868 6.554 6.051

side)

21) Pressure drop loop seal (decending 0.414 0.557 0.440 0.570 0.560 0.334

side)

22) Pressurizer level 0.235 0.235 0.235 0.250 0.212 0.235

23) Pressure drop Sg inlet-Utubes top 0.432 0.433 0.486 0.459 0.454 0.414

Calculation result 0.290 0.610 0.330 0.260 0.380 0.350

Tab. 13: Summary of results obtained by application of FFT method to the selected

parameters for the sensitivity calculations (AA values)

49
Calculation ID T30A 5301 5302 5303 5304 S305

1) Primary side pressure 0.072 0.072 0.070 0.068 0.064 0.061

2) Secondary side pressure 0.042 0.042 0.042 0.042 0.041 0.042

3) Accumulator 1 pressure 0.060 0.054 0.058 0.059 0.046 0.052

4) Accumulator 2 pressure 0.073 0.060 0.069 0.063 0.047 0.058

5) Fluid core inlet temperature 0.050 0.050 0.048 0.055 0.044 0.043

6) Fluid core outlet temperature 0.034 0.041 0.031 0.035 0.300 0.025

7) Upper plenum fluid temperature 0.054 0.057 0.058 0.057 0.057 0.057

8) Integral break mass flowrates 0.053 0.054 0.055 0.011 0.052 0.053

9) SG bottom downcomer fluid 0.059 0.054 0.056 0.066 0.054 0.067

temperature

10) Break mass flowrate 0.097 0.093 0.103 0.094 0.099 0.096

11) ECCS integral mass flowrate 0.045 0.047 0.046 0.004 0.047 0.047

12) Rod clad temperature (bottom 0.036 0.035 0.034 0.036 0.029 0.030

level)

13) Rod clad temperature (middle level) 0.036 0.031 0.031 0.034 0.030 0.029

14) Rod clad temperature (high level) 0.031 0.028 0.027 0.020 0.025 0.025

15) Primary side mass inventory 0.042 0.027 0.026 0.074 0.012 0.020

16) Core level 0.083 0.074 0.079 0.064 0.075 0.074

17) SG downcomer level 0.063 0.060 0.061 0.073 0.060 0.059

18) Pressure drop SG inlet-outlet 0.083 0.083 0.084 0.110 0.068 0.065

19) Core power 0.107 0.111 0.108 0.084 0.114 0.117

20) Pressure drop loop seal (ascending 0.124 0.129 0.122 0.117 0.131 0.120

side)

21) Pressure drop loop seal (decending 0.089 0.104 0.090 0.036 0.081 0.084

side) 1

22) Pressurizer level 0.070 0.070 0.070 0.067 0.077 0.070

23) Pressure drop Sg inlet-Utubes top 0.069 0.069 0.076 0.071 0.062 0.068

Calculation result 0.054 0.053 0.052 0.051 0.048 0.049

Tab. 14: Summary of results obtained by application of FFT method to the selected

parameters for the sensitivity calculations (WF values)

50
I

20.A

17.5

15.0

12.5

IO.O

10.0

7.5

5.0

2.5

0.0 r

-2.5 0 -200 0 200 400 600 800 1000 1200 1400 1600 1800 2000 2200

rume (s)

Fig. 14: SPES post test SP-SB-03 (run S301) - PRZ pressure

:E

800-

700

600

500

400

3WO

20O

100

.100

-200

!

SPES

COLD LEG BREAK LOCA

RELAPSJMOO3.2.

MO T30ASRIONTFLCAN

YYY 9803BI1F

5301 =BRKINTFLOW

II

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

0 200 400 600 800 1000 1200 1400 1600 1800 2000 2200

rime (s)

Fig. 15: SPES post test SP-SB-03 (run S301) - break integral flow rate

51
S

a.

I

S

a.

20.0

18.0

16.0

14.0

12.0

10.0

8.0

8.0

4.0

2.0

a -

SPES

COLD LEG BREAK LOCA

RELAPSjM03.2

)=C T3A50150000

yyy SBO3P.027P

ZZZ S302P15010000

I

I

I

I

I

!

I

I

I

I

I

-200 0 200 400 800 800 1000 1200 1400 1600 1800 2000 2200

lime(s)

Fig. 16: SPES post test SP-S]-03 (run 5302) - PRZ pressure

g

P.

7M0.

700.

650.

65O.

600.

550.

500.

4M0

400.

-200

I SPES --- T30AH1TEMPOSO000IG

COLD LECI BREAK LOCA WVy T3OAHrIEUP90000I20

RELAPS/M003. mZ sso3rWoSP44

### SBO3TWO1SP9

IAAA S302HrEMP90W=

US S302HTTEMPg0000I

f . S S S S S I I S I

0 200 400 600 800 1000 1200 1400 1600 1800 2000 2200

Time (s)

Fig. 17 SPES post test SP-SB-03 (run 5302) - rods cladding temperature (high level)

52
20.0

, 18.0

16.0

14.0

I 4 I I I

SPES

COLD LEG BREAK LOCA

RELAPSMOD3,2

XT310APISOI 0000

YYY S=OP.027PO

I;

2

&

12.0 F

10.0

8.0

6.0

* I

2.0 * I

0.0'

-a0'0 0 200 400 600 800 1000 1200 1400 160 1800 2000 2200

rume (s)

Fig. 18: SPES post test SP-SB-03 (run S303) - PRZ pressure

E

600

500

400

200

200

100

0

-100 ' -

-200 0 200 400 600 80 1000 1200 1400 16W 1800 2000 2200

ime (s)

Fig. 19: SPES post test SP-SB-03 (run S303) - break integral flow rate

53
e

CL

20.0

18.0

16.0

14,0

12.0

10.0

8.0

6.0

4.O

2.0

0.0 '

-200 0 200 400 600 800 1000 1200 1400 1600 1900 200 2200

lMew (S)

Fig. 20: SPES post test SP-SB-03 (run S304) - PRZ pressure

j

800

700

6W0

500

40W

300

200

100

0

_1/1 It

T

SPES

COLD LEG BREAK LOCA

RELAPSjIM0032

I::T30ABPJGNFLOW

YYY SBO381F

ZZS30BRGNTFLW

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

-200 0 200 400 600 800 1000 1200 1400 1600 1800 2000 200

Tmm (S)

Fig. 21: SPES post test SP-SB-03 (run 5304) - break integral flow rate

54
20.0 a a a a a 9 5 a a

SPES xxx T"0AP100oooo

18.0 COLD LEG BREAK LOCA y• ssoP2

RELAPSIMOD3002 ZZZ 30PSlOO

16.0

14.0

~V120

10.0

6.0

4.0

2.0 I

0.01 ~ 2 - 0 200 ,D0 600 800 1000 1200 1400 1600 1800 2000 2200

Thme (s)

Fig. 22: SPES post test SP-SB-03 (run S305) - PRZ pressure

SPES XXXTOAMrEUPOSM060

7 COLD LEG BREAK LOCA YYY 130AHNrEMP900001206

mZ S803TWOIGP44 750. . /- ... Mz S8o3,WO1SP03

iAAA s8wFrTMP9wi•O 20•

700.~A SWHTEMP9OO00120

600.OHTEP000

650.

1600.

450.

400. " I I I I I I I I

-200 0 200 400 600 800 1000 1200 1400 1600 1800 2000 2200

Mime (s)

Fig. 23 SPES post test SP-SB-03 (run S305) - rods cladding temperature (high level)

55

5. CONCLUSIONS

The analyzed transient (SP-SB-03) is a small break LOCA experiment originated by a rupture in

the cold leg in one of the three loops of the SPES facility. No high injection system is provided

during the test; accumulators intervention prevents unacceptable core rod temperature excursion up

to about 1500 s; two dryout situations occur: the first one, at about 120 s into the transient, is

quenched by an intrinsic mechanism like loop seal clearing; the second one is quenched by the

intervention of the low pressure injection system.

A qualified RelapS/Mod3.2 nodalization has been used for the analysis. The comparison between

the code prediction and the experimental data leads to the conclusion that the code is able to predict

all the significant aspects of the transient.

Three main discrepancies have been identified, relating to the mass flow rate from the break, the

ECCS delivered mass and the core level. Several sensitivity calculations have been performed,

addressing these specific aspects.

The following considerations can be pointed out:

1) the variation of parameters considered in the sensitivity calculations, does not affect the

phenomena but only the sequence of events;

2) a tuning of the break flow rate is needed: the tuning of about 20 % during all the transient seems

to be adequate; this means changing in a reproducible (related to all other small break LOCA

analyzed) way the break discharge coefficients of the Relap5 input deck in the range 0.75 - 1.2

(obviously keeping each coefficient constant during the transient);

3) the importance of the discharge coefficients is confirmed; in addition, the total accuracy shows a

non monotone trend as a function of the break discharge coefficient;

4) the prediction of the first dry out situation is quite random and depends upon whose values is

out of control of the code user; any case, is confirmed that the relevance of this phenomenon

appears not very high in terms of reactor safety.

The reference calculation can be used for uncertainty evaluation, ref. [6], and specifically, for the

development of Code having the capability of Internal Assessment of Uncertainty (CIAU), ref. [21].

57

REFERENCES

[1] D'Auria F., Galassi G.M., "Code assessment methodology and results", IAEA Technical

Workshop/Committee on Computer Aided Safety Analyses, Moscow, May 14-17, 1990.

[2] D'Auria F., "Experimental facilities and system codes in Nuclear Reactor safety", Int. Seminar

State of the Art on Safety Analyses and licensing of Nuclear Power Plants, Varna (BG),

November 2-6, 1987.

[3] D'Auria F., Ferri R., Galassi G.M., Sugaroni F., "Evaluation of the data base from the small

break LOCA counterpart tests performed in LOBI, SPES, BETHSY and LSTF facilities",

University of Pisa Report, DCMN-NT 185 (91), Pisa, December 1991.

[4] D'Anria F., Galassi G.M., "Planning of SPES experiments SP-SB-03 counterpart to Lstf

Bethsy and Lobi/Mod2 experiments", University of Pisa Report, DCMN-NT 171 (91), Pisa,

May 1991.

[5] D'Auria F., Galassi G.3&, "Post test analysis performed by Relap5/Mod2 code of the SPES

small break LOCA test SP-SB-03 counterpart to LstW Bethsy and LobiMod2 experiments",

University of Pisa Report, DCMN-NT 195 (92), Pisa, July 1992.

[6] D'Auria F., Debrecin N., Galassi G.M.,"Outline of the Uncertainty Methodology based on

Accuracy Extrapolation (UMAE)", OECD-CSNI Special Workshop on Uncertainty Analysis

Methods, London (UK), March 1-3 1994, J.Nuclear Technology - Vol. 109, Nr 1 1995, pags

21-38

[7] Bovalini R., D'Auria F., Leonardi M., "Qualification of the Fast Fourier Transform based

methodology for the quantification of thermalhydraulic code accuracy", DCMN Report, NT

194 (92), Pisa July 1992.

[8] D'Auria F., Galassi G.M., Ingegneri M., "Evaluation of the data base from high power and and

low power small break LOCA counterpart tests performed in LOBI, SPES, BETHSY and

LSTF facilities", University of Pisa Report, DCMN-NT 237 (94), Pisa, Nvember 1994.

[9] Bolognini C., Gandolfi S., Medich C., Rigamonti M., Vescovi 0., Visconti G., Boiardi A.,

"Experimental data report - SPES test SP-SB-04", SIET, Sviluppo e Qualifica di Componenti

Termomeccanici, Piacenza (ITALY), March 1992.

[10] Ramson W.H. et al, "Relap5/Mod2 code manual: user guide and input requirements",

NUREG/CR-4312 EGG-2396, Idaho (USA). March 1997.

[11] The Relap5 Code Development Team, "Relap5/Mod3 code manual", NUREG/CR-5535-V4,

Idaho (USA), June 1995.

[12] Bajs T., Bonuccelli M., D'Auria F., Debrecin N., Galassi G.M., "On transient qualification of

Lobi/Mod2, Spes, LstW Bethsy and Krsko plant nodalizations for Relap5/Mod2 code",

University of Pisa Report, DCMN-NT 185 (91), Pisa, December 1991.

[13] Bonuccelli M., D'Auria F., Debrecin N., Galassi G.M., "A methodology for the qualification of

thermaihydraulic code nodalizations", Proc. of NURETH-6 Conference, Grenoble (F), October

5-8, 1993.

[14] Bonuccelli M., D'Auria F., Galassi G.M., Lombardi P., "Post test analysis of Spes test SP-FW02 (ISP 22) with Relap5/Mod2 code", University of Pisa Report, DCMN-NT 175 (91), Pisa,

July 1991.

[15] Ambrosini W., Breghi M.P., D'Auria F., "Evaluation of code accuracy in the prediction of

OECD/CSNI ISP 22", University of Pisa Report, DCMN-NT 176 (91), Pisa, July 1991.

[16] D'Auria F., Galassi G.M., Galetti R., Leonardi M., "Application of Fast Fourier Transform

method to evaluate the accuracy of SBLOCA data base", University of Pisa Report, DCMNNT 284 (96), Pisa, June 1996.

[17] Aksan N., D'Auria F., Glaeser H., Lillington J., Pochard R., Sjoberg A., "Evaluation of the

Separate Effects Tests (SET) Validation Matrix", OECD/CSNI Report OECD/GD (97) 9,

Paris (F), November 1996.

59
[18] Annunziato A., Glaeser H., Lllington L., Marsili P., Renault C., Sjoberg A., "CSNI Integral

Test Facility Validation Matrix for the Assessment of Thermalhydraulic Codes for LWR

LOCA and Transients", OECD Nuclear Energy Agency, NEA/CSNI/R (96) 17, July 1996.

[19] Ambrosini W., Bovalini R., D'Auria F., "Evaluation of accuracy of thermaihydraulic code

calculations", Energia Nucleare, vol. 7, pp. 5-16, 1990.

[20] D'Auria F., Frogheri M., Giannotti W., "Relap5/Mod3.2 post test analysis and accuracy

quantification of SPES test SP-SB-04", University of Pisa Report, DCMN-NT 319 (97) Rev.

2, April 1998.

[21] D'Auria F., Eramo A.., Giannotti W., "Advancements in planning an IAU code" 40 Regional

Meeting on Nuclear Energy in Central Europe, Bled (SLO), Sept. 7-10 1997.

60
LIST OF ABBREVIATIONS

AA Average Amplitude

ACC Accumulator

ATWS Anticipated Transient Without Scram

BL Broken Loop

CAMP Code Assessment and Maintenance Program

CCFL Counter Current Flow Limitation

CSNI Committee on the Safety of Nuclear Installations

DC Downcomer

DCMN Dipartimento Costruzioni Meccaniche e Nucleari

DP Differential Pressure

ECCS Emergency Core Cooling Systems

FFT Fast Fourier Transform

HPIS High Pressure Injection System

ICAP International Code Assessment and Application Program

IL Intact Loop

INEL Idaho National Engineering Laboratories

IPA Integral parameter

ISP International Standard Problem

ITF Integral Test Facility

KReverse form loss coefficient

LOCA Loss Of Coolant Accident

LPIS Low Pressure Injection System

MFWIV Main Feed Water Injection Valve

NA Not Available

NPP Nuclear Power Plant

NRC Nuclear Regulatory Commission

PORV Pressurizer Operated Relief Valve

PRZ Pressurizer

SG Steam Generator

SVP Single Valued Parameter

TSE Time Sequence of Events

UH Upper Head

WF Weighted Frequency

SUBSCRIPTS

AR break area

c core

ER break elevation with respect to fluid mass distribution in the primary side

Gc overall core inlet flow rate

RL recirculation loop

V fluid volume

W core power

WI total energy supplied by the heater rods

61

Appendix 1

Steady state calculation

63

e

0.

20.000 . SPES

STEAD•

19.000 REAU RELAR,

18.000

17.000

16.000

15.000

14.000

13.000

12.000

-0.0 -60.0 -70.0

Fig. 1- PRZ pressure

-60.0 -50.0 -40.0 -30.0 -20.0 -10.0

Time (s)

0 10.0

I

9.000

80A

8.000

7.500

7.000

6.500

6.000

5.500

S.0OW-9

SPES )O(S3RPA'00IOGO

STEADY STATE Y 3P80OO

RELAP5JMOD3.2 MSO-0

AAA SSO3P-204S

$4SBO3-3=4

- p

0.0 -80.0 -70.0 -60.0 -50.0 -40.0 -30.0 -20.0 -10.0

Time (s)

0 10.0

Fig. 2- SGs secondary side pressure

65
5.500 o o ..

SPES X S 83ROP284010O0

ZV S3OMP-110E--

RELAPSIMOO3.2 s03P.•3OE 6 

5.000 ,

4.750

3.750

3.500

3.=

3.000

-90.0 -80.0 -70.0 -60.0 -50.0 -40.0 -30.0 -20.0 -10.0 0 10.0

Time (s)

Fig. 3- Accumulator pressure

750.

SPES XXX S3ROTEMPFIIOOOOO

725. .STEADY STATE WV S3FW1TEMPG1)O1CI0

RELAPSIMOD32 SBOV-003P

700.

675.

650.

6e00.

575.

550.

525.

500.

-90.0 -80.0 -70.0 -60.0 -50.0 -40.0 -30.0 -20.0 -10.0 0 10.0

Time (s)

Fig. 4- Core Inlet fluid temperature

66
SPES ::. S3RDTEBPF 500I1OOG

725 STEADY STATE YYY $ O O1 0000

RE! ~pAO3.28BO3T-012P - FELAPS/MOM.2 Z803"2

700. -

675.

! 625. v

00

575.

550.

525.

-I

I

750.

725.

700.

675.

650.

a2s.

600.

575.

550.

525.

IMn

)0.0 -80.0 -70.0 4-0.0 -50.0 -40.0 40.0 -20.0 -10.0 0 . 1

Time (s)

Fig. 5- Core outlet fluid temperature

SPES XXX S3ROTEMPFI0O10000

STEADY STATE TTS 3TEMPl• ? OO1.00'-

RELAPSMOMD.2

. . I

I.

"-... 7'

A.0

-90.0 -80.0 -70.0 -60.0 -50.0 -40.0 40.0 -20.0 -10.0

lime (s)

Fig. 6- Upper Head coolant temperature

0 10.0

67
800.

SPES

STEADY STATE

750. RELAPS/MOD32

700.

5501

M TEMPF:7T010000

YYY TEUPF670IOýK*

TZ EPF7701O"o

## S03"-102s

AAA SO3T-103S

$n SBO-2025

000 SBO3T-203S

&&& SBo3T-302S

BBS SSO3T-3033

- *. * - - --

p p p ACA I

-90.0 -80.0 -70.0 -60.0 -50.0 -4.0 -3.0 -20.0

TmI (s)

-10.0 0 10.0

Fig. 7- SG bottom DC fluid temperature

I

S.

0

6

I750.

725.

700.

675.

650.

625.

80&.

575.

550.

525.

50.-

-90.0 -80.0 -70.0 -60.0 -50.0 -40.0 -30.0 -20.0 -10.0

Time (s)

Fig. 8- Heater rod temperature (bottom level)

0 10.0

68
750. 1 1

SPES XXX H~rFEuPS6OO9OGo

725. STEADY STATE 'TYY

RELAPS/MOD32 M So3TWO15P,4

700. AA SB03TWOIP%4

675.

S650.

575.

550.

525.

500. p

-00.0 -60.0 -70.0 -60.0 -50.0 -40.0 -30.0 -20.0 -10.0 0 10.0

rime (a)

Fig. G- Heater rod temperature (middle level)

750.. . . . . . .a 1

SPES Mx IrTTEUPO500C0 26

725. STEADY STATE YY WTEMPW*1•05

RELAP5/MO3.2 ZN SBUoTwM P3

700. I

675.

S650.

625.

550.

525. I

500. A

-90.0 -80.0 -70.0 -60.0 -50.0 -40.0 -30.0 -20.0 -10.0 0 10.0

Time (s)

Fig. 10- Heater rod temperature (high level)

69
,550. . .. ..

SPES xI SIM WRONTRLVAR0

525. STEADY STATE YYY S8o3PU

RELAP5/MM32

500.

475.

450.

425. ,

40O.

350.

325.

300. I p

-90.0 -80.0 -70.0 -0.0 -50.0 -40.0 -30.0 -20.0 -10.0 0 10.0

Time (a)

Fig. 11- Primary side total mass

5.000 , 1 , , a 

SPES x= SSROCNTRLVAR150

STEADY STATE YYy SB0ML-CL

RELAPS/M0032

&7500

3.250

34.000

3.750

-90.0 -80.0 -70.0 -80.0 -50.0 -40.0 .30.0 .20.0 -10.0 0 1

time (a)

0.0

Fig. 12- Core collapsed level

70
18.000

17.000

16.000

15.000

14.000

13.000

12.000

11.000

-90.

SPES x~oc SOCNTRI..AR2

STEADY STATE TYTymoTwR

AAA BB03L-210S

SS6803L.31OS'

1.0 -60.0 "70.0 -60.0 -W0 -4M0 -. 0

lime (S)

-20.0 -10.0 0 10.0

Fig. 13- SG DC level

E

30.0

25.0

20.0

15.0

10.0

5.0

0.0

-5.0

-10.0

-15.0

.•,l.1l

- -- - - - - - - - - - - - - - - - - - - -IU - ---- 4 --

imam

-40.0 -80.0 -70.0 -60.0 -50.0 -40.0 -0.0 -20.0 -10.0

lime (s)

Fig. 14- Pressure drop across Inlet-outlet SG

0 10.0

71
x 10 5

8.40

SPES

STEAE

820 RELAF

&00

7.80

7.60

7.40

7.20

7.00 --

-90.0 -0.0 -70.0

Fig. 15- Core power

~YSTATE

'5M03.2

0 0 a a i

M S3ROCNTRLVARS4

yvr S80300aw'

I.

-60.0 -50.0 -40.0 -30.0 -20.0 -10.0

Time (s)

0 10.0

e

I

70.0

60.0

50.0

40.0

30.0

20.0

10.0

"fi

SPES

STEADY STATE

RELAPSJMOO32

OCS3RODPLUSSIl

mZ S3RtO PLAS

M SBOD3 -llop

AAA S8O3DP-210P a

$$$ S003DP41OP

a 

2-

a -

I -

I -

I -

0 A #$ #q

-IW0.0 -80.0 -70.0 -60.0 -50.0 -400 -30.0

Tin, (s)

Fig. 16- Pressure drop across loop seal (asmcendig side)

-2"0 -10.0 0 10.0

72
-26.0 . ...

SPES x)0C S3RODPLSDSG1

STEADY STATE Y ZZZ33,0DPL.S9S3 S3,RODPL=02

REL.APSIMOM3.2 M SB03DP-109P, D# 

AA S803DP-2O9Pi $U803OP-M0P

40.0

a./ I

436.0

-38.0

-M0.0 j

-00.0 -80.0 -70.0 -60.0 -60.0 -40.0 -0.0 -20.0 -10.0 0 10.0

Time (s)

Fig. 17- Pressure drop saoss loop seal (descendig side)

4.200

SPES ::x S3ROCNTRLVARI

STEADY STATE YYY S803L-O0P

4.000 RELAPS/MOD3.2

3.800

3.600

- 3.400

3.200 Y

3.000

2.800

-90.0 -80.0 -70.0 -60.0 -50.0 -40.0 -30.0 -20.0 -10.0 0 10.0

Time (s)

Fig. 18- PRZ level

73
350.

300. &E"A5

AAA SBO3DPJ-.A32

$$$ SBO3OP-UU3

250.

e200

S 150. a.

100.

-90.0 -80.0 -70.0 -60.0 -50.0 -40.0 -30.0 -20.0 -10.0 0 10.0

lime (s)

Fig. 19- Pressure drop between SC Inlet plenum and Utubes top

60.0 1..

SPES 6 Oxxx S3ROOPOCkUHY

50.0 STEADY STATE YYY SS03DPCOUHýY

RELAP51MOD32

40A.

30.0

'? 20.0

10.0

-0.0 -

-20.0

-30.0 ,

-90.0 -8.0 -70.0 -60.0 -0.0 -40.0 -30.0 -20.0 -10.0 0 10.0

lime (s)

Fig. 20- Pressure drop across DC-UH bypass

74
200. a

180. 1-

SPES

STEADY STATE

RELAPSMOM2

X 8( 3RODPLHOSOI

YYY 93RODPLHDS*2

SZ 3ROIDPLHOS933

Ml 98O3DP-105PI

AAA S803DP-MOPi

US$ 9903DP-SOP'

160.

140.

S120.

100.

ae 80.

60.

40.

20.

I

.0 40.0 -70.0 -60.0 -50.0 -40.0 -30.0 -20.0 -10.0 0 1

ninm (s)

0. 1 -90 10.0

Fig. 21- UlquLd hold up In SG (primaryside)

9.000

8.000

7.000

6.000

6 5.000

4.000

3.000

2.000

1.000

0.000'

-90.0 40.0 -70.0 -60.0 -50.0 -40.0 -30.0 -20.0 -10.0

rime (s)

0 10.0

Fig. 22- Core inlet flow rate

75
I

.2

II.

10.000

9.000

6.000

7.000

5.000

4.o00

3.OOO

3.000

2.000

1.000

0.000-90.0

SPES

STEADYSI

RELAPSJM(

3OC 3ROMFLOWJS0000C

WE YYS3ROMFLOVIWruulOOCX

Mu MO S80SF-102S'

AMA SBO3F-202S 3

0$) S803F402

000 S803P-103S

MA SBO3P-203S

8B3 S803F-a=a

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

-80.0 -70.0 -60.0 -50.0 -40.0

Tnme (s)

-30.0 -20.0 -10.0 0 10.0

Fig. 23- SG DC flowrat

S

200

100

0

-100

-200

-3MO

-400

9 1 1 a a 4 9 -

SPE )= WRIPS IOUNI

-500 o I0.0 - -70.0 -60.0 -50.0 -40.0 -30.0 -2

Time (s)

Fig. 24- pressure drop across SO outlet and vessel nonle.

11.0 -10.0 0 10.0

76
7.000

6.000

5.000

4.000

3.000

2.000

a

S

I

0.000 L-

-90.0 -80.0 -70.0 -60.0 -50.0 -40.0 -30.0 -20.0 -10.0

Time (s)

0 10.0

Fig. 25- Hot leg mass Ilowrate

C.

22.0

20.0

18.0

16.0

14.0

12.0

10.0

8.0

6.0

SPES

STEADY STATE

RELAPS/M•03.2

XXX S3ROPI5010000

YYY S3RoP520010OW

"N S3ROP720010900

AAA S803P.027P

M 803P-1 04S

000 S803P.-04S

&&& $803P-304=

V •

K

1 -1,, . w

hnt,

-90.0 -M0.0 -70.0 -60.0 -50.0 -40.0 40.0

Time (s)

-20.0 -10.0 0 10.0

Fig. 26- Primary and secondary pressure

77

Appendix 2

Results of the reference calculation (run T03A)

79

e

3

2

e

a.

20.0

18.0

16.0

14.0

12.0

10.0

8.0

6.0

4.0

2.0

Dfi

I SPES

COLD LEG BREAK LOCA

RELAP5/MOD3.2

)OCTMOP5MO1OOO YYY SMOP-027P

I

I

I

I

I

I

I

I

!

-2?DO 0 200 400 600 80 1000 1200 1400 1600 180 2000

ThuP (p)

Fig. I- PRZ pressure

'-S

I

8.500-

7.500

7.O00

6.500

6.000

5.500

5.000

-200

:j

SPES OCTOP

COLD LEG BREAK LOCA fYiAIBO

RELAPS/MOD3.2 . s~ 1

AAA SB03P 44

AAA s8oWP 4

H•hflrl rV•lfl

3=0000

MMODW

-104S

-2M

-304S

0 200 400 600 800 1000 1200 1400 1600 1800 2000

Time (s)

2200

Fig. 2- SGs secondary side pressure

81
SPES )= T30AP284010000

5.00 , COLD LEG BREAK LOCA YYY T30AP4410000

RELAPSMOO3.2 Mz SBO410E

4.500

45000

3-500

:3.000

2.500

2.W00

1.0001

-200 0 200 400 600 800 1000 1200 1400 1600 1800 2000 2200

Time (s)

Fig. 3- Accumulator pressure

675. £ .. . . .. . .

I SPESxx T30ATEMPFIIO100100 YYY TOTMG10OO

650. COLD LEG BREAK LOCA mYY T30ATEMPGI10000O.

RELAPS/IM003.2

625.

600.

1850.

525.

I-I

500.

47 . II I | | | | | I 450.

425. a 1-- 2 * a a

-200 0 200 400 600 800 1000 1200 1400 1600 1800 2000 2200

Time (8)

Ftg. 4- Core Iniet fluid temperature

82
I SPES xo TI"OATF.UPFI 50010000 SPEY T30ATEMPG16500I00

650. COLD LEG BREAK LOCA YmY T'O3ATEUrMl00100

RELAPSPIMAO32

625.

600.

0-.

600.

475.

450.

425. . . l * I l P l ! " -.

-200 0 200 400 600 800 1000 1200 1400 1600 1800 2000 2200

limeo(s)

Fig. 5- Core outlet fluid temperature

'700. * * • * * * * * *

SPES xCo T3OATEMPF190010000

COLD LEG BREAK LOCA YYY __ 0ATEMPG1900000"

65o. RELAPSMOO3.2

600.

o50.

450.

400. ' I , .. . I l U' "

-200 0 200 400 600 800 1000 1200 1400 1600 1800 2000 2200

rime (a)

Fig. 6- Upper Head coolant temperature

83
a

1200

1000

800

600

400

200

0

-200

0 250 500 750 1000 1250 1500 175 2000 2250 2500 2750

limobs)

Fig. 7-. Integral break flowrat

e

I-I.

580.0

570.0

560.0

550.0

540.0

5.0

520.0

510.0

.. ,, r

!I

I

I

I

!

SPES OCTEIAPF5=00IO

COLD LEG BREAK LOCA YYY TEILPF6OMOOOOO

ZZTEMPFn=0I0000

AAA S503T-1 02

000 SSM3T203S

-2 w00 0 200 400 600 800 1000 1200 1400 1600 1800 2000

rime (s)

Fig.8- SG bottom DC futd tenmperature

2200

84
' PES xxOC T .oMFLowJ

COLD LEG BREAK LOCA YYY SMBF

.O RELAPSIM0032

1.0

OAMo -X ---------

W1.000 I 5 f "

-200 0 200 400 600 800 1000 1200 1400 1600 1800 2000 2200

lrm (a)

Fig. 9- Break lowrate

4M 6 a I a I I a a 9

I SPES X~CT30AE=CINTFLOWV

350. - COLD LEG BREAK LOCA YYY 88o3MEc

RELAPS/M03.2

300.

250.

200.

150.

100.

560. . --

-200 0 200 400 600 800 1000 1200 1400 1600 1800 2000 2200

rim (a)

Fig. 10- ECCS ktegral flowrate

85
g

I

I.

I.-

g

S

I

Ii

W&k

625.

600.

575.

550.

5M2&5

M I

as5.

450.

I.

YYY H1TEMP900000

AM SBO3TWO11P44

-45200 0 200 400 600 800 1000 1200 1400 1600 1800 2000 2200

Time (s)

Fig. 11- Heater rod temperstre (bottom level)

650.

625.

600.

575.

550.

525.

500.

47M.

450.

42&.

200 0 200 400 600 800 1000 1200 1400 1600 1800 2000. 2200

Time (a)

Fig. 12- Heater rod temperature (middle level)

86
E

A

801-

750.

700.

650.

600.

650.

500.

450.

AMn

I ~OOC ~flEMP9OSO0OM6 I WYY HTTEMP9000012OS

ZZ1 SBO83TWO18P93

I M

-22O 0 200 400 600 8O0 1000 1200 1400 1600 1800 2000 2200

Time (s)

Fig. 13- Heater rod temperature (high level)

I

1400

1200

1000

800

600

400

200

A

SPES

COLD LEG BREAK LOCA

RELAPSIMOD3.2

)=O T3OACNTRLVARt2O

WYY SMOPM

a a a a a 11 a a a a a

m B g m g II I E m E

a 200 400 600 800 1000 1200 1400 1600 1800 2000 2200 2400

Time (s)

Fig. 14- Primary side total mass

87
-I

5.000 f . . a 

SPES -- T3OACNTRLYARlS0

4.500 COLD LEG BREAK LOCA YYY SO0ML-CL

RELAPSMO03.2

4.000

3.5OO

3.000

2.5OO

2.000

1..500

1.000

0.500

-200 0 200 400 600 800 1000 1200 1400 1600 1800 2000 2200

Time (s)

Fig. 15- Care collapsed levd

13.500

13.000

12.500

12.000

'd 11.500

11.00

10.50

10.•

IO.OO0

9.500O

T

SPES

COLD LEG BREAK LOCA

RELAPSJMOO32

X~CT30ACNTRLVARt2

YYY T30ACNTRLVAR3

Z T30ACNTFILVAR14

M S803LPIIOS

AAA SDOML2103

$$$ SBO3L-310

0 200 400 SWS0 1000 1200 1400 1600 1800 2000

Time (S)

Fig. 16- SG OC level

88
100.

8

8.RELAPSJUQO3.2 I AM "' 'i •-• 8003DP-403P

AAA 8803OP-4•OP

60.

40.

-200 0 200 400 600 800 1000 1200 1400 1600 1800 2000 2200

Tim (s)

Fig. 17- Pressure drop across Inlet-outlet SG

Xl0 6

1.00 •

0.90

0.80

0.70CA

0.50

0.30

0.20

0.00L

-200 0 200 400 600 800 1000 1200 1400 1600 1800 2

Time (s)

Fig. 18- Core power

89
100. i i | 4 * 4 I

SPES X~X T30ADPLSASCI

80. COLD LEG BREAK LOCA YYY T3A SG

ZZZ T3OADPSAS03 ORELAPSMO3 2 AAA M S803P-110P SS03P-2 ý0P

60. $ SB-O3"P-3

0 4.-

.20.

-20.

40.

4U I ~ -200 0 200 400 600 800 1000 1200 1400 1600 1800 2000 2200

lime (s)

Fig. 19- Pressure drop across loop sea (ascendig side)

600 -i I I I I I I I

SPES xxx T30ADPLSDSOi

COLD LEG BREAK LOCA TI T30 302

Soo ZZZ T3UADPLSOSM3 0 RELAPSM0032 M1 SS3aOP-1 O

AM SB03DP-209P

$# SB03DP-309P

400

~300 S

100

-100 i I ! I I I ! ! " " ! ,

-290 0 200 400 600 800 1000 1200 1400 16WO 1800 2000 220

Time (S)

Fig. 20- Pressuw: drop across loop seal (descendig side)

90
-I

4J00

4.OO

3.000

2.500

2.000

1.00

0.5000

O.Soo

0.000 -

).500- -200

I

COLD LEG BREAK LOCA

RELAPSIMOD3.2

~OCT3oAcfM~LYAR1

YYY 9603L.01OP

II

....... A Lo

* S S S S * S * * S S

0 200 400 600 800 1000 1200 1400 100 1800 2000

limo (S)

227I

Fig. 21- PRZ level

e

U

150.

125.

100.

75.

50.

25.

0.

-25.

.50.

-75.

.100.

0 200 400 600 800 1000 1200 1400 1600 10O 2000 220o 2400

lime (S)

Fig. 22- Prussure drop between SG Inlet plenum and Utubes top

91
400 9 9 9 9 a a 5 a

SPES )=x T3OADPOCUHgY

COLD LEG BREAK LOCA YYY SB03DMCDUHBY

300 RELABJIMOD3.2

200

e

IL

0 -

-100

-200 0 200 400 600 800 1000 1200 1400 1600 1800 2000 200

Time (a)

Fig. 23- Pressure drop across DC-UH bypass

60.0 T ...

SPES xxx T3ADPLS1

50.0 COLD LEG BREAK LOCA ZYY T30ADPUIDSG"

00RELAPS/MOD3.2 M SB0,DP-105P

AAA SO-3D206P

40.0 $ S8o3oP-.305P

'? 30.0

20.0

0.0 -

-10.0

-20.0 r

-200 0 200 400 600 800 1000 1200 1400 1600 1800 2000 2200

lime (s)

Fig. 24- Liquid hold up In SG (primary side)

92
U

I

12.5

10.0

7.5

5.0

0.0 -

-2.5

-5.0

-7.6

-10.0

-12.5 L

-200 0 200 400 600 800 1000 1200 1400 1600 1800 2000

lrim (S)

Fig. 25- Core Inlet fow rate

200.

150.

100.

50.

0.

-50.

SPES

COLD LEG BREAK LOCA

RELAP5IMOM2

X)OC T30ADPSGIOUTVIN

YYY T30ADPSG2OUTrN

ZmZ T30ADPSG3OUWVIN

0" SB03DPSGIOUnIN

AAAM S DPSG2OUTVIN $$s S8O3DPS03OUTVIN

* I

* I

-j d. .A LJI ... ~m' .. i X.,V V " -1- UP A

-100.' ' .. .. -

-200 0 200 400 600 800 1000 1200 1400 1600 1800 2000 2200

Time (s)

Fig. 26- pressure drop across SG outlet and vessel nozzle.

93
3

.2

IL

5.000

4.000

3.000

2.000

1.000

4.000

-- I

-1.000 - i

-200 0

Fig. 27-

SPES

COLD LEG BREAK LOCA

RELAP5/MOM2

XuX T30AMFLDWJ= 1000

YYY T30AMFLOWJ67001000C

" SB03F-1025

AAA SB3F-202S

$$$ SS03F-302S

000 SB03F-103S

&M, SB03F-203S

888 SB03F-303S

IIitdIhIUiJE1~LaJjjthLh.La I .uiLiLAL, OfrL&LI&LA.jII .i gH

200 400

SG DC flowrat

600 800 1000 1200 1400 1600 1800 2000

Time (s)

2200

a

I

SPES XXK T30AMFLOWJ20000

COLD LEG BREAK LOCA YYY T30AMFLOWJ30•• 12.5 REASMD2Zzz T30AMFLOWJ400 000I

RELAPS/MOD3.2 # SB03MFHLIP

AAA SB03MFHL2P

10.0

7.5

2.5

2.5

-5.0 I S I ' ' " * " *

-200 0 200 400 600 800 1000 1200 1400 1600 1800 2000 22

l1mo (S)

Fig. 28- Hot leg nmss flowrat

94
3

20.0

18.0

16.0

14.0

12.0

10.0

8.0

6.0

4.0

2.0

fin n

COLD LEG BREAK LOCA

RELAPSJMOO32

cXX 130APIGMOWO

YYy T30PSMO

= TWOMODWo

ff T30AP72MOM100

AAA SBMPO3PM7

$$$ S503P4 048

Cm0 5903P4m

9" Su3P40Sm

I

-2200 0 200 400 600 800 1000 1200 1400 1600 1800 2000

Tim (s)

Fig. 29- Priary and secondary pressure

2200

95

Appendix 3

Results of the sensitivity analyses (runs S301, S302, S303, S304, S305)

97

I

"A

1&0

156

16.6

7S

5.6

an

I SPES MOM LEG BREAK LOCA

awl mcaoofton

M• emopgleflomo zzz otPMeiOMO

off 86t04ff O

000 89WS

S" 909kaPo4S

am

See

600 an

-q

I 400

I

200 208

100

v• a

m0 aS 466 S66 6a6 16 1 1406 I6e6 16o 2666

Time (a)

1-5. 1-3361 Cm- Pffny mid seoid-Vy pmefum

2200 10 6 200 466 666 6an 1666 12W 14w 1666 1666 2666 2206

Flu. 2- SMICMi- EOCS h•eg fhfownvt mad petmmy aeid told mms to0

g

75..

7m.

M5e.

55o.

M6.

660.

45

8PES

COLD LEG BREAK LOCA

8•01 Cawmido

M0 BMOHrTEMP99000OM

8ff 8013011P44

AA 890317 M1P23

I

XXXY 6"IHTI!Mt

6ico. COLDLOG BREAK LOCA YYY B=eomwosEi •zz 8808IWO6ItM

aw1 CdouuIs ### ROSTW01P44

666. MAAA 85O31TPl4

7M.

660.

66 6 " 400 6e am 16 1 146 6ow l 2 2206

TIM. (0)

F. 4- 931 Cmo FfidW ored %MpeoU M e*lev

. . . . . . . . . . .

Am2 6 200 400 660 ON 1666 1200 1466 16e6 1oe 26000 2260

Th-m()
I

-US * O • • t . I O! rTi f lal s

oft. €OD LEG BREAK UOCA yvY em~m ' 2mWOot zzz smasyve"F"

Moo.

6m0.

-20 a 0 40000 60w 1000 120 1400 10 16N000 2 2

Tmm ()

ftg. S016Cm. H- 1%dood . hpe auetu(h"g

g

I

I!

•A

o€COLD LEG BAK LOCA Vvy 6nu1mP610o0 s 8301 Cdolonlt z~z now'mep

S6OL

4m~

no a 26 406 66 n I00N 1200 1460 1600 160 2000 226

Tim(s)

Fig. &*8301 C"e - Com, Niot Mid tMp.frmnw

'0

lyn

OPUS

COL1D LEG BREAK LOCA

Mal1 Omcudallo

XXnMMOEMNMFDW

WyyZ 35F

j

0e00

g0o

600

200

0

-OM

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

I

C"LE BREAK LOCA W MM

M a Cak-hr"- =" - AS --

406

4M'

I' 14' I' .... " Mn

46 IM

PFg.e-8361 Cm, Prssrdv• mas. leaop seal (meeadig a~e)

•w

6 2w0 400 am6 goo 1o0 1200 46 160e0 Ism 2006 20

Th.m (s)

mvl. 7-831m .. !off~s bmfe"* al
22.5

10.6

17.5

XY

IN6

a

I

A.

I

pig. 1- 302 Cae- Pftuy ,d SCofdte ipV urs

O6 6 166 406 66 606 1666 1266 1466 166 16 266 26

Fig. 2- 5362 Coo.- ECOS ntgnd flow•n d Iftmuy sle toWd mos

0

0

I

ON.

ON6. -

650.

6".

7me.

sm6.

An0.

!

SPES

COLD LEG BREAK LOCA

S362 CmoIAItlofl

)00( 302HTTEMPO0

U"7 866651W0P11

0" SO61W01P44

AM $80T1IP'3

g

I

SPES XcX 830HTm"Em

IaO. COLD LEG BREAK LOCA YYY 6 5302 oO~ U 3!OSTW~toIS t

fff 9803W"0P44

606 AAM 69031W16P44

me7.

-166 6 166 466O 660 1o 110: 1466 1666 1666 2m, 22

TIm (*)

i. 4-5930 Cm.- M W rod tWmpwmuivmedd

N ......

40 206 0 m 406 6s6 m 06 16an l 166 1460 1666 1s0" 1666 116

Fg.3-SS Cm- HeAbed rod lemptm (baoom fe

06
S

I

a!

B PES

850 COW LEO WREAK LOCA __y 1M-2

7w

Ms.

-s a ms 400 usO use tOs me tue teaIs" tuetea

Tiwo(s)

11~ a-m5cue.. "sgew led te,,pum~hilgl""w"

I

C OLD LEO ORuM LOCA VY MOM" 1Cowo 7M SM C~udwdmn asw55W

7Mo a u S u sta uewsteteuea

mies

oft -s2c - . dtfui uie~r

Cl 0

I

t20e

lows

ms

ams

450

m5

a

455

MPES

COLD LEO BREAK LOCA

am02 Ccum"

XXK 83MORENOLOW*

Wvy W

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

I

COLD LEO BREA LOCA yyy 8300"S03w.o tSO. as:CdcII't'im on BBSOPt1os

SA 85055P410OP

4M.

-2= a gao moms MI ste I iSt45t I 11656 taos t

Tim(s)

fIg. 7T-602 Cm.- bnouIbredifleur rige-ismcm"- pod-~mrew loop mi (momesui ~" 
a XY

-w MOO

-g

SoLD MEO BREAK OCA 8oMP 1, no =p 8ao~oeooos

AAAI AM P:O•BR4

soO 89oka"~e

000 81IM

JIM BOW 3M4

17.5 F

BO

I

156.

Its

10.0

I 400

9w8

7.5 P

S.6 "

2M6 2w0

100

o., I. 0

l a 200 4M5 an No 1000 10 flAO 168 16 2660 2M0

T.na (*)

Fig. I- sM~ on" -l'AMy mwt 08O VImemre

TIMu (a)

0 2-Ig 9.3M Ca" - CS 100sltpf flowaoe~t gad r MeaW. taMm*

g

5oe.

m50.

Am.

150.

6O0.

460,

000.

C SPES *cOt,9 tEO DRE. LOCA

5303 Ces•a~

Wy 83OiWnMI V" ISsTOPI

0" 160S1W0P44

AM 893oOsiwMis

&

SIPES XXK 86O3HTWW6

85*, COLD LEG BREAK LOCA Wy 830.I

S303 ~~ ~ f soWolow4 903T~on/ 

860. a•8 e1

150.

100.

so

JIM

-08 8 200 400 Be BR 10o0 '120 1400 1M "lo 0 2000 92

Timel (0)

Fly. 4.8368 Cm.. IHaalirodtsmpaaluve (middle lowd)

I

I

I

I

-M 0 266 M loo 4oo R 100 1200o 1400 1000 1wo 2000 2M)

T.i,• (a)

Fig.$S.9M0Cmo- Minterooding hunp~ta (botteuu In

00
I-I

760.

um. 750.

7w.

M5.

M0.

on0.

on4.

- I

am'

COLD LEG BREAK LOCA

am saaeat

)OM 8304flmaop6oms"N

1WY ases0M06Uoe mZ 89SIAanwsu ow sm gOF

1~*Y

g

8OO

6OO.

oft.

H _ - . . . . m m

466 6 206 466 6w 1 16 1to" to0w 60 1m 2666 226

Pig6-SCm.. Hmd tempelur. (high~ h

Fig. 6- 8360CmO e Cean hilt flud lempereuve

WI

lowo

460

m

a

UP'S

COLD LEG BREAK LOCA

I36M CRebdo

XXX 8309FM0WTFLUOW

WYy inrMM

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

. . . . . . . . . .

5I

I

SPES MOX 83EW.ASGI

60.6 COLD LEO MM LOCA WY V8 L0EASMO

use Ccuilsiiom ZZZ m SSCLBBG 83030P-t t0P

Off0 6A 903D-OP•

AAA 850DP-210P

-10." I

40A6

460 26 466 666 me 1666 1268 146 1660 166 26 22

T.•me ()

Fig. 8-8363MS Oe Pofmeu drop was "m sod (soaemedi o"a

4M 6 260 466 60 m6 1me 1200 1460 t660 me6 266 2f6

Timo~)

PIg. 7-3303Cm..hilegiu bwae~ftow 1
29

I

a.

I

22.

2U0

17.5

1560

12J5

10.0

66

0.0

SPES

COLD LEO BREAK LOCA

I -

ZZE noo0 m B~66Umoo em. 85o4P?u•tao

MA SBR0I4P

AmA

onama s Lu04o

I

8•04 C~dmk WY am9"

100

.900 6O ~ ' 46 60 O66 6 16 1206 1406 166 ON0 206 226

Fig. 2-8304 C...-E BOOms lgon ffowiue and pdhsm Vwy told. 4.41

6O

me

300

O0

O6

t

I I I

0

£00 6 200 400 600 M66 1006 1206 1400 1600 1660 2066 2266

T1wie (in)

P9. 1- s364 C, . Ps~ay mid mchndnT pvm,

I

. SPES xxx 8304Hrt1Mpgo0

M0. COLD LEO BRREAK LOCA mY ms 900i0i W zzA I001W011PI2 fl•04~~ c8rMlo n 90StMP44

ism.

460. -

- 0 200 4W6 60 660 160N 1260 1400 1600 166 26 226

Thm (0)

Pig. 8- s04CM. - Hl ~ epmue(otmlv

I

I PSxxx 64604HTTr!MooP~

5•0. * COLD LEO BREAK LOCA yyY B2IHnTT s~oa c2uzion1S0O1WOIsPI I

0" 303IM•woP44

A0. AAA s9e00 0 Pt4

750.

7M.

Gm0.

go*. I w a-" a l -" me II Im

-06 0 206 46 606 666 1666 120 14001 1606ed 2660 22

Fig. 4.9s04 cm.- Hestr rod tmpeNtr (midl Ii)

00
I

A

I

,o. SPI . . .. . . . . gms

am COLD LEO BRMICLOCAW qo0 *~o i~OF" am 1w 

658. ION. -A-- --A-J

4 0 0-.

480 a 20 0 4 00 O 1006 12" 1400 1816 1600 2086 2,1

Ig., 3340Cm. Wa ddo h wrkm (hokda IQ

g

800. ! " xYY 8•o411•upttomomo

COWD LEG BREAK LOCA mE BMW-or

4001 I i i i

431L

48M0 200 486 600 6ON O 1060 1200 1400 180 10SM 28M

Fig. 6- 8304 On. - Cem luht Mold ft1e6..rtu

m

to

0p

I

I~) SPES x 6 XASG1

cOOW LEG WEAK LOCA ZZ800LA0

* 934 OeubeAMI 890300p.20p

mAmSiap4O

4K.40 0 6 402O0OIM0O 1406 168 1600 2000 220

FM. -8304 Cm*- Pressumdropeomsi. oopd (mmd ais)

0 200 406 6860 686 10t0o 120 148 1606 1t6 208 s0

FIg. 7.3384 Cue.. hndlor blnc•m nfdt
COL L••OREM. LOCA __Y 869.psWUW

- Cm iou~m asospy eoo

0MA 88UP.W0P

am 8903p-148

7.6

40. 6 2 AN we we l6w f6 140066 l66 1s" M 2

F~g. 1-6 sC.•- Pdwuvp uoi .,dupRMu(a)

700

am

4wO I

266

lee

4M a 206 466 666 806 166 1266 1466 1666 I6 26 2266

T.-u (o )

filg. 2-83050m. - ECCa iegri foreedpl~ ie111

m

lea

0

0

g

I

a SPES . . S. " P9 4M

o. coLD LEG BREK LOCA YWY M091r4EM

hfU SBO6NW~ItP44

8am. AA 8•603IP23

750.

70a.

usm.

4w6.

-"a6 2 466 sm6 lo6106 12'6 14,00 t66 1666 26D6 22M

FIV. 8--38M Case- 11masot rod tvmpet~lw (boll*m ikl)

S

* SPES mOc M"HT!P

COLD LEG BREAK LOCA yyy 83DSHIWWPI

0"U 8103TWO1SP44

666. I MA SUOSTWOISPI4

7m0.

eoft

An,.

4•M s8 2w6 46 m w 1m0 m 146 I1m6 10

mhm(s)

Fig.4-SM6Cm.- Hetebds mIvmpinwmRddia s"wd. m

N
g

M. COLD LEM BREAKLOCA f

liru,

IF

sm.

45 0 .-

400.1o . . ,.o ,. .o o . . o

206 400 0 ON 1000 120 1400 00 ION 2000

Tine (9)

Sg.S 3S o C n Dow fealrtd ts"m~m t~we (?oft Ii

g

I PtS xx SW!mmWiomoomU

/ COLD LEO iREAKLOCA ,WY6 l0069UP110t00000

.26 6 20 400 m 600 1000 120 1480 1600 11100 200 Ut

Thme(s)

iftg .25Cr. onhitfeltmeaer

NO S

I

'RUe 100

60

SPES

COLD LEG BREAK LOCA

6065 Ceh~c

uua0 S9A68PITFWM

YYY 3005SF

.... .. --- --.. ....

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

I

150. T " " ' " 1

S PtS NO( SSOSIWtIEO

MDOL LEG BREAK LOCA VYY 3MOMBASG2

A1A 8803OP-MOP

-105.

40 6 2 40 6ON 6 ION 1200 1406 IN0 10 2000 20

Tim(s)

Pfg. .816Cm- Fur.drep sewan lOp sad (smendig W"i

0 2W0 400 600 1000 1200 1400 1"00 109 2000 2

T.nI (9)

ng. 7-8906 Cae. Itdegmibrkflowrie
Appendix 3

Reference calculation input deck

109

100 new b'ui

•tiestlps AVn e

0000201 100...-7 0.5 07003 20 100 100

0000202 400.... 0.1 07003 20500 500

0000203 460. .5e-5 0.05 07003 40 1000 1000

0000204 1200. .5e-S 0.010700320040004000

0000205 2200. .5-5 0.05 07003 40 1000 1000

0000206 3200. .e-7 0.05 07003 401000 1000

0000207 1.c6 .So-7 0.1 07003 10040004000

nilnor odt

348 mlv

349 mflowj

350 mf-owj

351 mflowi

*352 rho

0353 zho

*354 tho

79100000

58000000

68000000

73000000

510000000

610000000

710000000

* pssures & varies

301 p 015010000 lx pre

302 p 520010000 8gl aaro.

303 p 620010000 *ag2 asp.

304 p 720010000 sg3OUpre.

305 voidg 570050000 • sgi sa do void

306 voidg 670050000 * sg2 as dcvoid

307 voidg 770050000 $ sg3 a dc void

3083 trivar 150 OcareM

309caUlvar 151 *rpv M

: ena•y balasw

310 caivar 064 Core power

311 caftvar 021 asgbhettransfer

312 clvar 022 g2heat ansfer

313 tlvar023 ag3 hea tamt

314 carivar 056 s hat h intesfr

315 cntdvar 060 pe •izt. heatas

316 clvar 061 *aorenanrod

317 ctzhivar 090 0 hes losses ps total

318 catrvar 091 heat ossesitoal

* iiquid levels & masses

319 ctrivarOOl * prz level

320 ctrlvar 002 asgl dc lv

321 cadvar 003 *s2 dc M

322 catrIvar 004 *so dc Iv1

323 catrilvar 020 * pstotal mass

324 catrlvar036 * sgl tlow mass

325 catrlva037 * 8&2 towalmass

326 atrvar 038 * g3 towl na.s

*327 catva r200 ps power knb.

* flaiea

323 tampg 120010000 am inlet

329 tcmpf 120010000 cor inlct

330 tcapf 140010000 core outlet

331 Stung 140010000 core outlet

332 tempg 015010000 p*zbaot

333 tempf 015010000 p'zbot

334 tempg 180010000 upper head

335 tanpf 180010000 upper head

336 tempf 010030000 surge line

$ mass flowurates

355 rnflow 105010000

356 wflowj 120010000

357 niflowi 113000000

358 .flovj 135010000

359 mflowj 160040000

360 inflw 010010000

361 mflowj 200010000

362 mflowj 300010000

363 wfiowi 400010000

* mass flowrates

364 milovd 59500000

365 mflowi 695000000

366 umlowi 795000000

367 milowi 045000000

368 nflawj 065000000

369 mflowj 530000000

370 mflowi 680000000

371 nfioowj 730000000

372 milowi 575000000

* mass fIowrsles

373 mfayow 231000000

374 mfIowj 481000000

375 mnflowj 383000000

376 mflowj 510020000

377 mflowj 610020000

373 mflowj 710020000

379 mflowj 597000000

390 mflowj 697000000

381 rfiowj 797000000

* rod s erf= teapetres

332 htUap 950001205

333 htbm 950001105

334 htkbrp 950001005

335 temap 900001205

386 ht=p 900001105

337 bnp 900000405

388 hncop 910000101

389 hfmfp 920000101

390 emp 020100102

• pressure diafatials

391 artriv 106

392 carvw 100

393 cativar 107

394 ctdvar 108

395 carlvar 109

396 catdvar 110

397 tivar 101

398 catrivar 102

399 aftvar 103

0 *eed watae3

0 ateamlinelI

0 steaml1= 2

*0 teamline 3

*rpvdc

• cotaiet

care id

*d ou by-asin

* dh bypass ou * surge line

*hll

•h12

*h13

*sg2IMcm-

• ag2 lvi conr.

* liz lvi ce.

*Sgl i cm *qgprzct . * ag1pr cotr.

* sgI do

" looPI aco * lop3 MCC

* break

"sgl aep liq

" g3.eq iq

*l p lvi cm+ * g2OvM m + * ag3 lvico+1

" but rod

" bat rod

" hot rod

0 average od

* average od

• average rod

average rod in ¥

Oaverage rod inup

*ptz ii heater

*l1hldp

* Sg ps

* il loop meal asc leg dp

*llpudp

0 lg3 dp

al1l tat 4p

*fludtempadxur

337 tanpf 290010000

333 tcmpf 390010000

339 tmpf 490010000

340 tenpf 570010000

341 t=pf 670010000

342 tempr 770010000

343 empg 520010000

344 tempg 620010000

345 tempg 720010000

11 itemp *12 d temp

*13 CI temp

• ugi dot

* mg2dot.

* sg3 dot.

Igl adt.

•g3 sdt.

*fed water

*feed water 2

S

S

• heat kases tepatare talke ir.

501taOrccnul0 0. 1

Pi F=M- Conssrecol

503timeOge mfl0 0. 1

504time Oge ul0 99. 1

602 503 zor 504 n

l

0Pump, trip

*

* doanre

• fluid flowrates 5-

346

347 rflowi

591000000

691000000

111
503te 0 ltni 0-1. 1

06tifme 0 jgsnl 0 106.

* pumpl deay *0 g3 fw dosum

562IpO30010000 knell 0 13.06e6 1 * tip for viv do

puinp2 tip

508tin 0 k tnfll 0-1. 1 pun2trip

509 pO30 0 1OOOO kmill 0 13.0c6 1 * pumzp2 decay (mqp.

506)

:pump3 tip

511timealt0 IlO. Ppunp3 * trip

512 p 03 0 010000kt 0ll0 13.0e6 1 punp3 decay (Ckn.

506)

0

0 3gi prsm cool

515imle0gonnllo. I*eg1

516 p 030010000 k null 0 13.0e6 10 trip for vlv sl Co

610 .515 mr 516 n opening

: s&2 pmssm conftol

517fm= 0 ge null 0-1. l*Pg2

518pO3OOlOOOO1knu10 13.0c6 l tripforviv aclo

611517 =r 512 n opening

• .g3 pess contr

519ifm 0 Sgen nl 0-1. SSg3

520p030010000 knul0 13.0c6 1* p for vlv a do

612 519 xx520 n opening

* lX level ceolr

522 fine 0 go mzl 0 0. 1 hi corol p=ez

523 timu 0 geo ullo 99.9 1 4 M coamwl t,

606522 :eo 523 Is M ced ral xz 0

0 i3. n lvc,, coatrol (deady state)

524 tneme 0 gonu 0. 1 aOgl

525fme 0 p,,mxU 0 90. 1 *sgl vlcoat stop

607 524 mr 525 n sgI licCotin.

• sg2 a levd conmbl (seady state)

526t -i 0 geoD 0 0. 1 sg2

527fme ge m ] 0 90. 1 *2M mcoat stop

608 526 xor 527 n sg2 lvl coat in.

* zS3 s level cntrol (steady state)

528 time 0 ge ll 0 0. i sg3

529 time 0 o null 0 90. 1 so3 l coat stop

609 523z•or529 n sg3 M cct im.

• end prosamm

540time0gonul0 2500. 1 aend

600 540 *ed pop=m

• gl safety valve

550 p 520010000 gomm0 7.20e6 n 0

551 p 520010000 pgnul1030.24c6 i 0

552 p 5200100001k mllO 7.00c n sglsa. clo

630 550xor551 a n sglsa.oP.

: sg2 safety valv

553 p 620010000l 1n1llO 7.20e• a 0

554 p 620010000ipnnll030.24e6 1

555 p 620010000 k dl 7.00e6 a *sg2sa. clo.

631 553x-r554 n sgoSa.oIL

• aS3 saf tyvalv

556 p 720010000gonnllO 7.20c6 n *

557 p 720010000 gnull030.246 1 4

552 p 720010000kinullO 7.006 n *sag3 s.€o.

632 556 xzr557 n • sg3 s. op.

563 time 0 me null 0 100. 1

0

Ssgl-Sg2 VvCosnniec optaing

56 ti=0BenullO 1.U6 1 sg14g2Ca0.op.

* sg141ec vv iCopeion

569•ine0 poull0 0.0 1 * 4g1.0• m .op.

* Piz intranueaten stop

570 cadrv00llt ml 0 1.11 a •iizhealshut-off 150

575 timne 0 genui 0 -L 10m

*si signal tr4p((iot utilzed

*576pO300lOOOOkfll O 11.70c6 1•sitp 0

* %&is acuadtim loop I & 3

580 p 03001000 le ull 0 2.50c6 l'*b

521 hap 95000120 5 gt nllO 700. lspis -582 bd ,9-50001103 St zu 0 700. 1046~ 583&&=Vp 950001005 gtMfllO 700. •¥pis

645 521 ar582 n*

646 645 or 593 n*

647 646andS580 a* op.

94 time• 0 go null 0 11P5L 1 tinhclu uace exp

* accvv, loop 1 achudim

535p2800100001 t mu0 4.22e6 I

56 wcvliq 294 tenno 00.001 1 lvivcl•.

648 586 or 594 1 *

650 59•zo5 643 n * vlv op.

acc; vv loop 3 acnaiaa & dosur

5C7p480OlOOOOtnullO 4.22.6 I*

88 acvliq 4S4 leInu 0 0.001 l* P v cdo.

649 588 or P54 is

651 587zor649 a * vlv op.

*5, cocupon•xts

* sMWfine

0100000 SLLM Pipe

01000016

0100101 4.64e-4 6

0100301 1.804 1

0100302 1.863 2

0100303 2.600 3

01003042.000 5

0100305 2.062 6

01004010. 6

010060190. 2

0100602 0. 3

0100603 90. 6

0100701 1.804 1

0100702 1.863 2

0100703 0. 3

0100704 2.000 5

0100705 2.062 6

0100201 4.--5 0.0243 6

0100901 1.e-6 1.e"6 1

01009020.5 0.5 2

01009030.5 0.5 3

0100904 1." 1."-5

01010010000000 6

01011010000000 5

* gi fw dlos=r

56OpO 3

001OOOOIt mull 0 13.06.6

* sg2 fw •losur

56lpC30010000 It,-nl 0 13.06e6 0

1 tip for lvdo

1 t*ip for vlv CIO

112
010120100O 15.420o06 1.05306 2.4549c60.0.1

0101202 000 15.4200.6 1.0534c6 2.4549.60.O.2

0101203 000 15.420Oc6 1.0534c6 2.4549.60.0.3

0101204 000 15.420O06 1.05346 2.4549.60.0.4

0101205 000 15.420oe6 1.05306 2.4549c60. 0. 5

0101206000 15.420oe6 1.0530.6 2.4549c60.0.6

0101300 1

01013010.0.0. 5

* p=czbotl

0150000 rc.bot. brmnch

0150001 21

01501010..679 0.008504 0.90.0.679 4.A.. 0.06970 0000000

0150200 000 15.13006 1.5910e6 2.4549.60.

0151101015010000 020000000 0. l.e4 1." 0000000

0152101010010000 01500000O 0.0.5 0.5 0000000

0151201 0. 0. 0.

0152201 0.0.0.

* p= boc2

0200000 plb.u branch

020000111

02001010.0.679 0.009532 0.90.0.679 4..-5 0. 0000000

0200200 000 15.13006 1.5910e6 2.4549.60.

0201101 020010000 025000000 .0. 0. 0000000

02012010.0.0.

* IpiZVmd~

0250000 premsf pip.

02500016

0250101 0.014208 6

02503010.679 6

02504010. 6

025060190. 6

0250701 0.679 6

0250901 4A.5 0.1345 6

0250901 1..6 1.6 5

025100100000006

02511010000000 5

0251201000 15.13006 1.59106 2.454060. 0.2

025120200 15.1300.6 1.5910.6 2.4540.60.34 0.3

0251203000 15.13o0e6 1.5910e6 2.4540.6 1. 0.6

0251300 1

0251301 0.0.0. 5

*prcztopl

0300000 pmtrop, 1r i

0300001 11

03001010.014208 0.6790. 0.90.0.679 4.- 0. 0000000

0300200 000 15.1300.6 159 10e6 2.45406 1.

0301101025010000 030000000 0. 1."- 1..-6 0000000

03012010.0.0.

*

* preztop2

0350000 prL.up brhnc

0350001 11

03501010.014208 0.679. 0. 90. 0.679 4.e.5 0. 0000000

035020 000 15.13006 1.5910c6 2.4540 1.

0351101030010000 0350000000 . L." 1&.6 0000000

03512010. 0. 0.

* P=e M Coatrol vol

0400000 pevo ondpvl

04001010. 10.10.0.90.10.4.0-5 0. 0000000

04002002

04002010. 150.e60.

: pnZ level coatrolj

0450000 prz.1c t2jm

0450101040000000 015010000 0.

0450200 1 606 aivar 001

0450201-1. 0. 0. 0.

0450202 1. 4.5 0. 0.

0450203 3.0 3.2 0. 0.

0450204 3.16 0.0 0. 0.

0450205 4.2 0. 0. 0.

0450206 5.2 -1. 0. 0.

0450207 10. -3. 0. 0.

0

* deady stale presoure c-atrol

0600000 pwftl tmndpivo

06001010.01212.0.0.0. 0.4.g-50.0000000

06002002

0600201 0.15.13c6 1.0

: tdp comn valv to pm:

0650000 pr.tv valve

0650101035010000 060000000 0.01 1.0-6 I...6 00O0000

0650201 10.0.0.

0650300 tpvlv

0650301 602

0

0 lowaeplnumu I

1000000 Io.pll hunc

100000111

1000101 0. 0.798 0.04734 0. 90. 0.798 4.e-5 0.013367

0000000

1000200 000 15.580c6 1.24206 2.4799c 0.

1001101 100010000 110000000.01127 0.5 035 0000000

10012010. 0. 0.

0

* lower downhoa.bbr.

1050000 ldc.bar 1ban

105000121

10501010.006656 0.344 0. 0. 0.0. 4.e-5 0.09206 0000000

1050200 000 15.5606 12420W6 2.47"6 0.

1051101 115010000 105000000 . 035 035 0000000

1052101 105010000 110000000.006656 1.5 1.5 00000

10512014.45 0.0.

1052201 4.45 0.0.

0

* Iowa plammm 2

1100000 imp12 hunch

110000121

1100101 0.01127 0.753 0. 0. 90. 0.753 4.-5 0.013367

0000O00

1100200 000 15560e 1.2420.6 2.4799e60.

1101101 110010000 120000000.009197 0.1 0.10000000

1102101 110010000 112000000.001441 26. 36. 0000000

1101201 4.2 0. 0.

11022010.25 0. 0.

1120000 co.bylo pýe

11200014

11201010.001441 4

1120301 1.015 2

1120302 1374 4

11204010. 4

11206010. 2

112060290. 4

11207010. 2

11207021.374 4

1120:01 4.e.5 0.0428 4

1120901 !.A.6 1.- 1

1120902035 0.5 2

1120903 I.e.6 1.A.63

11210010000000 4

11211010000000 3

1121201 000 15.4800.6 1.2420.6 2.4799c60.0.4

1121300 1

11213010.25 0.0.3

: core bypam coc jun (valve)

1130000 by.by.j ,ngljim

1130101 112010000 114000000 0. 1.".6 1..6 0000000

1130201 10.25 0. 0.

"Cam bypaw upper pat

1140000 ooby.up pipe

11400014

11401010.001441 4

113
1140301 1.081 2

1140302 1.015 4

11404010. 4

114060190. 2

11406020. 4

11407011.031 2

11407020. 4

1140801 4.A-5 0.0428 4

1140901 1.64 1. 1

11409020.5 0.5 2

1140903 1.o-6 1..6 3

11410010000000 4

1141101 0000000 3

11412010 15.4600c6 1.2420c6 2.4799e6 0.0.4

1141300 1

1141301 0.25 0. 0. 3

: downcone pip

1150000 downcx= pipe

115M001 7

11501010.006656 7

1150301M0.23 7

11504010. 7

1150601-90. 7

1150701 .0.23 7

1150801 4.-5 0.09206 7

1150901 1.0.4 ..6 6

1151001 0000000 7

11511010000000 6

1151201000 15.50006 1.2457e6 2.4799•6 0.0.7

11513001

11513014.45 0.0.6

•lowerplI 3

1200000 kpll branch

120000111

1200101 0.01127 0.486 0. 0. 90. 0.486 4.0-5 0.013367

0000000

1200200 000 154.M61.2420.6 2.47996 0.

1201101 120010000 130000000.009197 0.1 0.10000000

1201201 4.2 0. 0.

* upper downcomar - d cmm.6ztim

1250000 udc.d branch

1250001 5 1

12501010.0.49 0.0032614 0. -90. -0.49 4.A-5 0.125 0000000

1250200 000 15.40.86 1.2420o 2.47996 0.

1251101290010000 125000000.002734 0.5 0.50000000

1252101390010000 125000000.002734 0.5 0.5 0000000

1253101490010000 125000000.0027340.5 0.5 0000000

1254101 125010000 115000000.006656 0.1 0.1 0000000

1255101 125000000 1350000000. 0.1 0.10000000

1251201 1.49 0. 0.

1252201 1.49 0. 0.

12532011.49 0.0.

1254201 4.45 0. 0.

12552010.02 0.0.

: Coca active 1aig&

1300000 cm pipe

1300001 12

1300101.00964U 12

1300301.183 2

1300302.366 10

1300303.183 12

1300401 0. 12

130060190.12

1300801 1.270-7 0.011476 12

13009010.05 0.05 1

13009020.170.17 2

1300903 0.05 0.05 3

1300904 0.170.17 4

1300905 0.05 0.05 5

1300906 0.170.17 6

1300907 0.05 0.05 7

1300908 0.170.17 3

1300909 0.05 0.05 9

1300910 0.170.17 10

1300911 0.05 0.05 11

1301001 0000000 12

13011010000000 11

1301201000 15.5624o6

1301202 000 15.5255c6

1301203 000 15.5087.6

1301204 000 15.4919c6

1301205 000 15.4851e6

1301206 000 15.4882.6

1301207 000 15.4714.6

1301208 000 15.4705.6

1301209 000 15.4645c6

1301210 000 15.4445c6

1301211 000 15.4345c6

1301212 000 15.4245c6

1301300 1

13013014.2 0.0.11 0

1.2500.6 2.5164.6 0.0.

1.2677.6 2.51646" 0.0.

1.27996 2.5164. 0.0.

1.220.6 2.51646 0.0.

1.2942e6 2.51646 0. 0.

1.3163.6 2.5164c6 0. 0.

1.3235o6 2.5164C6 0.0.

1.3300.6 2.5164.6 0.0.

1.3526o6 2.5164.6 0.0.

13776o6 2.5164 60.0.

1.3826•6 2.5164c60.0.

1.3M00 2.5164o6 0. 0.

I

2

3

4

$

6

7

2

9

10

11

12

* dDnO top

135000 dc.topl Inc

1350001 11

13501010.0.3560.003261 0. 90.0.356 4.-. 0.114 0000000

1350200 000 15.430.6 1.3500c6 2.4799o6 0.

1351101 135010000 145000000.0002360 0.5 10.0 0000000

1351201 0.02 0.0.

0

occratop

1400000 cometop branch

140000121

1400101 0. 0.332 .00362 0. 90. .392 4..-5 0.011476

0000000

1400200 000 15.467766 1.400006 2.5164.60.

1401101 130010000 140000000 0.007571 0.3 0.5 0000000

1402101 140010000 150000000 0.007571 0.5 0.5 0000000

14012014.2 0.0.

14022014.2 0.0.

d.uhbypass

1450000 dc.uhby pipe

1450001 5

14501010.0004632 5

1450301 1.201 1

1450302 0.463 3

1450303 0.415 4

14503040.582 5

14504010. 5

145060190. 1

14506020. 3

145060390. 4

14506040. 5

1450701 1.201 1

14507020. 3

14507030.415 4

145=0740. 5

1450801 4.0-5 0.0243 5

145M01 0.5 10.0 1

1450902.02 10.0 2

1450903 0.5 10.0 4

14510010000000 5

1451101 0000000 4

1451201 000 15.4040.6 1.1900o6 2.4799o60. 0. 5

1451300 1

1451301 0.034 0.0.4 *

* cmn,-qpan cocncmeto

1500000 co.by.co 1 4

150000121

15001010.019607 0.382 0. 0. 90. .382 4.0-5 0.158 0000000

1500200000 15.4007.6 1.40006 2.5212e6 0.

1501101 150010000 160000000 0. 1.",6 1.0.6 0000000

1502101 114010000 1500100000.001441 50. 100. 0000000

15012014.45 0. 0.

15220l 0.25 0. 0. a

114
• do.uht. cbamjun (ulvc)

1550000 dcm.2j Wgujum

1550101 145010000 180000000 0. 1.0 10.0 0000000

1550201 10.02 0.0.

Supper pleam-hl doections

160000 up.hLoo fandch

1600001 41

16001010.019607 0.688 0. 0. 90. .698 4.0-5 0.15: 0000000

1600200 000 15.4007. 1.4000c6 2.5212 60.

1601101 160010000 200000000 0.003489 1. 1. 0000000

1602101 160010000 300000000 0.003489 1. 1. 0000000

1603101 160010000400000000 0.003489 1. 1. 0000000

1604101 170010000 160010000 0. 1." 1A* 0000000

1601201 1.49 0. 0.

1602201 1.49 0. 0.

1603201 1.49 0. 0.

1604201 0.02 0. 0.

: uppa-hbad 1

1700000 uI.1 brndl

1700001 1 1

17001010.0196070.936 0.0. -90. -.936 4.v.S 0.158 0000000

1700200000 1538976• 1.19006 2.5312c60.

1701101 180010000 170000000 0.1400c-4 0.1 10.0

0000000

17012010.034 0.0.

upper head 2

1800000 uh.2 branch

1300001 1 1

1300101 0. 0.936 0.022281 0..-90.-.936 4.o-5 0.158 0000000

1900200 000 153897c 1.1900v6 2.4799W 0.

130110L 190010000 100000000. 0.1 0.1 0000000

18012010. 0.0.

: upper head 3

1900000 uh i pe

19000012

19001010.027465 2

1900301 0.642 2

1900401 0. 2

1900601-90. 2

190070140.642 2

1900801 4.e-5 0.117 2

1900901 1."-6 Le-6 1

19010010000000 2

19011010000000 1

1901201 000 15.4000. 1.19006 2.4799. 0.0.2

1901300 1

19013010.0.0. 1

: oop lqpv4ko=

2000000 1.lpv bnmch

2000001 11

20001010.003489 0.782 0.0. 0. 0. 4.0- 0.0666 0000000

2000200 000 15.4597c6 1.400056 2.5212.60.

20011012000100002100000000. 1...6 1ý@6 0000000

2001201 1.49 0.0.

* loop 1 zpv..hl c

2100000 llfl•o branch

2100001 1 1

21001010.003489 0.791 0.0. 0. 0. 4.-S 0.0666 0000000

2100o00 000 15.459766 1.4000.6 2.52126 0.

21011012100100002200000000. 0.5 0.5 0000000

21012011.49 0.0.

* loop I hl-qg a=n. pipe

2200000 I.LM pipe

22000014

2200101 0.003489 3

22001020. 4

2200301 O.85 2

2200302 0.569 3

2200303 0.474 4

22004010. 3

2200402 0.00269 4

220060190. 4

2200701 0.r/S 2

2200702 0.417 3

2200703 0.474 4

2200801 4.0-5 0.066663

22008024.e-5 0.01542 4

2200901 1.e.6 1.c-6 2

22009020.1 0.1 3

2201001 000000 4

2201101 0000000 3

2201201 000 15.4540c6 1.4000O6 2.5212c60.0.4

2201300 1

2201301 1.49 0.0. 3

loop I bl-cam= j=L

2250000 11.hlut weitum

22501012200100002300000000. 0.20.2 0000000

2250201 1 .49 0.0.

Sloop I ps gu4ubcs

230000 ll.agut pipe

2300001 14

23001010.002427714

2300301 0.5000 2

2300302 1.0000 2

23003031.2780 10

23003042.0000 13

2300305 1.0000 14

23004010. 14

230060190. 9

2300602 -90. 14

2300701 0.5 2

2300702 1.0 8

2300703 1.278 9

2300704-1.278 10

2300705 -2.0 13

2300706-1.0 14

2300801 3.&-6 0.01542 14

23009010. 0. 3

23009020.01 0.01 9

23009030. 0. 13

23010010000000 14

23011010000000 13

2301201 000 15.4440c6 1.3950c6 2.52126 0. 0. 1

2301202 000 15.4440c6 1.38836 2.52126 0. 0. 2

2301203 000 15.4440. 1.373.6 2.5212c6 0.0.3

2301204 000 15.4440c6 13683.6 2.5212c 0.0.4

2301205 000 15.44406 13.533 2.52126 0. 0. 5

2301206 000 15.44406 13483M6 2.52126 0. 0. 6

2301207 000 15.4440.6 13383.6 2.5212c6 0.0.7

2301208 000 15.4440.6 13283.6 2.52126 0. 0. 0

2301209 000 15.44406 13183.6 2.52124. 0.0.9

2301210 000 15.44406 1.3083.6 2.5212.60. 0. 10

2301211 000 15.4440.6 1.29836 2.52126 0. 0. 11

2301212 000 15.4440. 1283. 2.5212M6 .O. 12

2301213 000 15.44406 1.270I36 2.5212.60.0.13

2301214 000 15.444O0 1.25004 2.5212 60.0. 14

2301300 1

2301301 10.490.0. 13

loop I €dut m. ja.

23S0000 l.cd.ut mejan

23501012300100002400000000. 0.010.2 0000000

2350201 1 1.49 0.0.

b loop I c14g com. pipe

2400000 l1..€g pip.

24000012

24001010. 1

24001020. 2

24003010.474 1

2400302 0.569 2

24004010.00269 1

2400402 0.00162 2

115
2400601-90. 2 2701107 0.6 1.03

2400701-0.474 1 2701108 0.7 1.07

2400702-0.417 2 2701109 0.8 1.06

2400801 4.o-S 0.01542 1 2701110 0.9 1.04

2400•2 4.5.. 0.04.9242 2701111 1.0 1.

2400901 0.1 0.1 1 *

24010010000000 2 2701200 12

2401101 0000000 1 2701201 0. -1.9

2401201 000 15.4000c6 1.2420c6 2.5212c6 0.0.2 2701202 0.2 -1.2

2401300 1 2701203 0.3 -.5

2401301 1.490.0. 1 2701204 0.4 -.2

* 2701205 0.6 .29

• loop I loop seal 1 3 2701206 0.7 .45

2500000 IlIr 1 h 2701207 0.3 .64

250000121 2701208 0.9 .8

2500101 0.001904 0.893 0. 0. -90. -0.898 4.o-5 0.04924 2701209 0.95 .9

0000000 2701210 1. 1.

2500200 000 15.4000c6 L2420e6 2.5212c60. 0

25011012400100002500000000. 1.o.6 1.o6 0000000 2701300 13

2502101 250010000 260000000 0. I.e-6 1..4 0000000 2701301 -1. 1.65

2501201 1.49 0.0. 2701302 ..9 1.53

2502=01 1.49 0.0. 2701303 -.8 1.4

* 2701304 -%7 1.32

looplloop ellpipe 2701305-.6 I1.2" 

2600000 li.b~pi pip 2701306 -.5 1.13

26000017 2701307 -.4 1.13

26001010.001904 7 2701303 -.3 1.12

26002010. 2 2701309 -.2 1.11

2600202 0.000929 3 2701310 -.1 1.11

26002030. 6 2701311 0. 1.1

26003010.359 1 0

2600302 1.021 4 2701400 14

2600303 0.727 5 2701401 -1. 1.65"

2600304 1.503 6 2701402 -.9 1.42

2600305 1.2 7 2701403 o.3 1.19

26004010. 7 2701404 -.7 1.03

2600601-90. 4 2701405 -.6 0.87

26006020. 5 2701406 -.5 0.74

260060390. 7 2701407 -.4 0.64

2600701 0.859 1 2701403 -.3 0.53

2600702-1.021 4 2701409 -.2 0.51

26007030. 5 2701410 -.1 0.45

26007041.503 6 2701411 0. 0.39

2600705 1.200 7 *

2600301 4.o-S 0.04924 7 2701500 15

2600901 .L" 1."4 2 2701501 0. .39

26009020.1 0.1 3 2701502 .1 .43

26009030.1 0.1 4 2701503 .2 .43

26009040.1 0.1 5 2701504 3 .52

2600905 1.04 1.04 6 2701505 .4 .56

26010010000000 7 2701506.5 .6

2601101 0000000 6 2701507.6 .64

2601201000 15.4000e6 1.2420e6 2.5212c60.0.7 2701503 .7 .68

26013001 2701509 .3 .71

2601301 1.490.0. 6 2701510 .9 .72

l 2701511 1. .73

* loop 1 jun• *

2700000 11U-mmp pump 2701600 16

27001010.0.26 4.340o-3 0.90. 0.26 0000000 2701601 0. .39

2700103260010000.0019 0.010.010000000 2701602 .1 .35

2700109275000000.0019 0.010.010000000 2701603 .2 .33

2700200 000 15.45006 1.24206 2.4749e6 0. 2701604.3 .34

2700201110.65 0.0. 2701605 .4 .36

2700202 110.65 0.0. 2701606.5 .39

270030100 0-10505 1 2701607.6 .42

2700302 335.0 0.12000 0.0106 77.0 59.7 3.5 2701603.7 .47

2700303 747.30.0. 0. 0. 0. 2701609.3 .53

• 2701610 .9 .63

b head cam *So 2701611 1. .73

270110011 *

2701101 0. 1.1 2701700 17

2701102 0.1 1.12 2701701 -1. -1.9

2701103 0.2 1.12 2701702 -.9 -12

2701104 0.3 1.11 2701703 -.3 -.3

2701105 0.4 1.1 2701704 -.7 -.5

2701106 0.5 1.09 2701705 -.6 -.25

116
2701706 -.5 0.

2701707 -A4 .1

2701702 -.3 .19

2701709 -.2 .27

2701710 -.1 .34

2701711 0. .39

2701200 1 ncm rilxctaf

2701201-1. -1.11

2701902 -.7 -1.4

2701203 -.5 -1.34

2701204 -.3 -1.17

2701905 -.1 -091

2701206 0. -0.72

2701900 2 

1

2701901 0. .75

2701902 .1 .79

2701903 .2 .78

2701904 3 .79

2701905 .4 .21

2701906 .5 .92

2701907.6 .25

2701908 .7 .36

2701909 .2 .22

2701910 .9 -91

2701911 1. 1.

270200022

2702001 0.

2702002 .1

2702003.3

2702004 .4

2702005 .6

2702006.2

2702007 .9

2702002 1.

2702100 2 

3

2702101 -1.

2702102 -.9

2702103 -.2

2702104 -.7

2702105 -.

5

2702106 -3

2702107 0.

2702200 24

2702201 -1.

2702202 -9

2702203 -.

2

2702204 -.7

2702205 -.

6

2702206 -.5

2702207 -.

4

2702208 -.3

2702209 -.2

2702210 -.

1

2702211 0.

2702300 2 5

2702301 0.

2702302.1

2702303 .2

2702304.3

2702305 

A

2702306 .5

2702307.6

2702308 .7

2702309 .2

2702310 -9

2702311 1.

2702400 26

2702401 0.

-.5

-.35

.2

.15

.4

.67

.84

1.

2702402.1 .95

2702403 .2 .91

2702404.3 .9

2702405 .4 .M7

2702406.5 .93

2702407.6 .2

2702408 .7 .75

2702409.2 .72

2702410.9 .68

2702411 1. .6

2702500 27

270251 -.6 -1.6

2702502 -.5 -1.4

2702503 -.45 -1.3

27025(4 -.38 -1.2

2702505 -.3 -1.

2702506 -.25 -.95

2702507 -.2 -.28

2702502 -.15 -.

2

2702509 

- -.7

2702510 -.05 -.64

2702511 0. -.

5

2702600 28 A ncmripoara

2702601 -1.-0.519

2702602 0. -0.512 S

S*t*oP cnmvs muhiplim 

*

27030000

27030010. 0.

2703002 .2 0.

2703003 .43 1.

2703004 .95 1.

2703005 1. 0. s

27031000

27031010.0.

2703102 1. 0.

***two-phaw c rvm &ffau=c 

*

270410011

2704101 0. .165

2704102 .05 .774

2704103 .1 .21

2704104 .3 .773

2704105 .5 .204

2704106 .7 .328

2704107 1. .216 0

2704200 12

27042010. .22

2704202.1 .2225

27041033 .248

2704204.5 .329

2704205.7 .477

27042061. .216 *

2704300 1 3

2704301 -1. -.92

2704302 -.2 -11.71

2704303 -.7 -1.6695

2704304 %.5 -1.72

2704305 -.3 -1.5

2704306 -.2 -1.137

2704307 -%1 -.5895

2704308 0. 0.165 S

2704400 14

2704401 -1. -.92

2704402 -.90 -.533

2704403 -.g -.33

2704404 -.6 -.092

2704405 -.4 -.045

2704406 -.2 -.039

2704407 0. -.039

1.2

1.

.9

.27

.83

.79

.75

1.2

1.12

1.1

1.1

1.2

1.3

1.3

1.25

1.2

1.

0.99

-.56

-.4

-.32

-.2

-.1

.069

.2

.2m

.4

.55

.63

.99

117
*

2704500 15

2704501 0. -.046

2704502 .2 -.366

2704503 .4 -.53

2704504 .6 -.6805

2704505.7 -.693

2704506 .8 -.676

2704507 1. -%482 *

2704600 16

2704601 0. -.039

2704602.2 -.066

2704603 3 -.095

2704604 .4 -%097

2704605 .6 -.173

2704606.2 -331

2704607 1. -%482

270470 17

2704701 -1. .89

2704702 -.7 .7

2704703 -.5 .653

2704704 -.3 366

2704705-.1t .1

2704706 0. -.046

2704801 -1. .89

2704802 -.7 37

270480 -.5 .03

2704804-3 .2

2704805 -.1 .22

2704806 0. .22 *

s*** tw*haw trque•ww diMumm Qo* 12-5)

27049002 1

27049010. 1.

27049021.1.

05000 2 2

27050010. 1.

27050 1. 1.

270510023

2705101 -L 1.9843

2705102 -80096 1.394

2705103 -.60638 1.0975

2705104 -.40686 0.82

2705105 -.19928 0.6648

2705106 0. 0.6032

2705200 2 4

2705201 -1.0000 1.9843

2705202 -.82234 1.8303

2705203 -.63371 1.6824

2705204 -.45853 1J.57

2705205 -.26702 1.436

2705206 -.17610 13179

2705207 -.0893 13481

2705203 0. 1.2336

2705300 2 5

2705301 0. -.45

2705302 .4 -.25

2705303 .5 0.

2705304 L .3569

2705400 26

27054010. 1.2336

2705402 .09 1.1965

2705403 .1885 1.1096

2705404.2734 1.0416

2705405 .4586 0.8953

2705406 .5744 .7807

2705407.7381 .6134

270540 .7635 .5849

2705409 .37 .4877

2705410 L .357 0

2705500 27

2705501 -1. -1.

2705502 -.3 -.9

2705503 -.1 -.5

2705504 0. -.45

2705600 22

2705601 -1. -1.

2705602 -.25 -.9

2705603 -.03 -.%

2705604 0. -.67

0

*** loop I pump demy velocity

2706100 506

2706101 0. 40.2

2706102 3. 0.0

2706103 l.e6 0.

0

*loop I coldlegpulpoutle pl

2750000 Il.cpl brUvmd

275000111

27501010.002734 0.706 0.0. 0. 0 4.-5 0.05900 0000000

2750200 000 15.5200c6 L2420o6 2.5212a6 0.

2751101275010000 280000000. 1.0-6 1."- 0000000

2751201 1.49 0.0. 0

* loopl Vu tnk

277000 ollp.ta tmdpvol

27701010.10. 10.0.0.0.4.0.5 0.0000000

277020000

27702010. 26.0065 2.291c5 2.582e6 0.

SP, lpbisj.

2780000 llJp4 t

2780101 277000000 280010000 0.

2780200 1 647

2780201 -L 0. 0. 0.

2780202 0. 0. 0. 0.

2780203 1. 0.130. 0.

2780204 l.e6 0.120. 0.

* loop I cold Leg pump oudet p2

2300000 II.cp2 Iunh

2300001 11

2800101 0.002734 0.706 0.0. 0. 0. 4.0-5 0.05900 0000000

2800200 000 15.520006 1242006 2.5212c6 0.

28011012800100002150000000. 1.e.6 1." 000000

2801201 1.49 0.0.

loop I acmviv

2810000 II.sgvp valva

2110101 282000000 280000000 0.08a.-3 300. 1.6 0000100 1.

1.

281020110.0.0.

2810300 znb viv

2210301650 648 1.5 0.

* loop I cc iec.on line

2820000 1 acci pip

2820001 16

2820101 0.45o-3 16

28203010.520 1

2820302 0.400 3

2820303 0.429 4

28203040.366 13

2820305 0.375 14

2820306 0.420 15

2820307 0.452 16

28204010. 16

2820601 45. 1

28206020. 3

28206030. 4

118
2820604-90. 13

2820605 -90. 14

28206060. 15

282060790. 16

2820201 4.-5 0.0 16

22210010000000 16

22211010000000 15

2221201000 4.19OO06 1.9960 2.4400 0. 0. 16

2821300 1

2821301 0. 0. 0. 15 0

0 loop 1 accumulator

2840000 II.a=c ac

2840101 0. 2.073 0.096 0. 90. 2.073

2240102 4.0v-5 0. 0011000

2240200 4.22e6 322.5 0.

2241101 222010000 0.24-3 10. 10.0000000

22422000.0610.06.290-3.3010.01250 0. 0.

loop I oold kg puznp•ouc p

3

2850000 11 dp3 I 1rcd

2250001 1 1

2250101 0.002734 0.706 0. 0. 0. 0. 4.e-S 0.05900 0000000

2850200 000 15.5200e6 1.2420e6 2.5212o6 0.

22511012250100002900000000. 1.e.6 .- 6 0000000

2251201 1.49 0.0.

Sloop 1 cold kg tpv com branc p4

2900000 ld.Ap 4 branch

29000010

29001010.002734 0.706 0.0. 0. 0. 4.A-5 0.05900 0000000

29002D0 000 01.50OOe 1.2420.6 2.52126 0.

* loop 2 rpv-hl moo

3000000 M2hlpv brach

3000001 11

30001010.0034890.722 0.0. 0. 0. 4.5- 0.0666 0000000

3000200 000 15.45076 1.4000v6 2.52126 0.

30011013000100003100000000. 1...6 1.".6 0OO0O00

30012011.49 0.0.

* loop 2 rpv.hI oam

3100000 t2 braonc

310000121

3100101 0.003489 0.721 0.0. 0. 0. 4..-S 0.0666 0000000

3100200 000 15.45976 1.40006 2.5212. 0.

3101101310010000 320000000 0. 0.5 0.5 0000000

3102101310010000 010000000 0. 1.0 1.0 0000000

31012011.49 0. 0.

31022010. 0.0.

*loop 21ý.g eo- pip.

3200000 1 ig pipe

32000014

3200101 0.003489 3

32001020. 4

3200301 0.2725 2

3200302 0.569 3

3200303 0.474 4

32004010. 3

3200402 0.00269 4

320060190. 4

3200701 0.2725 2

3200702 0.417 3

3200703 0.474 4

32008014.0-5 0.06666 3

3200802 4..-5 0.01542 4

3200901 1..46 U.6 2

32009020.1 0.1 3

32010010000000 4

32011010000000 3

3201201000 15.4540.6 1.4000.6 2.52126 0.0. 4

3201300 1

32013011.49 0.0. 3 l

* loop 2 b~l-.t cow. jun

3250000 M2.hLut mgljtn

32501013200100003300000000. 0.2 0.2 0000000

3250201 11.49 0. 0. 0

* loop 2pss gu4ubes

3300000 n.t•ut pipe

3300001 14

33001010.002427714

3300301 0.5000 2

3300302 1.0000 2

3300303 1.2720 10

33003042.0000 13

3300305 LO000 14

33004010. 14

330060190. 9

3300602 -90. 14

33007010.5 2

33007021.0 8

3300703 1.27L 9

3300704-1.272 10

330070 -2.0 13

3300706 -1.0 14

3300801 3.e"6 0.01542 14

33009010. 0. 2

3300902 0.01 0.01 9

33009030. 0. 13

33010010000000 14

3301101 0000000 13

3301201000 15.4440o6 139M06

3301202 000 15.4440v6 13&3W6

3301203 000 15.4440.6 13723e6

3301204 000 15.4440.6 13683e6

3301205 000 15.4440.6 13523.6

3301206 000 15.4440v6 13423.6

3301207 000 15.4440.6 1.33n346

330120 000 15.4440.6 1323.6

33012090 015.4440.6 131D.6

3301210 000 15.4440.6 1303.6

3301211000 15.4440.6 1.2983.6

3301212 000 15.444006 1.223.6

3301213 000 15.4440W6 1.2703.6

3301214 000 15.4440v6 1.250006

3301300 1

3301301 1.49 0.0. 13 0

2.3212c6 0. 0. 1

2.5212U60.0.2

2.52126 0.0.3

2.5212M60.0.4

2.5212M60. 0. 5

2.5212.60.0.6

2.5212.60.0.7

2.52126 0.0. 8

2.52126 0. 0. 9

2.21206.0O. 10

2.521260. 0. 11

2.5212c60.0. 12

2M212060.0.13

2.5212o6 0.'0. 14

* loop 2 d- ca= jun.

3350000 12.cLut snejum

3350101330010000 340000000 0. 0.01 0.2 0000000

335020111.49 0.0. 0

* loop 2 d-.g C= pipe

3400000 I2.cxg pipe

34000012

34001010. 1

34001020. 2

34003010.474 1

3400302 0.569 2

3400401 0.00269 1

3400402 0.00162 2

3400601 -90. 2

34007014).474 1

3400702 4.A17 2

3400801 4.o-S 0.01542 1

3400802 4.e-0 0.04924 2

34009010.1 0.1 1

34010010000000 2

3401101 OOOO0 1

3401201 000 15.4000.6 1.242006 2.5212.6 0.0. 2

3401300 1

34013011.49 0.0. 1 0

* loop 2 loop seal..bzih

3500000 12.br branch

350000121

3500101 0.001904 0.292 0. 0. -90. .298 4.e-5 0.04924

0000000

119
350020000015.4000.61.2420c6 2.5212e60.

3501101340010000 350000000 0. Ie.46 1.04 0000000

35021013500100003600000000. 1.o4 1.o6 0000000

3501201 1.49 0. 0.

3502201 1.49 0. 0.

loop 2 loop ad pipe

3600000 ELka.$ pipe

3600001 7

3600101 0.001904 7

3600201 0. 2

3600202 0.000929 3

36002030. 6

3600301 0.859 1

36003O2 1.021 4

3600303 0.727 5

36003041.503 6

36003051.2 7

3600401 0. 7

3600601-90. 4

36006020. 5

360060390. 7

3600701-0.259 1

3600702 -1.021 4

36007030. 5

3600704 1.503 6

3600705 1.200 7

3600801 4.4.5 0.04924 7

3600901 ..4 1.o6 2

36009020.1 0.1 3

36009030.1 0.1 4

36009040.1 0.1 5

3600905 1.U4 1." 6

36010010000000 7

3601101 0000000 6

3601201000 15.0000e6 1.2420e6 2.5212c6 0.0.7

36013001

36013011.49 0.0. 6

: loop 2 pimp

3700000 12-1pmp pump

37001010.0.26 4.3400.3 0.90.0.26 0000000

3700108 360010000.0019 0.010.010000000

3700109 375000000.0019 0.010.01 0000000

3700200 000 15.1500e6 1.242006 2.4749e6 0.

3700201 110.65 0.0.

3700202 110.65 0.0.

3700301270 270 270.-10 503 1

3700302 335.0 0.12000 0.0106 77.0 59.7 3.5

3700303 747.3 0.0. 0. 0.0.

0" loop 2 pump dc=yvlocity

3706100 506

3706101 0. 40.2

3706102 12. 0.

3706103 le6 0.

loop 2 coldleg pump outlet p1

3750000 ELcd.pl Iram

3750001 11

37501010.002734 0.706 0.0. 0. 0. 4.o-5 0.05900 0000000

3750200 000 15.5200c6 1.2420e6 2.52126 0.

3751101375010000 380000000 0. 1."6 14 0000000

37512011.49 0.0.

* loop 2 cold leg pu=p outt p2

38000 12.d.p2 Irac

3800001 1 1

3300101 0.002734 0.706 0.0. 0. 0. 4.,.5 0.05900 0000000

3800200 000 15.5200e6 1.2420e6 2.52126 0.

38011013800100003350000000. 1.06 1.4-6 0000000

3801201 1.49 0.0.

* loop2 brea= usim

3330000 12.break valve

3330101380010000 334000000 4.07150.4 L 1. 0000100 0.8

0.3 0.$ *aa 05 ndcsb04a2

3830201 10.0.0. aud 4.0715000o.S

3830300 tpvlv

3830301563

* loop2 re• volume

3840000 12.r.Ia txmd

38401010. 10.10.0.0.0.4.o-S 0.0000000

340200 00

32402010. 1.40d5 1.862e5 2.582e6 0.

*loop 2coldlcgpmpout p

3

335000 12.d.p3 3tk

3350001 11

38501010.0027340.706 0.0. 0. 0. 4.A-50.05900 0000000

3850200 000 15.5200.6 1.2420a6 2.5212e6 0.

38511013850100003900000000. l.6 1.4 0000000

3851201 1.49 0.0.

*loop 2 coldlegqmcu•o. bn p

4

3900000 12.dp4 fram

39000010

39001010.002734 0.706 0.0. 0. 0. 4.8-S 0.0590 0000000

3900200 000 15.5OOO6 1.2420c6 2.5212.6.

loop 3 rp•- eam

4000000 l3.l~pv Izu

400000111

4000101 0.003489 0.732 0.0. 0.0. 4.o-5 0.0666 0000000

4000200000 15.4597.6 1.4000e6 2.5212.60.

40011014000100004100000000. l.e 1.&4 0000000

40012011.490.0.

* loop 3 -d omm

4100000 13.6lho branch

4100001 11

41001010.00348 0.731 0.0. 0. 0. 4.A-5 0.06660000000

4100200 000 15.459766 1.4000c6 2.5212c60.

41011014100100004200000000. 0.5 0.5 0000000

41012011.49 0.0.

* loop 3 h"-a oo. pipe

4200000 .hSg pipe

4200001 4

4200101 0.003489 3

42001020. 4

4200301 0.3725 2

4200302 0.569 3

4200303 0.474 4

42004010. 3

4200402 0.00269 4

420060190. 4

4200701 0.3725 2

4200702 0.417 3

4200703 0.474 4

4200801 4.e-0 0.06666 3

4200802 4.*.5 0.01542 4

4200901 1.o.6 1."4 2

42009020.1 0.1 3

42010010000000 4

42011010000000 3

420120100015.4540e6 1.4000. 2.5212.60.0.4

42013001

42013011.490.0. 3

4

0 loop 3 hl-.t ca. .jiu .

4250000 D3.hlut mgtum

42501014200100004300000000. 0.20.2 0000000

42502011 1.49 0.0. s

* lbop 3 pas u.-4ubes

4300000 1Dgt pipe

430000114

43001010.0024277 14

43003010.5000 2

120
4300302 1.0000 X

4300303 1.27U0 10

4300304 2.0000 13

4300305 1.0000 14

43004010. 14

430060190. 9

4300602 -90. 14

43007010.5 2

4300702 1.0 3

4300703 1.278 9

4300704-1.272 10

4300705 -2.0 13

4300706-1.0 14

4300801 3."- 0.01542 14

43009010. 0. £

43009020.01 0.01 9

43009030. 0. 13

43010010000000 14

43011010000000 13

4301201 000 15.4440.6 1.3950.6

4301202000 15.4440c6 1.3893c6

4301203 000 15.4440e6 1.3783.6

4301204000 15.4440.6 1.363e6

4301205 000 15.4440W6 1.358336

4301206 000 1S.4440e6 1.3483I6

4301207000 15.4440c6 1.3383.6

4301208 000 15.4440e6 13283•6

4301209 000 15.4440M6 1.31836

4301210 000 15.4440c6 130•3C6

4301211 000 15.444006 1.292306

4301212 000 15.44006 1.2•3•6

4301213 000 15.4440.6 1.2703c6

4301214 000 15.44406 1.250006

43013001

4301301 1.49 0.0. 13 0

2.52126 0. 0. 1

2.52126 O.0.2

2.5212e6 0.0.3

2.5212e6 0.0.4

2.5212c6 0.0.5

2.5212c6 0.0.6

2.5212.6 0.0.7

2.5212.60. 0. 8

2.52126 0. 0. 9

2.5212c 0. 0. 10

2.5212c6 .0. 11

2..212•6 O.0. 12

2.5212e6 0.0.13

2.521260.0.14

* loop 3 dc.ut a jam

4350000 13.d.ut wgjim

4350101430010000 440000000 0. 0.01 0.2 0000000

4350201 11.49 0.0.

Sloop 3 1.ag -•o pipe

4400000 13.dg pipe

44000012

44001010. 1

44001020. 2

44003010.474 1

4400302 0.569 2

44004010.00269 1

4400402 0.00162 2

4400601-90. 2

4400701-0.474 1

4400702-0.417 2

4400801 4U-S 0.01542 1

4400802 4.@-5 0.04924 2

44009010.1 0.1 1

44010010000000 2

44011010000000 1

4401201000 15.4000e6 1.2420e6 2.5212e60.0.2

44013001

44013011.490.0. 1

0

* loop 3 loop eal klmi

4500000 Dstbr branch

450000121

4500101 0.001904 0.398 0. 0. -90. -0.98 4.A-5 0.04924

0000000

4500200 000 15.4000c6 1.2420e6 2.5212c6 0.

4501101440010000 450000000 0. 1..-6 1."-6 0000000

4502101450010000 460000000 0. 1."-6 1..-6 0000000

4501201 1.49 0.0.

4502201 1.49 0. 0.

4loop3loop w.pipe

460000013.7~pi pipc

46000017

4600101 0.001904 7

46002010. 2

4600202 0.000929 3

4600203 0. 6

4600301 0.859 1

46003021.021 4

4600303 0.727 5

4600304 1.503 6

4600305 1.2 7

46004010. 7

4600601-90. 4

46006020. 5

4600603 90. 7

4600701 -.059 1

4600702-1.021 4

46007030. 5

4600704 1.503 6

4600705 1.200 7

46008014.0-5 0.049247

4600901 1.6 U..-6 2

46009020.1 0.1 3

46009030.1 0.1 4

46009040.1 0.1 5

4600905 1.".6 1." 6

46010010000000 7

46011010000000 6

4601201000 15.4000.6 1.2420e6 2.5212.60.0.7

46013001

4601301 1.49 0.0. 6

* loop 3 pump

4700000o 1- pmp

47001010.0.264340..30.90.0.26 0000000

4700108 460010000.0019 0.010.01 0000000

4700109 475000000.0019 0.010.010000000

4700200 000 15.15006 1.2420c6 2.4749.60.

4700201 11.49 0.0.

470020211.49 0.0.

4700301270270270-10 5111

4700302 335.0 0.12000 0.0106 77.0 59.7 3.5

4700303 747.3 0. 0. 0. 0. 0.

' loop 3 pump dmcay velocity'.'

4706100 506

4706101 0. 40.2

4706102 15. 0.

4706103 1.96 0.

'loop 3 cold legpump cutlet pl

4750000 D

3 .cpl branch

47500011 1

47501010.002734 0.706 0.0. 0. 0. 4.-50.05900 0000000

4750200 000 15.5200.6 1.2420.6 2.52126 0.

4751101475010000 480000000 0. 1."-6 1."- 0000000

47512011.49 0.0.

*loop3 yh tk

47700• 3Jp..ta kndpv

47701010.10.10.0.0.0.4.o.5 0.0000000

477020000

47702010.26.00.5 2.2916.2.5826 0.

• loopl ipisj.

4780000 IlJpiU tnn

4780101477000000 480010000 0.

47802001 647

4780201 -1. 0. 0. 0.

4780202 0. 0. 0. 0.

4780203 1. 0.13 0. 0.

4780204 1.c6 0.13 0. 0.

'iloop3 cold leg pump cutle p2

4800000 13.Ap2 randi

480000111

48001010.002734 0.706 0.0. 0. 0. 4.a.5 0.0M00 0000000

4800200 000 15.5200.6 1.2420.6 2.5212.60.

121
4801101480010000 485000000 0. 1.o.6 1.-6 0000000

4801201 1.49 0.0. S

* loop 3 atmviv

4810000 I3gvp7 vaha

4810101 482000000 480000000 0.08o-3 300. 1.e6 0000100 1.

1.

4810201 10.0.0.

4810300 mdviv

48103016516491.5 0.

Sloop 3 aceinjeiohne

4820000 13.aoi pipe

4820001 16

4820101 0.45e-3 16

4820301 0.520 1

4820302 0.445 3

48203030.449 4

4820304 0.366 13

4820305 0.370 14

48203060.440 15

4820307 0.512 16

48204010. 16

482060145. 1

48206020. 3

48206030. 4

4820604-90. 13

4820605 -90. 14

48206060. 15

4920607 90. 16

4820801 4.*-5 0.0 16

4821001 0000000 16

48211010000000 15

4821201000 4.19000c6 .I960e5 2.4400c60.0.16

4821300 1

4821301.0. 0. 15

* loop 3 accumutlat

484000013.=o acc=

4840101 0. 2.073 0.096 0. 90. 2.073

4840102 4.0c-5 0. 0000000

4940200 4.22c6 322.7 0.

48411014820100000.240-3 10. 10.0000000

4842200 0.061 0.0 6.435 -3.296 0.0125 0 0. 0.

S

*loop 3 cold Iegpump oudl p

3

4850000 13.cLp3 hmrch

48500011 1

4850101 0.002734 0.706 0.0. 0. 0. 4.o-5 0.05900 0000000

4850200000 15.5200c6 1.2420.6 2.5212e6 0.

48511014850100004900000000. 1...6 1.,.6 0000000

48512011.49 0.0. C

: loop 3 cold lgrpv n.1x brai p4

4900000 13.D-p4 fumch

49000010

4900101 0.002734 0.706 0.0. 0. 0. 4.*-5 0.05900 0000000

4900200000 15.5000v6 1.2420.6 2.5212c6 0.

*

*loopl 3 riser

5000000 I1.gri pipe

5000001 12

5000101 0.01764 4 xz1.515

5000102 0.01164 9

50001030. 11

5000104 0.007028 12

50003010.5 2

50003021. 3

5000303 1.271 9

5000W304 1.1645 11

5000305 1.097 12

50004010. 9

5000402 0.022962 11

50004030. 12

500060190. 12

50007010.5 2

5000702 1.0 8

5000703 1.2M7 9

5000704 1.1645 11

5000705 1.097 12

5=00001 4.o-5.0111 9

5000802 4.0-5.0800 12

50009010.0010.0013

5000O02 0.01 0.01 11

5001001 0000000 12

5w001101 0000000 11

5001201000 6.91006 1

5001202 000 6.8750.6 1

5001203 000 6.8700.6 1

5001204000 6.17'006 1

5001205000 6.8700.6 1

5001206000 6.8700c6 1

5001207000 6.8600c6 1

5001203000 6.8600c6 1

5001209 000 6.8600c6 1

5001210 000 6.600c6 1

5001211 000 6.85006 1

5001212 000 6.8455.6 1

5001300 1

50013013.57 .0 0.3

5001302 3.55 .02 0.5

5001303 3.50 .07 0.7

5001304 3.473 0.097 0. 11

.24046 2.5924.6 .033 0. 1

.2449c6 2.58246 .061 0. 2

.2447. 2.58246 .111 0. 3

L.217.6 2.56.6 .161 0. 4

.2524 "2.254 24 0. 5

.2526e6 2.5825c6 .232 0. 6

.25246 2.5U2.•6 .235 0. 7

L.222.6 2.58206.230 0. 8

.25146 2.5826e6 .233 0. 9

.25186 2.-5826.233 0. 10

.2511c6 2.5829c6 .259 0. 11

.2550O6 2.58306.2890 . 12

O looptjgriscer ., 5050000 llsg.m branch

505000111

5050101.007083 1.000 0.0.90. 1.000 4..-5.011 0000000

5050200 000 6.840.6 1.2508.6 2.5820W6 0.29!

5051101 500010000 505000000 0. 1. 1. 0000000

5051201 3.473 0.0970.

0

"loop, s3gsqsqdrw

5100000 ll.sg& scp.f

510000131

5100101.0070580.9610.0.90.0.961 4.o.-5.010 0000000

5100200 000 6.40c6 1.5006 2.58206 0.8102

5101101 510010000 520000000 0.0.1 0.1 0000000 0.5

5102101 510000000 540010000 0. 1. 1. 0000000 0.15

5103101 5050100003510000000 0. 1& 1. 0000000

51012010. 0.097 0.

51022013.4730. 0.

51032013.473.097 0.

0

* loopi sg ss st.m dome

5200000 I~sgsad h=&

5200001 1 1

52001010. 1.3550.1370.90. 1.355 4Ue-50.0 000000

5200200 000 6.8406 1.250025 20.2582W0.99

5201101 520010000 5250000000.0 0.1 0.1 0000000

5201201 0.0.0970.

"sg ag &3 comion

5210OOO pr.m valn

5210101 520010000 720010000 0.01 1.o4 1.60000100 1 1.

521020110.0.0.

5210300 Upvtv

5210301 569 0

0 loopi sas gul

5250000 lIlig pipe

5250001 1

5250101 0.004260 1

5250301 &023 1

52504010. 1

52506010. 1

52507010. 1

5250801 4.e-5 0.07 1

122
52510010000000 1

5251201000 6.140e6 1.2500e6 2.5820e6 0.99 0. 1 *

l loop! sg s dc-ed mction oane

5300000 l1.dcd branch

530000121

5300101.01371 0-9610.0.90.0.961 4.A-5.051 0000000

5300200 000 6.840c6 1.2500.6 2.5820c6 1.000

5301101 530010000 520000000 0.0018 500. 500. 0000000

53021015400100005300000000. 1." 1...6 0000000

53012010.0.0.

5302201 0.0.0.

* loopi sig, dctop

5400000 ll.dc.to bru

540000111

5400101.013371 1.000 0.0.90. l000 4.o.5.051 0000000

5400200 000 6140e6 1.250006 2.582006 L

5401101560010000 540000000 0.0 1...6 1."-6 0000000

5401201 -3.473 00. C

* looplages dc Upper pmrt

5600000 11k..up branch

560000121

56001010.1.0420.0191430.90.1.042 4.e-5.051 0000000

5600200000 6.240e6 1.250e6 2.5820e6 0.1

5601101 560000000 570010000 0.0 1."-6 l.- 0000000

5602101560010000 565010000 0.0 0.5 0.5 0000000

5601201 3.57 0.0.

56022010.097 0.0. C

* oopl sg a fwl

5650000 11nign pipe

5650001 1

5650101 0.002268 1

5650301 5.145 1

56504010. 1

56506010. 1

56507010. 1

5650801 4.e.5 0.04 1

56510010000000 1

5651201000 65Oe6 653.c3 2.7000e60. 0. 1

*loopl ig sdc

5700000 II.mg.dc pipe

5700001 5

57001010. 1

5700102 0.0029 4

5700103 0. 5

57003012.1324 5

5700401 0.007412 1

57004020. 4

5700403 0.007412 5

570060190.5

57007012.1324 5

5700801 4.O-5 0.04 5

5700901 1." 1.-6 4

57010010000000 5

57011010000000 4

57012010006.340.6 1.2050e6 2.5820e6 0. 0.1

5701202000 6.8406 1.2050c6 2.5820e6 0. 0.5

5701300 1

5701301-3.570. 0.4

* loopl Igss &4iser comec4ijuncton

5750000 IlzAd mglj=

5750101570000000 00000000 . S. 8. 0000000

575020113.57 0. 0.

* loopl viv ca. to tlxdpol (p-coast.)

5800000 lligp vaiv

5800101 525010000 581000000 0.0040 Le.6 1."66 0000100 1.

1.

580020110.0.0970.

5800300 movlv

5800301610 516 1.5 1.

-loopi P-Ccst. OL.

5810000 llsgtv ttmolo

58101010. 10. 10. 0. 90. 10. 4.*-S 0. 0000000

581020000

58102010. 69.4e5 1.255c6 2.5820e6 1.

* loop Ig safety viv

5840000 lLssju valve

5840101 520010000 585000000 2.12376-5 1. 1. 0000100 1. 1.

* d-5.2 na

5840201 10.0.0.

5840300 ctrvtv

5840301 630 552 1.5 0.

loopl sg uytank

5850000 U.eatv tzvol

58501010. 10. 10.0. 90. 10.4.e-50. 0000000

5850200 20

5850201 0. 5.4e5 0.9999 C

:Jo• 1 sg fwtank

590m0 l1.iARi lmdpvol

5•900 0. 10. 10. .0.0. 4.e-S 0. 0000000

590020000

5900201 0. 80.40.5 637.6.3 2.7060.

* loo1P sgfw

5910000 l1-fwj tomdjm

5910101 590000000 565000000 0.

5910200 1 560

5910201 -1.0 0.0970. 0.

5910202 3.0 0.097 0. 0.

5910203 10. 0. 0. 0.

5910204 102. 0. 0. 0.

5910205 1.c6 0. 0. 0.

loopl sg Wl conmltank

5940000 ll.lv.cv tmdpol

5940101 0. 10. 10.0.0.0.4.-5 0. 0000000

594020000

59402010. 0.4065 1.25•0e6 2.70c6 0.

looplmg gM cotroljun.

5950000 lliv.q Umdpju

5950101 594000000 560010000 0.

5950200 1 607 atvar 002

5950201 -1.0 0. 0. 0.

5950202 1.0 6.0 0. 0.

5950203 U.6 5.5 0. 0.

5950204 12.0 4. 0. 0.

5950205 13.00 0. 0. 0.

5950206 15.00 0. 0. 0.

* loop Ig Mlv motrol tok

5960000 llJv.cl tdpvol

59601010. 10.10.0.0.0.4.e-S 0.0000000

596020000

59602010. 70.40d 1.067c6 2.70.60.

0

* loopl Kg M conro:ljuzL

5970000 llivJj UM=piz

5970101 560010000 596000000 0.

5970200 1 607 atir' 002

5970201 -1.0 0. 0. 0.

5970202 1.0 0. 0. 0.

5970203 11.30 0. 0. 0.

5970204 11.80 4. 0. 0.

5970205 16.00 6. 0. 0.

* loop2 ug as riser

6000000 12.sgii pipe

6000001 12

6000101 0.01764 4

6000102 0.01164 9

60001030. 11

123
6000104 0.007088 12

60003010.5 2

60003021. 3

6000303 1.273 9

6000304 1.1645 11

6000305 1.097 12

60004010. 9

6000402 0.022962 11

60004030. 12

6000601 90. 12

60007010.5 2

6000702 1.0 8

6000703 1.278 9

60007041.1645 11

6000705 1.097 12

6000801 4.o-5.0111 9

6000802 4.c-5 .0800 12

60009010.0010.001 a

6000902 0.01 0.01 11

6001001 0000000 12

60011010000000 11

6001201 000 6.8800c6

6001202 000 6.875046

6001203000 6.8700.6

6001204000 6.8700e6

6001205 000 6.3700e6

6001206 000 6.8700.6

6001207000 6.860006

6001208 000 6.860D06

6001209000 6.O6006

6001210 000 6.8600e6

6O01211 000 6.35006

6001212 000 6.455.e6

60013001

6001301 3.57 .0 0.3

6001302 3.55 0.020. 5

6001303 3.50 0.07 0.7

1.24046 2.5924e6.033 0. 1

1.2449o6 2.5824e6 .061 0. 2

1.2447e6 2.5824.6 .111 0. 3

1.2517c6 2.5826o6 .161 0. 4

1.2524a 2.5825.6.2040. 5

1.2526. 2..582.6 .232 0. 6

1.2524. 62.5825c6 .235 0. 7

1.2522.6 2.58206 .230 0. 3

1.2514.6 2.5826e6 .233 0. 9

1.2518.6 2.5829.6 .233 0. 10

1.25116 2.58296 .259 0. 11

1.250g6 2.5830e6.289 0. 12

625100100000001

6251201000 6.840c612500M 2.5820o6 0.99 0. 1

* oop2 35a &o-ad coano.6m zwoo

6300000 11..dd brawn

63000012 1

6300101.018371 0.961 0. 0. 90.0.961 4.o-5.051 OO0OO O

6300200O0 &840o6 M2 M 2.58206 1.000

6301101 6300100006200000000.0018 500. 500. 0000000

63021016400100006300000000. 1.4 1.o-6 0000000

63012010.0.0.

63022010.0.0.

loop2 xg n dc top

6400000 12.dA.to bra

640000111

6400101.018371 1.000 0.0.90.1.000 4.A-3 .051 0000000

6400200 000 6.940o 1.25OO6 2.5820c6 1.

6401101660010000 640000000 0.0 1.-6 LO4 0000000

6401201-3.473 0.0.

0

O loop2• gu do upptpaut

6600000 12.dc.up brmh

66000012 1

66001010.1.042 0.019143 0.90. 1.042 4.0-5 .051 0000000

6600200 000. 40e6 L067.6 2.5820.6 0.1

66011016600000006700100000.0 1.04 1.-4 0000000

66021016600100006650100000.0 0.5 0.5' 0000000

66012013.57 0.0.

6602201 0.097 0.0. s

0loop2g Safwd

6650o0 .sA pip

6650001 1

66501010.002268 1

66503015.145 1

66504010. 1

66506010. 1

66507010. 1

6650801 4.0-5 0.04 1

66510010000000 1

66512010006.350c6 653.e3 2.70O0c6 0. 0. 1

60013043.473 0.0970. 11

loop2 sgrisa ck

605000012 sg raecI

6050001 11

6050101.00708,1.0000.0.90. 1.000 4.o-5.011 000000

6050200 000 6.840.6 1.250.6 2.58206 0.295

60511016000100006050000000. 1. 1.OOOO0

60512013.473 0.0970.

*loop2 sg asu upar

6100000 12.Mmsesaxe

610000131

6100101.0070580.9610.0.90.0.961 4.o-5.010 0000000

61002000006.40.e61.25006 2.5820.60.8102

6101101 610010000 620000000 0. 0.1 0.10000000 0.5

6102101 610000000 640010000 0. 1. 1. 0000000 0.15

6103101 605010000 610000000 0. 18. 18. OOO0

61012010. 0.097 0.

6102201 3.473 0. 0.

61032013.473 0.097 0.

M goop2 a stem dam

620000012sgo i 1h

6200001 11

62001010. 1.355 0.137 0.90. 1.355 4.o.5 0.0 0000000

62002000006.840O61.2500O6 2.5820.60.99

6201101 6200100006250000000.0 0.1 0.1 0000000

6201201 0.0.097 0.

"loop2 s• a A

6250000 12.sgA pipe

6250001 1

62501010.004260 1

6250301 8.028 1

62504010. 1

62506010. 1

62507010. 1

6250801 4.A5 0.07 1

• loop2 sg i dc

6700000oo 2u• pip

6700001 5

6700101 0. 1

6700102 0.0029 4

67001030. 5

6700301 2.1324 5

6700401 0.007412 1

67004020. 4

6700403 0.007412 5

670060190.5

67007012.1324 5

6700801 4.e-5 0.04 5

6700901 1.". 1.-4 4

6701001 OO0000 5

6701101 OOOO00 4

6701201000 6.840.6 1.2

6701202 000 6.840o6 1.2

67013001

6701301-3.570.000 0.4

050. 2.58206 0. 0. 1

0506 2.5820.6 0. 0.5

* loop2 s a docim omctiajumtion

6750000 12.rLde mggiu

6750101 67000000 600000000 0. 8. 8. 0000000

675020113.570. 0.

0 oa vvcmto tmpvo(p-ccmt.)

6800000 12.sgvp valve

6800101625010000 6810000000.00400 1.-6 l.-6 0000100 1.

1.

6800201 10.0.097 0.

6800300 mtrvlv

6800301 611 5181.5 1.

124
* looV21-omt. voL

6810000 .zgtv tandpo1

68101010. 10. 10.0. 90. 10.4.g-50. 0000000

6810200 0-0

68102010. 69AC5 1.255c6 2.5220c6 L

* loop2 ag u•aftyvfv

6840000 12.sau av

6840101 620010000 685000000 2.1237e-5 1. L 0000100LI.

684201 10. 0. 0.

6840301 631 555 1.5 0.

I oop2 xg sfety taak

85000 t.tv pvol

68501010. 10.10.0. 90. 10. 4.e.5 0.000000

6850200 20

68502010. 5.4c5 0.9999 S

Sloop2xgfwtank

6900000 lWW. trmuxlpol

69001010. 10. 10.0.0.0.4.0-5 0.0000000

690020000

69002010. 80.4065 687.6e3 2.7.60. S

: loop2 sgfw

6910000 1.id fj im

6910101690000000 665000000 0.

69102001 561

6910201 -1.0 0.0970. 0.

6910202 8.0 0.097 0. 0.

6910203 10. 0. 0. 0.

6910204 102. 0. 0. 0.

6910205 l.6 0. 0. 0. 4

: loop2 ag lI conrol tank

6940000 12.t-cv tmndvol

69401010. 10. 10.0.0.0.4.c-5 0.0000000

6940200 0 0

69402010. M0.40e5 1250.0W3 2.70c6 0.

I oop2 sg Mv controljtm.

6950o00 12.v.4 tji

6950101694000000 660010000 0.

6950200 1 608 azflivrb-O3

6950201 -1.0 0. 0. 0.

6950202 1.0 6.0 0. 0.

6950203 U.6 5.5 0. 0.

6950204 11.00 4.00 0. 0.

6950205 11.30 0. 0. 0.

6950206 14.0 0. 0. 0. S

* oop2 xg Mv cotrol tank

6960000 W.v.. ftovo1

69601010. 10.10.0.0.0.4.0-5 0.0000000

6960200 00

69602010..405 1.0676 2.70c60.

* loop2 ag vi coar.jm

6970000 12"Jj tn~jM=

6970101 660010000 696000000 0.

6970200 1 603 Cmvrt0O03

6970201 -1.0 0. 0. 0.

6970202 1.0 0.0 0. 0.

6970203 11.30 0.0 0. 0.

6970204 11S0 4.00 0. 0.

6970205 16.00 6. 0. 0.

4 loop3 sg ss rbar

7000000 13.a pipe

7000001 12

7000101 0.01764 4

7000102 0.01164 9

70001030. 11

7000104 0.0070M 12

70003010.5 2

7000302 1. I

7000303 1.278 9

7000304 1.1645 11

7000305 1.097 12

7000401 0. 9

7000402 0.022962 11

70004030. 12

700060190. 12

70007010.5 2

7000702 1.0 3

7000703 1.278 9

70007041.1645 11

7000705 1.097 12

700001 4.o-5.0111 9

7000802 4.0-5.0800 12

70009010.0010.0013

70009020.01 0.01 11

70010010000000 12

70011010000000 11

7001201000 6.88006

7001202000 61750.6

7001203 000 63700v6

7001204000 63700.6

7001205000 6.2700c6

7001206000 6.8006

7001207000 61600.6

7001208000 6.600c6

7001209 000 6.86006

7001210 000 O0W6

7001211 000 6.8500c6

7001212000 6.3455c6

70013001

70013013.57 .0 0.3

70013023.55 0.020.5

7001303 3.50 0.070. 7

1.24046 2.5924.6.033 0.

12449c6 2.3524c6 .061 0.

1.244766 2.5824c .111 0.

1.2517.6 2.5826c6 .161 0.

1.25246 2.5825c6 .204 0.

1.526c 2.58256 .232 0.

1.2524c6 2-5825c6 .235 0.

1.25226 2.5820e6 .2300.

1.214e6 2.5266 .233 0.

1.21 2.5828.6.233 0.

1.5116 2.39 .259 0.

1.0M58 2.38306.289 0.

1

2

3

4

S

6

7

3

9

10

11

12

70013043.473 0.097 0. 11

: loop3 g ris• cidt

7050000 D3.•.r. bran&h

7050001 11

7050101.007088 1.000 0. 0. 90.1.000 4..-5.011 0000000

7050200 000 6.a406 1.25086 2.5820c 0.295

70511017000100007050000000. 1. 1.0000000

7051201 3.4730.0970.

0

0 1op0 g ispart7100000 13.sj sepux*

7100001 3 1

7100101.007088 0.9610.0.90.0.961 4.o-5 .010 0000000

71002000006.840.61.2500. 2.5220c•.0102

7101101710010000 720000000 0. 0.10.1 0000000 0.5

7102101710000000 740010000 0. 1. 1. 0000000 0.15

7103101 705010000 710000000 0. 18. 18. 0000000

71012010. 0.097 0.

71022013.473 0. 0.

71032013.473 0.097 0.

* loop3 sgunt~domcd

72000 13ug~sd himc

720000111

72001010. 1.355 0.137 0.90. 1.355 4.a-5 0.0 0000000

7200200 000 6.40•. 120OOc6 2.5820c6 0.99

72011017200100007250000000.0 0.1 0.1 0000000

72012010.0.097 0.

* loop3 sgnml

7250000•3D.va pie

72501 1

72501010.004260 1

7250301 8.028 1

72504010. 1

72506010. 1

72507010. 1

7250801 4.e-5 0.07 1

72510010000000 1

125
7251201 000 6.•046 1.2006 2.5820e6 0.99 0. 1

0

* loop3 sg = doad cmctionzon

7300000 D1.&Ad 1n1-

730000121

7300101.0183710.9610.0. 90.0.961 4.o-5.051 0000000

7300200 000 &.40c6 1.2500.6 2.5820e61.0000

7301101 730010000 720000000 0.0018 500. 500. 0000000

73021017400100007300000000. 1.-4 I.e. 0000000

73012010.0.0.

73022010.0.0.

'loop3 sag dctop

7400000 D.da.to banmch

7400001 11

7400101.018371 1.000 0.0.90. 1.00 4.U5.051 0000000

7400200 000 6.840c6 1.2500W 2.5820c6 1.

7401101 760010000 740000000 0.0 1."-5 1."- 0000000

7401201-3.473 0.0.

* loop3 a do uppaput

7600000 .dc.up bmanc

7600001 21

76001010. 1.0420.0191430.90. 1.042 4.e.5.051 0000000

76002000006.240o61.067e6 2.5820c6 0.1

760110176000000770010000 0.0 1.-6 1.40000000

7602101760100007650100000.0 0.5 0.5 0000000

7601201 3.57 0.0.

7602201 0.097 0.0. s

* loop3 sga fMl

7650000 13.sgit pip.

7650001 1

7650101 0.002268 1

7650301 5.145 1

76504010. 1

76506010. 1

76507010. 1

7650801 4.*.5 0.04 1

76510010000000 1

7651201000 6.200c6 653.c3 2.7000.6 0. 0. 1

• 1oop3 agu do

7700000 flqgdo Vpip

7700001 5

77001010. 1

7700102 0.0029 4

7700103 0. 5

7700301 2.1324 5

77004010.007412 1

77004020. 4

77004030007412 5

7700601 90.5

77007012.1324 5

7700801 4.o.5 0.04 5

770901 1.4 1.&6 4

77010010000000 5

7701101 0000000 4

7701201 000 6.540c6 1.20506 2.5820.6 0. 0. 1

7701202 000 6.40c6 1.20506 2.5•20c6 0. 0.5

77013001

7701301-3.570. 0.4

* oop3 sa g do-r•a coonedimjundion

7750000 D3.udo sigejun

7750101770000000700000000 . L. 2. 0000000

7750201 13.57 0. 0.

loop3 vlvaom to UmVM (p-col)at

7200000 D.sgyp valv

7800101 725010000 721000000 0.00400 1..4 1.". 0000100

1.1.

7200201 10.0.097 0.

7800300 ntrvlv

7800301 612 520 1.5 1. *

* j,,p 3 VoL

7210000 Disp tm4pv

72101010.10.10.0. 90. 10. 4.e.S 0. 0000000

7810200 0 0

78102010. 69.4.5 1.55 2.58206 1.

* lop3 2a9 ftyviv

724000 Diisju valve

7240101 720010000 785000000 2.1237.-5 1. 1. 0000100 1. 1.

7840201 10.0.0. '7240300 m•vl

740301 632 558 1.5 0.

* loop3 igsanfdytank

7250000 Ds..v toiivd

78501010. 10. 10.0. 90. 10.4.*-5 0. 0000000

725020020

72502010. 5.4.5 0.M9

0

* loop3 sg fwtank

790•000 fw.U dpvol

79001010.10. 10.0.0.0.4..-5 0. 0000000

790020000

79002010. 80.40d5 664.33 2.766 0.

0

* loop3 sgfw

7910000l3Iw taidpjtm

7910101790000000 765000000 0.

7910200 1 562

7910201 -1.0 0.0970. 0.

7910202 2.0 0.097 0. 0.

7910203 10. 0.0 0. 0.

7910204 102. 0.0 0. 0.

7910205 1.e6 0.0 0. 0.

0

* loop3 sg v control tank

7940000 Jwvcv ttndývl

79401010. 10. 10.0.0.0.4.-5 0. 0000000

794020000

79402010. 80.4065 1067.63 2.70C6 0.

0

* loo3 s1 MvlColjum

7950000 131v.q tmodpium

7950101794000000 760010000 0.

7950200 1 609 ctdvar 004

7950201 -1.0 0. 0. 0.

7950202 1.0 6.0 0. 0.

7950203 3L6 5.5 0. 0.

7950204 11.00 4.00 0. 0.

7950205 11.30 0. 0. 0.

7950206 14.0 0. 0. 0.

* loop3 sg Mv control t•k

7960000 131v.cl tmdpvol

79601010. 10. 10.0.0. 0. 4.e-5 0. 0000000

796020000

79602010.70.40@5 1.067c6 2.70e6 0. *

loop3 29 Mi Coutol m

7970000l3I1V4 toidpjta

7970101760010000 796000000 0.

79702001 609 cativu 004

770201 -1.0 0. 0. 0.

7970202 1.0 0.0 0. 0.

7970203 11.30 0.0 0. 0.

7970204 11.30 4.00 0. 0.

7970205 16.00 6.00 0. 0.

& upe line wall.

1010100065 210.01215

126
10101100 01

10101101 40.0167

10101201 1 4

101013010.4

101014000

10101401 567.5

10101501 0100100000 1 1 1.304 1

10101502 010020000 0 1 11.863 2

10101503 010030000 0 1 12.600 3

10101504 010040000 0 1 12.000 4

10101505 010050000 0 1 12.000 5

10101506 010060000 0 11 2.W02 6

10101601-999 03101 1 1.304 1

10101602 -M 0310111. 3 2

10101603-999 03101112.6003

10101604-999 0310112.0004

10101605-M9 0310112.0005

10101606-999 0 3101110626

1010170100.0.0.6

101013010. 10. 10. 0. 0. 0. 0. 1.6

: PrZ vesel walls

1015100010 5 2 1 0.06725

1015110001

1015110140.0005

101512011 4

101513010.4

101514000

10151401 567.5

10151501015010000 0 1 1 0.679 1

10151502020010000 0 1 10.6792

10151503 025010000 10000 1 10.679 3

10151504030010000 0 110.6799

10151505 035010000 0 1 1 0.679 10

10151601000000000 0 0 1 0.679 10

1015170100.0.0.10

101518010. 10. 10. 0. 0. 0. 0. 1. 10

*piz bottom end

1015200015 110.

101521000 1

10152101 4 0.150

10152201 1 4

10152301 0.4

101524000

10152401 560.5

10152501015010000 0 11 0.0142 1

10152601000000000 0 0 10.0142 1

10152701 00.0.0.1

101528010. 10. 10.0.0.0.0. 1. 1 a

Slxzop od wall

1015300015 110.

1015310001

1015310140.120

10153201 1 4

101533010.4

101534000

10153401 560.5

10153501035010000 0 110.0142 1

1015361000000000 0 0 10.0142 1

1015370100.0.0. 1

101533010. 10.10.0.0.0.0. 1. 1

paiz kezmlheateii

10201000 2 10 2 1 0.0

10201100 0 1

10201101 3 0.0040

10201102 1 0.0050

10201103 1 0.0070

10201104 1 0.0086

10201105 1 0.0100

10201106 2 0.0110

10201201 3 3

10201202 2 4

10201203 5 5

10201204 5 6

10201205 2 7

10201206 2 9

10201301 0.043

10201302 0.0 6

10201303 0.967

10201304 0.0 9

10201401 561.0 10

10201501 000000000 0 0 1 2.37 1

10201502 000000000 0 0 1 0.303 2

10201601 015010000 0 1 1 2.37 1

10201602 020010000 0 1 1 0.303 2

10201701 910 0.r7 0.0 0.0 1

10201702 910 0.13 0.0 0.0 2

10201901 0.01223 10. 10.0.0.0.0. 1. 1

10201902 0.01223 10. 10. 0. 0. 0. 0. L 2

0

* Iowa- pt=zm bono

1100100013 110.

1100110001

1100110140.0700

110012011 4

110013010.4

110014000

11001401560.5

11001501 100010000 0 110.2313 1

11001601000000000 0 010.2313 1

1100170100.0.0.1

110018010. 10. 10. 0. 0. 0.0. 1. 1

0

* Iowa pleawn walls

11002000 15 2 10.183

1100210001

110021014 0.2400

11002201 1 4

110023010.4

110024000

11002401 567.5

11002501 100010000 0 110.793 1

11002601 000000000 0 0 10.798 1

1100270100.0.0.1

110023010. 10. 10. 0.0.0.0. 1. 1

4

- do wa&ls ibL Iowa" hoc. pt

1105100095 2 10.04603

1105110001

11051101 40.092

11051201 1 4

110513010.4

110514000

11051401 567.5

11051501 1050100000 1 1 0.344 1

11051502 115010000 10000 11 0.323 3

11051503 125010000 0 110.3599

11051601-999 0 3100 10.344 1

11051602 -999 0 3100 10.823 3

11051603 -999 0 3100103599

1105170100.0.0. 9

110518010. 10. 10.0.0.0.0. 1. 1

11051:02 0. 10. 10. 0. 0. 0. 0. 1. 9

110513030. 10. 10. 0. 0. 0. 0. 1.9

110519010. 10. 10.0. 0. 0. 0. 1. 1

110519020. 10. 10.0.0.0.0. 1.3

11051903 0. 10. 10. 0. 0. 0. 0. 1. 9

0 lowa" pteumi walls pat ii

1110100035 2 10.076

1110110001

11101101 40.090

11101201 1 4

111013010.4

111014000

11101401 567.5

11101501 1000100000 110.264 1

11101502 110010000 0 110.753 2

11101503 120010000 0 110.486 3

127
11101601-999 0 3200 10.-7641

11101602-999 0 3200 10.7532

11101603-999 0 3200 10.4863

1110170100.0.0.3

111018010. 10. 10.0.0.0.0. 1.3

0 coanbypm wasl

1112100085 2 10.04284

1112110001

11121101 40.06032

111212011 4

111213010.4

111214000

11121401567.5

11121501 112010000 10000 111.015 2

11121502 112030000 10000 11 L3744

11121503 114010000 10000 111.081 6

11121504114030000 10000 111.0152

111216010000000000 011.0152

11121602000000000 0 011.3744

11121603000000000 0 01 1.0816

111216040000000000 011.0152

1112170100.0.0.2

1112101 0. 10. 10. 0. 0. 0. 0. 1. 3

odcwamltop oarwpat)

1125100025 210.0625

1125110001

11251101 40.0925

11251201 1 4

112513010.4

112514000

11251401 567.5

11251501 125010000 0 110.131 1

11251502 135010000 0 110.132 2

112516010000000000 010.131 1

11251602 00000000 0 010.132 2

1125170100.0.0. 2

112518010. 10. 10. 0. 0. 0. 0. 1. 1

11251W020.10.10.0.0.0.0.1.2

112519010. 10. 10. 0. 0. 0. 0. 1. 1

112519020. 10. 10.0.0.0.0. 1.2

rpvwalng. coneI

11301000 13 5 2 1 0.074t

1130110001

1130110140.125

11301201 1 4

113013010.4

113014000

11301401 567.5

11301501 130010000 10000 110.123 2

11301502 130030000 10000 110.366 10

11301503 130110000 10000 110.183 12

113015041400100000 1 1 0.382 13

11301601-999 0 3210 10.183 2

11301602-999 0 321010.366 10

11301603-999 0 3210 10.183 12

11301604-999 0 32101 0.382 13

1130170100.0.0. 13

113013010. 10. 10.0.0.0.0. 1.2

11301802 0. 10. 10. 0. 0. 0. 0. L 10

113018030. 10. 10.0.0.0.0. 1. 12

113018040.10.10.0.0.0.0.1.13

113019010.10.10.0.0.0.0.1.2

11301902 0. 10. 10. 0. 0. 0. 0. 1. 10

11301903 0. 10. 10.0.0.0.0. 1. 12

113019040. 10.10.0.0.0.0. 1. 13

11351000 15 110.

1135110001

11351101 4 0.05W0

11351201 1 4

11351301 0.4

113514000

11351401 60. 5

113515011350100000 110.0122 1

11351601000000000 0 0 10.0122 1

1135170100.0.0. 1

113518010. 10. 10. 0 0. 0. 0.01. 1 0

o do-up bmypas ws

114510005 5 2 10.01215

1145110001

11451101 40.0167

11451201 1 4

11451301 0.4

114514000

11451401 567. 5

11451501 145010000 0 111.201 1

11451502 145020000 10000 110.46 3

11451503 145040000 0 110.4154

11451504145050000 0 1 1 0.582 5

11451601-999 0 3225 1 1.201 1

11451602-999 0 3225 10.463 3

11451603-999 0 322510.415 4

11451604-999 0 322510.-52 5

1145170100.0.0. 5

114512010. 10.10. 0. 0. 0. 0. 1. 1

114512020.10.10.0.0.0.0.1.3

11451203 0. 10. 10.0.0.0.0. L 4

11451804 0. 10.10. 0. 0. 0. 0. L 5

114519010. 10. 10. 0. 0. 0. 0. L 1

11451902 0. 10.10.0.0.0.0.1.3

11451903 0. 10. 10.0.0.0.0. L 4

114519040. 10. 10. 0. 0. 0. 0. L 5 0

* rpv walls - upper pllargiwI

115010003 5 210.079

11501100 01

11501101 4 0.1025

11501201 1 4

115013010.4

115014000

11501401 567.5

115015011500100000 110.382 1

11501502 1600100000 110.682 2

11501503 170010000 0 110.936 3

11501601-999 0 322010.382 1

11501602-999 0 3220 1 068 2

11501603-999 0 322010.936 3

1150170100.0.0. 3

11501801 0. 10. 10. 0. 0. 0. 0. 1. 1

115012020. 10. 10. 0. 0. 0. 0. 1. 2

11501803 0.10.10.0.0.0.0. 1.3

115019010. 10. 10. 0. 0. 0. 0. 1. 1

115102 0. 10. 10.0.0.0.0. 1.2

11501903 0.10.10.0.0.0.0.1.3

*rpvwalk- upperad =region

112010003 5 2 1 0.0935

1120110001

112011014 0.1225

11801201 1 4

11801301 0.4

118014000

11801401 567. 5

11201501 180010000 0 1 1 0.936 1

11201502 190010000 10000 110.642 3

11801601-999 0 323010.936 1

11801602-999 0 3230 10.642 3

1120170100.0.0. 3

112012010. 10. 10. 0. 0. 0. 0.1.1

112018020.10.10.0.0.0.0.1.3

112019010. 10. 10. 0. 0. 0. 0.1. 1

112019020.10.10.0.0.0.0.1.3

0

* uppa head top plate

1190100015 110.

1190110001

119011014 0.0700

128
11901201 1 4

11901301. 4

119014000

11901401560.5

11901501 1900100000 1 10.0275 1

11901601000000000 0 0 10.0275 1

1190170100.0.0. 1

I1901101 0. 10. 10. 0. 0. 0. 0. 1. 1

• loop I h pipewalls

12001000 5 5 2 10.0333

12001100 0 1

12001101 4 0.0445

12001201 1 4

12001301 0.4

120014000

12001401 567.5

120015012000100000 110.792 1

12001502 210010000 0 110.791 2

12001503 220010000 10000 110.8725 4

120015042200300000 110.569 5

12001601-999 0 3300 1 0.732 1

12001602-999 0 3300 10.791 2

12001603-999 0 3300 1 0785 4

12001604-999 0 3300 10.569

120017010 0.0.0. 5

12001801 0. 10. 10. 0. 0. 0. 0. 1. 1

120012020.10. 10.0.0.0.0. 1.2

120018030.10. 10.0.0.0.0. 1.4

120013040. 10. 10.0.0.0.0. 1.5

120019010.10. 10.0.0. 0.0. 1. 1

120019020. 10. 10.0.0.0.0. 1.2

120019030.10.10.0.0.0.0.1.4

120019040. 10. 10.0.0.0.0. 1.5

4

4 loop I agti W & oute plena asall pipe walls

12201000 2 5 2 10.031

1220110001

12201101 40.036

122012011 4

12201301 0.4

122014000

12201401 567. 5

12201501 220040000 0 110.166 1

12201502 240010000 0 110.166 2

12201601 000000000 0 010.1662

1220170100.0.0. 2

12201301 0.10.10.0.0.0.0.1.2

122019010. 10. 10.0.0.0.0. 1.2

l kop 1 asklet & ouddt lena I-Pre 1 pWalls

122020002 5 2 1 0.054

1220210001

12202101 4 0.064

12202201 1 4

122023010.4

122024000

12202401 567. 5

12202501220040000 0 110.110 1

122025022400100000 110.110 2

122026010000000000 010.110 2

1220270100.0.0. 2

122022010. 10. 10.0.0.0.0. 1.2

122029010. 10.10.0.0.0.0. 1.2

: loop 1 sep. wall bdwcen idt ,and outet plena

1220300013 110.

1220310001

12203101 2 0.010

12203201 1 2

122033010.2

122034000

12203401 560.3

12203501 220040000 0 110.04771

12203601240010000 0 110.0477 1

1220370100.0.0. 1

122033010.10.10.0. 0. 0. 0. 1. 1

122039010. 10. 10.0.0.0.0. 1. 1

0

0 loop I sgplat1 (ecai. wighs - assinndisolatW Mfl Uck.)

1220400025 110.

122041000 1

12204101 40.045

12204201 1 4

12204301 0.4

122044000

12204401 6O. 5

12204501220040000 0 110.0710 1

12204502 240010000 0 110.0710 2

12204601000000000 0 0 10.0710 2

1220470100.0.0.2

12204800. 10. 10. 0. 0. 0.0. 1.2

122049010. 10. 10.0.0.0.0.1.2 *

loop 1 sg u-tbes wals

12301000 I 5 2 10.00771

1230110001

123011014 0.00873

1230120124

12301301 0.4

12301400 0

12301401567.5

12301501230010000 10000 116.500 2

12301502 230030000 10000 11 13.00 8

12301503 230090000 10000 1116.614 10

123015042301100000 1113.00 12

12301505 2301200000 1 1 13.00 14

12301506 230130000 0 1 1 13.00 16

12301507 2301400000 1 1 6.500 13

12301601 500010000 10000 1 1 6-500 2

12301602 500030000 10000 11 13.00 8

12301603 50000000 1 1 16.61410

12301604 5S0080000 -10000 1113.00 16

12301605 500020000 -10000 116.500 16

1230170100.0.0. 13

123013010. 10. 10. 0. 0. 0. 0. 1. 1I

123019010. 10. 10. 0. 0. 0. 0. 1. 18

Sloopl cold leg pipewvalls (igto punp)

124010009 5 210.0246

1240110001

124011014 0.0302

124012011 4

124013010.4

124014000

12401401567.5

124015012400200000 110.569 1

12401502 250010000 0 1 1 0.893 2

124015032600100000 110.859 3

12401504 260020000 10000 11 1.021 6

12401505 260050000 0 110.727 7

12401506 260060000 0 11 1503 8

12401507260070000 0 11 1.200 9

12401601-999 0 3310 10.569 1

12401602-999 0 3310 10.898 2

12401603 -999 0 3310 1 0.59 3

12401604-999 0 331011.021 6

12401605-999 0 3310 10.727 7

12401606-999 0 3310 1 L503 3

12401607-999 0 3310 1 1.200 9

1240170100.0.0. 9

124018010. 10. 10.0.0.0.0. 1.9

124019010. 10. 10.0.0.0.0. 1.9

loop 1 pump wall

12701000 1 5 2 10.033

1270110001

127011014 0.083

127012011 4

12701301 0.4

127014000

12701401567.5

129
12701501 270010000 0 1 10.520 1

12701601-999 0 3320 10.520 1 -999 3320

12701701 00.0 . 0. 1

12701301 0. 10. 10. 0. 0. . 0.1. 1

127019010. 10. 10. 0. 0. 0. 0. L 1

: loop I cold Leg pipe wall (pump to qpv)

128010004 5 210.0295

1280110001

12801101 4 0.0365

12801201 1 4

128013010.4

128014000

12801401 567. 5

128015012750100000 1 10.723 1

128015022800100000 1 10.723 2

12801503 285010000 0 1 10.723 3

12801504 290010000 0 1 1 0.723 4

12801601-999 0 33301 0.723 1

12801602-999 0 33301 0.723 2

12801603-999 0 3330 1 0.723 3

12801604-999 0 33301 0.723 4

1280170100.0.0. 4

128018010. 10. 10.0.0.0.0. 1.4

128019010. 10. 10.0.0.0.0.1.4 *

* loop 2 ht leg pim walls

13001000 5 5 2 10.0333

1300110001

13001101 40.0445

130012011 4

13001301 0.4

13001400 0

13001401 567. 5

13001501 3000100000 1 1 0.72 1

13001502 310010000 0 110.731 2

13001503 320010000 10000 11 0.75 4

130015043200300000 110.569 5

13001601-999 0 3300 1 0.782 1

13001602-999 0 3300 10.731 2

13001603-999 0 3300 1 0.375 4

13001604-999 0 330010.569 5

1300170100.0.0. 5

130018010. 10.10.0.0.0.0. 1.5

130019010. 10. 10.0.0.0.0.1.5

: loop 2 g inlet & outlet plma small pipe walls

132010002 5 210.031

1320110001

132011014 0.036

132012011 4

132013010.4

132014000

13201401 567.5

132015013200400000 110.166 1

13201502 340010000 0 1 10.166 2

13201601000000000 0 010.1662

1320170100.0.0. 2

13201801 0. 10.10.0.0.0.0. 1.2

132019010. 10.10.0.0.0.0.1.2

• lop 2 sg inlt & outlet plam lar pipe walls

132020002 5 2 10.054

1320210001

13202101 4 0.064

132022011 4

132023010.4

132024000

13202401567.5

132025013200400000 11 0.110 1

13202502 340010000 0 11 0.110 2

13202601 000000000 0 010.110 2

1320270100.0.0. 2

13202801 0. 10.10. 0. 0. 0. 0. 1. 2

13202901 0.10.10.0.0.0.0.1.2

* loop 2 sep. waU bween inlet and outlet plns

13203000 13 110.

1320310001

1320310120.010

132032011 2

13203301 0.2

132034000

13203401 560. 3

13203501320040000 0 110.0477 1

13203601340010000 0 110.0477 1

1320370100.0.0.1

132038010. 10. 10. 0. 0. 0. 0. L 1

132039010. 10.10. 0. 0. 0. 0.1.1

* loop 2 sg plate (p=. wih as - asumd Woited, 1/2 *hi)

1320400025 110.

1320410001

132041014 0.045

132042011 4

132043010.4

132044000

13204401560.5

13204501320040000 0 110.0710 1

13204502 340010000 011 0.0710 2

1320460100000 0 0 10.0710 2

13204701 0.0.0.2

132048010. 10. 10.0.0.0.0.1.2

132049010. 10. 10.0.0.0. 0. 1.2

* loop 2 sg u-tubcs walls

13301000 It5 2 10.00771

1330110001

133011014 0.00873

133012012 4

133013010.4

133014000

13301401 567.5

13301501330010000 10000 116.500 2

13301502330030000 10000 11 13.00 3

13301503 330090000 10000 1116.61410

133015043301100000 1113.00 12

13301505 3301200000 1113.00 14

133015063301300000 1113.00 16

13301507 330140000 0 1 1 6.500 18

13301601 600010000 10000 1 16.500 2

13301602 600030000 10000 11 13.00 8

13301603 600090000 0 1116.61410

13301604 600080000 -10000 1 1 13.00 16

13301605 600020000 -10000 1 1 6.500 13

1330170100.0.0. 13

133018010. 10. 10.0. 0. 0. 0. 1. 13

13301901 0. 10. 10. 0. 0. 0.0. 1. 13

• loop 2 cold leg pipe walls (Sgto pump)

13401000 9 5 2 10.0246

1340110001

134011014 0.0302

134012011 4

134013010.4

134014000

13401401567.3

13401501340020000 0 110.569 1

13401502 3500100000 110.398 2

13401503 3600100000 1 10.359 3

13401504 360020000 10000 11 1.021 6

13401505 360050000 0 1 10.727 7

13401506 360060000 0 111.503 3

134015073600700000 111.200 9

13401601-999 0 3310 1 0.569 1

13401602-999 0 3310 1 0.893 2

13401603-999 0 33101 0.359 3

13401604-999 0 33101 1.021 6

13401605-999 0 331010.727 7

13401606-999 0 3310 11.503 3

13401607-999 0 3310 11.200 9

134017010 0.0.0. 9

130
134018010. 10. 10.0.0.0.0. 1.9

134019010. 10. 10.0.0.0.0. 1.9

: loop 2 pump wall

13701000 1 5 2 1 0.033

1370110001

137011014 0.083

13701201 1 4

137013010.4

137014000

13701401567.5

13701501 3700100000 110.520 1

13701601-999 0 3320 10.520 1 -99

1370170100.0.0. 1

137018010. 10. 10. 0. 0. 0. 0. 1. 1

137019010. 10. 10. 0. 0. 0. 0. 1. 1

I loop 2 cold kg Pipe wall (pump to zpv)

138010004 S 2 1 0.0295

1380110001

1380110140.0365

13801201 1 4

13801301 0.4

132014000

13801401567.5

138015013750100000 110.723 1

138015023800100000 110.723 2

13801503 385010000 0 110.723 3

138015043900100000 110.723 4

13801601-999 0 3330 10.723 1

13801602 -999 0 3330 1 0.723 2

13801603-999 0 3330 10.723 3

13801604 -999 0 3330 1 0.723 4

1380170100.0.0. 4

138018010. 10. 10.0.0.0.0. 1.4

138019010. 10. 10.0.0.0.0. 1.4 0

loop 3 hot egppewalls

14001000 5 5 2 10.0333

1400110001

14001101 4 0.0445

14001201 1 4

14001301 0.4

140014000

14001401567.5

14001501400010000 0 110.782 1

14001502 410010000 0 110.781 2

14001503 420010000 10000 11 0.8785 4

140015044200300000 110.569 5

14001601-999 0 3300 10.782 1

14001602-999 0 3300 10.781 2

14001603-999 0 3300 1 0.785 4

14001604 -999 0 330010.569 5

1400170100.0.0. 5

140018010 . 10. 10.0.0.0.0. 1. 5

140019010. 10. 10. 0. 0. 0. 0. L 5 0

: loop 3 og inlet & cutlet plena mull pipc wafll

142010002 5 2 10.031

1420110001

142011014 0.036

142012011 4

142013010.4

142014000

14201401567.5

14201501 420040000 0 110.166 1

14201502 440010000 0 1 10.166 2

14201601000000000 0 0 10.166 2

1420170100.0.0. 2

14201801 0. 10. 10.0.0.0.0. 1.2

14201901 0. 10. 10.0.0.0.0. 1.2 0

: loop 3 mg inlet & outlet pleat larg pipe walls

142020002 5 2 1 0.054

142021000 1

142021014 0.064

3320

14202201 1 4

142023010.4

142024000

14202401567.5

142025014200400000 110.110 1

142025024400100000 110.1102

14202601000000000 0 010.110 2

1420270100.0.0. 2

142028010. 10. 10.0.0.0.0. 1.2

14202901 0.10.10.0.0.0.0.1.2 0

"loop 3 sep. wall betwen inl tad ou tlenpam

14203000 13 110.

1420310001

142031012 0.010

14203201 1 2

142033010.2

142034000

14203401 560.3

14203501 4200400000 110.0477 1

14203601440010000 0 1 1 0.0477 1

1420370100.0.0. 1

142038010. 10. 10. 0. 0. 0. 0. 1. 1

142039010. 10. 10.0.0.0.0. 1. 1

* loop 3 sgplate (cim. with as- asuned isolated, 1f l*,,)

1420400025 110.

142041000 1

142041014 0.045

142042011 4

14204301 0.4

142044000

14204401560.5

142045014200400000110.07101

14204502 4400100000 110.07102

14204601000000000 0 0 10.0710 2

1420470100.0.0.2

142048010. 10. 10.0. 0.0.0. 1.2

142049010. 10. 10.0.0.0.0. 1. 2 0

Sloop 3 sguu4nbes wals

1430100018 5 2 10.00771

143011000 1

143011014 0.00873

1430120124

143013010.4

143014000

14301401567.5

14301501 430010000 10000 116.500 2

14301502 430030000 10000 11 13.00 8

14301503 430090000 10000 1 1 16.614 10

143015044301100000 1113.00 12

14301505 4301200000 1113.00 14

14301506 430130000 0 1 1 13.00 16

14301507 430140000 0 11 6.500 18

14301601 700010000 10000 1 16.500 2

14301602 700030000 10000 1 1 13.00 8

143016037000900000 1116.61410

14301604 700080000 -10000 11 13.00 16

14301605 700020000-10000 116.500 18

14301701 0.0.0. 18

14301801 0. 10. 10. 0. 0. 0. 0. 1. 18

143019010. 10. 10. 0. 0. 0. 0. 1. 18 0

* loop 3 cold leg pipe walls (sglo pump)

14401000 9 5 2 10.0246

1440110001

14401101 4 0.0302

144012011 4

144013010.4

144014000

14401401 567.5

14401501440020000 0 110.569 1

14401502 450010000 0 11 0.98 2

14401503 460010000 0 110.859 3

14401504 460020000 10000 111.021 6

131
14401505 460050000 0 110.727 7

14401506 460060000 0 111.503 3

14401507 460070000 0 111.2009

14401601 -999 0 331010.569 1

14401602 -9" 0 331010.893 2

14401603-999 0 331010.359 3

14401604-999 0 33101 1.021 6

14401605-999 0 3310 10.727 7

14401606-999 0 331011.503 2

14401607-999 0 3310 11.200 9

1440170100.0.0. 9

144018010. 10.10.0.0.0.0. 1.9

144019010.10.10.0.0.0.0. 1.9

* loop 3 pump wal

147010001 5 210.033

1470110001

14701101 4 0.023

14701201 1 4

147013010.4

147014000

14701401567.5

147015014700100000 110.520 1

14701601-999 0 3320 10.520 1 -999 3320

1470170100.0.0. 1

147012010. 10. 10.0.0.0.0. 1. 1

147019010. 10. 10. 0. 0. 0. 0. 1. 1

* loop 3 cold leg pipe wall (pump to rpv)

143010004 S 21 0.0295

1480110001

14301101 4 0.0365

143012011 4

148013010.4

14801400 0

14301401 567. 5

14301501475010000 0 110.723 1

14801502 430010000 0 110.723 2

14201503 485010000 0 110.723 3

14301504490010000 0 110.723 4

14301601-999 0 3330 10.723 1

14801602-999 0 3330 0.723 2

14201603-999 0 3330 10.723 3

14D01604-999 0 3330 10.723 4

1480170100.0.0. 4

142012010. 10.10.0.0.0.0. 1.4

143019010. 10. 10.0.0.0.0. 1.4

0 loop lsg. risw waU (oquivalt s-uct)

15001000 125 21 0.026

1500110001

1500110140.112

150012011 4

150013010.4

150014000

15001401 %67.5

15001501 500010000 10000 110.500 2

15001502 500030000 10000 111.000 8

15001503 500090000 0 1 11.27

15001504500100000 10000 111.1645 11

15001505 5001200000 1 1 1.097 12

15001601-999 0 34001 0.500 2

15001602-999 0 3400 1 LOOG 8

15001603-999 0 3400 1 273 9

15001604-999 0 340011.164511

15001605-999 0 34001 1.097 12

15001701 00. 0.. 12

150012010. 10.10.0.0.0.0. 1.12

150019010. 10.10.0.0.0.0. 1.12

,loop lsg n spastor inmtWa waM (qauiv. sru±)

151010004 3 210.050

1510110001

15101101 2 0.053

15101201 1 2

15101301 0.2

151014000

15101401567.3

15101501510010000 0 111.000 1

13101502 510010000 0 1 1 1.261 2

15101503 520010000 0 1 1 9.000 3

15101504 00120000 0 1 1 1.042 4

15101601 540010000 0 111.000 1

15101602 530010000 0 111.261 2

15101603 000000000 0 019.0003

15101604 5600100000 1 1 1.042 4

1510170100.0.0. 4

151012010. 10.10. 0. 0. 0. 0. 1. 4

151019010. 10.10.0.0.0.0.1.4

* loop 1sgtart d=4m ex al wals

15201000 1 5 210.254

1520110001

152011014 0.294

152012011 4

152013010.4

152014000

15201401567.5

15201501 520010000 0 11 L355 1

15201601-999 0 34101 1.355 1

1520170100.0.0. 1

152012010.10. 10. 0. 0. 0. 0. 1. 1

152019010.10.10. 0. 0. 0. 0. L I

* loop lsgdowncoa= smzzlurpa wz b

153010003 5 210.094

1530110001

15301101 40.111

153012011 4

15301301 0.4

153014000

15301401567.5

15301501 530010000 0 1 10.961 1

15301502 540010000 0 111.000 2

153015035 6010000 0 11 1.042 3

15301601-999 0 3420 10.61 1

15301602-999 0 342011.000 2

15301603-999 0 342011.042 3

15301701 00.0.0. 3

15301801 0. 10. 10.0.0.0.0. 1.3

15301901 0.10. 10.0.0.0.0. 1.3

* loop lsg dowoamatdtuhular pawt walb

15701000 5 5 2 10.0215

15701100 0 1

1570110140.02425

15701201 1 4

157013010.4

15701400 0

15701401 567. 5

15701501570010000 10000 1 14.4002 5

15701601-999 0 3430 1 t4008 5

1570170100.0.0. 3

157012010.10.10. 0. 0. 0. 0.1. 5

157019010. 10. 10. 0. 0. 0. 0. 1.5

0

* loop 2sS a riswr wa&ls ( ,iva sua)

16001000 12.5 2 10.026

1600110001

160011014 0.112

160012011 4

160013010.4

160014000

16001401 567.5

16001501 600010000 10000 110.500 2

16001502,600030000 10000 111.000 2

16001503 600090000 0 11 LX729

16001504 600100000 10000 11 1.1645 11

16001505 600120000 0 111.097 12

16001601-999 0 3400 1 0.500 2

16001602-999 0 34001 1.000 2

16001603-999 0 3400 11.271 9

132
16001604-999 0 34001 1.164511

16001605-999 0 34001 1.097 12

1600170100.0.0. 12

160018010. 10. 10.0.0.0.0. 1.12

160019010. 10. 10.0.0.0.0.1. 12 S

* loop 2m g sepamr mesmal walls (eqmiv. mtut)

16101000 4 3 2 10.050

1610110001

161011012 0.053

16101201 1 2

161013010.2

161014000

16101401 567.3

161015016100100000 111.000 1

161015026100100000 111.261 2

16101503 620010000 0 1 1 9.000 3

161015046001200000 1 1 1.042 4

161016016400100000 1 1 1.000 1

16101602 630010000 0 11 1.261 2

16101603 000000000 0 019.0003

16101604660010000 0 1-1 1.042 4

1610170100.0.0. 4

161012010. 10. 10. 0. 0. 0.0. 1.4

161019010. 10. 10. 0. 0.0. 0. 1.4 S

* loop 2ag steam dame caIaml walls

16201000 1 5 2 10.254

1620110001

16201101 40.294

16201201 1 4

162013010.4

162014000

16201401 567. 5

162015016200100000 111.355 1

16201601-999 0 341011355 1

1620170100.0.0. 1

162018010. 10. 10. 0. 0. 0. 0. 1. 1

162019010. 10. 10. 0. 0. 0. 0. 1. 1

: boop 2sg dowwomncr -nnla put walls

163010003 5 210.094

1630110001

1630110140.111

16301201 1 4

16301301 0.4

163014000

16301401 567. 5

163015016300100000 110.961 1

16301502 640010000 0 1 1 1.000 2

16301503 660010000 0 111.0423

16301601-999 0 342010.961 1

16301602 -999 0 3420 11.000 2

16301603.999 0 3420 11.042 3

1630170100.0.0. 3

163013010. 10. 10. 0.0. 0. 0. 1.3

163019010.10.10. 0.0. 0.0.1.3

4

* loop 3sg downomer tubular part walls

16701000 5 5 2 10.0215

1670110001

1670110140.02425

167012011 4

167013010.4

167014000

16701401567.5

16701501670010000 10000 1 14.40085

16701601-999 0 3430 14.4008 5

1670170100.0.0. 5

167018010. 10. 10.0. 0. 0. 0. 1. 5

167019010. 10. 10.0.0.0.0.1. 5

* loop 3ag is cis= walls (eqi s.&a)

17001000 12 5 2 10.086

1700110001

170011014 0.112

170012011 4

170013010.4

170014000

17001401 567.5

17001501 700010000 10000 110.500 2

17001502 700030000 10000 11 1.000

17001503 700090000 0 111.27 9

17001504700100000 10000 111.1645 11

17001505 700120000 0 111.097 12

17001601 -999 0 3400 1 0.500 2

17001602-999 0 3400 11.000 2

17001603 -9 0 340011.278 9

17001604-999 0 34001 1.1645 11

17001605 -999 0 34001 1.097 12

1700170100.0.0. 12

170018010. 10. 10.0.0.0.0.1. 12

170019010.10.10.0.0.0.0.1.12

0 lowp 3sg as acpanior idntna walls (equiv. 9aCL)

171010004 3 2 10.050

1710110001

17101101 2 0.053

17101201 1 2

171013010.2

171014000

17101401 567.3

17101501710010000 0 111.000 1

171015027100100000 1 11.261 2

17101503 720010000 0 1 19.000 3

171015"4700120000 0 111.042 4

17101601740010000 0 111.000 1

17101602 730010000 0 111.261 2

171016030000000000 019.0003

17101604 760010000 0 111.042 4

17101701 0.0. 0. 4

17101801 0. 10. 10.0.0.0.0.1.4

17101901 0. 10. 10.0.0.0.0. 1.4

S

0 loop 3sg tearm dome extea walls

17201000 1 5 2 1 0.254

1720110001

17201101 40.294

17201201 1 4

17201301 0.4

172014000

17201401 567.5

17201501 720010000 0 111.355 1

17201601-999 0 341011355 1

1720170100.0.0. 1

172011010. 10. 10. 0. 0. 0.0. 1. 1

172019010. 10. 10. 0. 0. 0.0. 1.1

* oWp 3mg dowucoc -1-a part walls

173010003 5 210.094

1730110001

1730110140.111

173012011 4

173013010.4

173014000

17301401567.5

17301501730010000 0 110.961 1

17301502 740010000 0 11 .000 2

17301503 760010000 0 111.042 3

17301601-999 0 3420 10.961 1

17301602 -999 0 342011.000 2

17301603-999 0 3420 11.042 3

1730170100.0.0. 3

173011010. 10. 10.0. 0.0.0. 1.3

173019010. 10. 10.0.0.0.0. 1.3

4 loop 3sg downc•c• tbdar pat walls

177010005 5 210.0215

1770110001

177011014 0.02425

177012011 4

17701301 0.4

1 33
177014000

17701401567.5

17701501 770010000 10000 114.4002 5

17701601-999 0 343014.40085

1770170100.0.0. 5

177018010. 10.10. 0. 0. 0. 0.1. 5

177019010.10.10.0.0.0.0. 1.5

* core active ze (94 rods- low power)

19000000 12 62 1 0.00395

190001000 1

19000101 5 0.00475

19000201 2 5

19000301 1. 5

190004000

19000401 527.6

190005010 0 0 1 17.202 2

190005020 0 0 1 34.404 10

190005030 0 0 1 17.202 12

19000601 130010000 10000 111 1 17.202

19000602 130030000 10000 111 1 34.404

19000603 130110000 10000 111 1 17.202

L9000719000.041250. 0. 2

19000702 900 0.0962500 . 0. 10

2

10

12

19000703 900 0.043125 0. 0. 12

190009O01

190009010.0.0915 0.0915 0.2325 0.1375 0.5 0.5

1.31

19000902 0.0.0915 0.0915 0.0495 0.3205 0.5 0.5

1.32

19000903 0. 0.133 0.183 0.275 0.225 0.5 0.5

1.33

190009040. 0.133 0.123 0.409 0.091 0.5 0.5

1.34

19000905 0. 0.183 0.183 0.043 0.475 0.5 0.5

1.35

19000906 0.0.123 0.183 0.177 0.323 0.5 0.5

1.36

190009070.0.193 0.183 0.311 0.189 0.5 0.5

1.37

19000908 0.0.183 0.133 0.445 0.055 0.5 0.5

1.38

19000909 0.0.183 0.183 0.079 0.421 0.50.5

1.39

19000910 0. 0.183 0.133 0.213 0.227 0.5 0.5

1.310

190009110.0.0915 0.0915 0.4385 0.0615 0.5 0.5

1.311

19000912 0.0.0915 0.0915 0.2555 0.2445 0.5 0.5

1.312

0 core rods (97 rods -zao power - lower planm)

191000003 3210.00200

1910010001

191001012 0.00475

191002013 2

191003010. 2

191004000

19100401527.3

191005010 0 0 1 77.406 1

191005020 0 0 1 73.041 2

191005030 0 0 1 47.142 3

19100601 100010000 0 1 1 77.406 1

19100602110010000 0 1 1 73.041 2

19100603 120010000 0 1 1 47.142 3

191007010 0. 0.0. 3

191009010. 10.10. 0. 0. 0. 0.1.1

19100902 0. 10. 10.0.0.0.0. 1.2

19100903 0. 10.10.0.0.0.0. 1.3 S

* core rods (97 rods - zao powr- uppar plamut)

19200000 1 3 210.

192001000 1

19200101 2 0.00335

192002014 2

192003010. 2

1.3.66 1.326

1.3.66 1.326

1.3.66 1.326

1.3.66 1.326

1. 3.66 1.326

1. 3.66 1.326

1. 3.66 1.326

1. 3.66 1.326

1.3.66 1.326

1.3.66 1.326

1.3.66 1.326

1.3.661.326

192004000

19200401587.3

192005010 0 0 1 37.054 1

19200601 140010000 0 1 1 37.054 1

192007010 0. 0.0. 1

19200901 0. 10. 10. 0. 0. 0. 0. 1.1

core activve zrn (3 rods.- i&h powar)

1950000012 62 10.00375

1950010001

19500101 5 0.00475

195002012 5

19500301 1. 5

195004000

19500401527.6

19500501 0 0 0 1 0.549 2

195005020 0 0 1 1.098 10

195005030 0 0 1 0.549 12

19500601 130010000 10000 111 1 0.549 2

19500602130030000 10000 111 1 1.092 10

19500603 130110000 10000 111 1 0.549 12

19500701900 0.00175 0. 0. 2

1950702 900 0.003750 0. 0. 10

19500703 900 0.001875 0. 0. 12

195009001

19500901 0.0.0915 0.0915 0.2325 0.1375 0.5 0.5 L 3.66 1.326

131

19500902 0.0.0915 0.0915 0.0495 03205 0.5 0.5 1.3.66 1.326

13 2

19500903 0. 0.183 0.133 0.275 0.225 0.5 0.5 1.3.66 1.326

133

19500904 0.0.183 0.183 0.409 0.091 0.5 0.5 1.3.66 1.326

134

19500905 0.0.183 0.183 0.043 0.475 0.5 0.5 1.3.66 1.326

1.35

19500906 0. 0.183 0.183 0.177 0323 0.5 0.5 1.3.661326

136

19500907 0. 0.183 0.183 0311 0.189 0.5 0.5 1.3.66 1326

137

19500908 0. 0.183 0.183 0.445 0.055 0.5 0.5 1. 3.66 1.326

132

19500909 0.0.133 0.133 0.079 0.421 0.5 0.5 L 3.66 1.326

139

19500910 0.0.133 0.133 0.213 0.227 0.5 0.5 1. 3.66 1.326

1.310

195009110.0.0915 0.0915 0.4385 0.0615 0.5 0.5 1.3.66 1326

1311

19500912 0.0.0915 0.0915 0.2555 0.2445 0.5 .L 3.66 1326

1312

Smatriah'tables

20100100 tb1x 1 1

20100200 tbl/frn 1 1

20100300 W1f 1 1

20100400 /fft 1 1

20100500 U/ft 11

20100101 93.14.700

20100102 2073.18.60

* heat capacity &Lk)

20100151 93. 3.62e6

20100152 2073. 4.21e6 4

I inc 600 (vense) cm ctiv (w/m&)

20100201 13. 12.

20100202 473. 15.5

20100203 573. &l1

20100204700. 20.4

20100205 922. 243

20100206 1033. 26.9

20100207 1144. 29.4

134
20100208 1477. 36.1

201002092477. 36.1

* U t•he capacity W Ug)

20100251 13. 3.46e6

20100252 373. 3.67c6

20100253 473. 3.97e6

20100254 573. 4.05e6

20100255 673. 4.26c6

20100256 2073. 436e6

* CoppW coma ors 0uctiv* (whm/t)

20100301 93. 390.2

20100302 533. 3749

20100303 813. 373.0

20100304 1082. 364.8

20100305 2800. 355.0 *

* bad cqwi, GWmcg)

2010035193. 3.75c6

20100352 1000. 4.05.6

20100353 2073. 405c6

* z.1200 conducfivity (win/k)

20100401 93. 79.2

20100402 533. 61.9

20100403 813. 59.0

20100404 108l. 64.3

20100405 2800. 67.0

2010045193. 4.05.6

20100452 2073. 4.0506 a

* borna niri

20100501 293. 33-9

20100502 300. 34.9

20100503 400. 32.3

20100504 500. 29.9

20100505 600. 27.7

20100506 700. 26.4

20100507 300. 25.4

20100508 900. 24.5

20100509 1000. 23.7

201005101050. 23.3

20100511 1500. 22.9

-" d copack OW

20100551 293. 1.55.6

20100552 300. 1.55o6

20100553 400. 2.14c6

20100554 500. 2.53e6

20100555 600. 2.84e6

20100556 700. 3.09c6

20100557 800. 3.31c6

20100552 900. 3.48.6

20100559 1000. 3.64.6

20100560 1050. 3.77e6

20100561 150. 3-95.6

•gen.• tdAbe

* Iowa plamn vessl walls hbe loses

20220000 htct.

20220001 0. 27.

20220002 1U6 27.

Score regien vessel walls hea losses

20221000 blot

20221001 0. 16.

20221002 1.C6 16.

: uppcrpl•pm vessel walls hed losses

20222000 W4

20222001 0 35.

20222002 300. 35.

20222003 310. 135. 35nwlpre20222004 1000. 335. * 35 nel pv20222005 1010. 35. *35 ae pro20222006 1.e6 35.•5*'' *0

* do-up bypass walh eat loses

20222500 bb

20222501 0. 40.

20222502 le6 40.

: upper head vased walls hea losses

20223000 W4

20223001 0. 12.

20223002 300. 12.

20223003 310. 112.

20223004 1000. 112.

20223005 1010. 12.

20223006 l.x6 12.

S

* ho legs 1&2&3 walls ha• losses

20230000 htb20230001 0. 9.

20230002 1.U6 9.

* loop weals 1&2&3 walls heal loses

20231000 4

20231001 0. 23.

20231002 1e6 23.

:pumps 1&2&3 walls heat los

20232000 htc-t

20232001 0. 400.

20232002 1000. 400.

20232003 3200. 400.

20232004 le6 400. a

* cold legs 1&2&3 walls bealt Ios

20233000 W4t

20233001 0. 11S.*29couisp.a43+26kw

20233002 1.e6 115.

oag• 1U2&3 rser iwalls loskm

20240000 hto4

20240001 0. 4. *4.

20240002 300. 4. *4.

20240003 310. IA *4.

20240004 1*6 IA * 4.

S

* ag a 1&2&3 gteam dome walls heal Ioaes

20241000 htc4

20241001 0. 1.3 *63

20241002 300. 1.3 * 6.3

20241003 310. 0.3 *6.3

20241004 1..6 0.3 •6.3

* sg asl&2&3 u-d walls he losses

20242000 Wac4

20242001 0. 15. *15.

20242002 300. 15. *15.

20242003 310. 3.5 0 15.

20242004 1.6 3.5 * 15. 0

* dc wall hea lomses

20210000 ht,.t

20210001 -1.0 0.0

20210002 0. 14.

20210003 1.C6 14.

* uwge line beat losses

20210100 hto-t

20210101 -1.0 0.0

20210102 0. 21. * 7. inpre4st

20210103 1*6 21. 0""

4

135
*sgn 1&2&3 l.dcwallsbeslosse

20243000 lMtM

20243001 0. 10. * 10.

20243002 300. 10. $ 10.

20243003 310. 1.0 * 10.

20243004 l.c6 1.0 010. a

* cam' powertablo

20290000 powcr 575 1.0 1.e3

20290001 -1.762.

20290002 0. 76&.

20290003 99.9 762.

20290004 100. 761.1

20290005 102. 767.7

20290006 106. 762.3

20290007 10&. 61&.3

20290008 113. 613.4

20290009 12L 600.1

20290010 135. 591.9

20290011 149. 585.7

20290012 160. 575.0

20290013 170. 552.5

20290014 180. 503.1

20290015 190. 454.3

20290016 200. 412.7

20290017 210. 395.5

20290018 220. 360.5

20290019 240. 30&.0

20290020 250. 299.3

20290021 300. 223.5

20290022 400. 152.5

20290023 500. 136.5

20290024 700. 123.4

2029.005 900. 114.0

20290026 1100. 10&.7

20290027 1300. 102.9

20290022 1500. 9&.9

20290029 1900.94.6

20290030 2100. 91.5

20290031 2132. 90.2

20290032 2300. 90.2

20290033 1.e6 90.2

* pm heater power decay table

20291000 powea 570 1.0 10.57e3

20291001 0. 1.

20291002 1. 0.

20291003 1.6 0.

: avfr npea•• u table (far het-loss)

20299900 temp 501

20299901 -1. 320.

20299902 0. 320.

20299903 1.6 320. v

* €oafrolvariablesn

20500203

20500204

20500205

20500206

20500207

20500208

0

1.042

2.1324

2.1324

2.1324

2.1324

2.1324

vowd

vowd!

vowd! vowl

560010000

570010000

57O02O0OO

570030000

570040000

570050000

* doncom:er Iv LS.2

20500300 ddcs2 m= 1. 0. 1

20500301 0. 0.961 voW 630010000

20500302 1.000 void! 640010000

20500303 1.042 voWId 660010000

20500304 2.1324 void! 670010000

20500305 2.1324 void! 670020000

20500306 2.1324 void! 670030000

20500307 2.1324 void! 670040000

20500302 2.1324 v" 670050000

0

* downoomer ICVC1L53

20500400 ddVs3 sum 1.

20500401 0. 0.961 vod

20500402 LOGO voidf

20500403 1.042 voidf

20500404 2.1324 void!

20500405 2.1324 voi

20500406 2.1324 voWid

20500407 2.1324 vod

20500408 2.1324 voidf

Stotal nmm (pEM71 d&1)

20501000 knI sum 1.

20501001 0. 9.370560o..4 ho

20501002 2.644320o.4 dho

20501003 12.064000o4 zho

20501004 9.280000o-4 fto

20501005 9.2800004 dzo

20501006 9.56760o.4 rho

20501007 3.504000o.3 rho

20501002 9.532000(-.3 d

20501009 9.647232o.3 rho

20501010 9.647232a-3 tho

20501011 9.647232z-3 tho

20501012 9.647232o-3 rho

20501013 9.647232o-3 rho

20501014 9.647232-.3 zho

20501015 9.647232o-3 dbo

20501016 9.647232a-3 &ha

20501017 4.734000o-2 rho

20501012 2.296640-3 sho

20501019 2.486310o-3 rho

0. 1

730010000

740010000

760010000

770010000

770020000

770030000

770040000

77005OOOO

0. 1

010010000

010020000

010030000

010040000

010050000

010060000

015010000

020010000

02501OO00

025020000

025030000

025040000

025050000

025060000

030010000

035010000

100010000

105010000

110010000

0. I

112010000

112020000

112030000

112040000

114010000

114020000

114030000

114040000

115010000

115020000

115030000

115040000

115050000

115060000

115070000

120010000

125010000

0. 1

130010000

130020000

130030000

130040000

S prenuriLlid

20500100 pr'MvI mn 1. 0. 1

20500101 0. 0.679 void! 015010000

20500102 0.679 void! 02O010000

20500103 0.679 void! 025010000

20500104 0.679 voidf 025020000

20500105 0.679 voudf 025030000

20500106 0.679 voidf 025040000

20500107 0.679 voidf 025050000

20500108 0.679 void 025060000

20500109 0.679 voidf 030010000

20500110 0.679 void! 035010000

0

20501100

20501101

20501102

20501103

20501104

20501105

20501106

20501107

20501108

20501109

20501110

20501111

20501112

20501113

20501114

20501115

20501116

20501117

0

t2 sum 1.

0. 1.462615o.3 6o

1.4626150-3 rh

1.979934o-3 rho

1.979934.3 ft

1.557721o-3 do

1.557721o-3 ft

1.462615-3 rho

1.462615o-3 dho

5.47788W3

5.4778810-3

5.477280o.3

5.47788-3

5.4778o-3

5.477880o-3

5.477220o-3

3.26140003

rho

dbo

dho

zho aba

zho

zho

a dowmcomcrlcvc&&l

20500200 dchg um 1.

20500201 0. 0361 vod

20500202 1.000 vow

0. 1

530010000

540010000

20501200 tin3 sm 1.

20501201 0. 1.765584o-3 rho

20501202 1.765584-3 :ho

20501203 3.5311686-3 rho

20501204 3.53116W-3 fh

136
2050120O

20501206

20501207

20501208

20501209

20501210

20501211

20501212

20501213

20501214

20501215

20501216

20501217

20501213

20501219

20501220

3.531168.-3 rho

3.M311680-3 rho

3.531163c-3 rho

3.531169o.3 rho

3.5311680-S &ho

3.53116ge-3 rho

1.765584o-3 rho

1.765384o-3 rho

3.261000c-3 rho

3.62000003 rho

5.570238e-4 rho

2.147394e.4 rho

2.147394&-4 tho

1-924770c4 rho

2.699316c-4 rho

7.489974e-3 rho

130050000

130060000

130070000

130080000

130090000

130100000

130110000

130120000

135010000

140010000

145010000

145020000

145030000

145040000

145050000

150010000

0. 1

160010000

170010000

130010000

19010000

19020000

200010000

210010000

220010000

220020000

220O30000

220040000

20501607

20501602

20501609

20501610

20501611

20501612

20501613

20501614

20501615

20501616

20501617

2.427700O-3 rho

2.4277000-3 tho

3.102601.-3 rho

3.102601c-3 zho

4.355400.-3 rho

4.955400c-3 rho

4.955400e-3 dho

2.4277000-3 rho

2.690000c-3 rho

1.6200000-S rho

1.709792.-3 xho

330070000

330030000

330090000

33010000

330110000

330120000

330130000

330140000

340010000

340020000

350010000

20501300 tn4 5u 1.

20501301 0. 1.348962z-2 rho

20501302 1.335215e-2 rho

20501303 2.228100e-2 sho

20501304 1.763253.-2 rho

20501305 1.763253*-2 tho

20501306 2.728398e-3 rho

20501307 2.724909o-3 rho

20501308 3.065086-3 tho

20501309 3.065086o-3 tho

20501310 1.985241e-3 tho

20501311 2.690000e-3 rho

S

20501700 trr8 mm 1. 0. 1

20501701 0. 1.6355360-3 rho 360010000

20501702 1.943984o-3 rho 360020000

20501703 0.929000.-3 rho 36003M 00

20501704 1343984o-3 r&o 360040000

20501705 1384208.-3 1•o 360050000

20501706 2.861712a-3 rho 360060000

20501707 2.284800-3 rho 360070000

20501708 4.340000-3 rbo 370010000

20501709 1973408o-3 sho 380010000

20501710 178-4e-3 rho 390010000

20501711 2.728398e-3 tho 400010000

20501712 2.724909e-3 rho 410010000

20501713 3.065086-3 rho 420010000

20501714 3.06"86e-3 rho 420020000

20501715 1.92541e-3 rho 420030000

20501716 2.690000-3 rho 420040000

20501717 1.979000o-3 rbo 375010000

20501713 1.9780000-S rho 335010000 0

20501400 tn5 m 1. 0. 1

20501401 0. 1.213850c-3 sho 230010000

20501402 1.213850e-3 sho 230020000

20501403 2.427700.-3 tho 230030000

20501404 2.427700o-3 rho 230040000

20501405 2.427700a-3 tho 230050000

20501406 2.427700o-3 rho 230060000

20501407 2.427700e-3 sho 230070000

20501408 2.427700-3 rho 230080000

20501409 3.102601e-3 tho 230090000

20501410 3.102601e-3 rho 230100000

20501411 4.855400o-3 rho 230110000

20501412 4.355400e-3 rho 230120000

20501413 4M5400.-3 rho 230130000

20501414 2.427700c-3 rho 230140000

20501415 2.690000-3 rho 240010000

20501416 1.620000o-3 rho 240020000

20501417 1.709792.e-3 dho 250010000 S8

20501300 tm9 5= 1.

20501301 0. 1.213850e-3 rho

20501302 1.213850o-3 rho

205013O3 2.427700e-3 rho

20501804 2.4277000-3 rho

20501305 2.427700o.3 rho

20501306 2.427700.3 tho

20501307 2.427700o-3 rho

20501308 2.427700e-3 rho

20501809 3.102601.-3 rho

20501310 3.1026010-3 tho

20501311 4.3554000 rho

20501312 4.355400o-3 &ho

20501313 4.95540003 rho

20501314 14277000.3 rho

20501815 2.690000e-3 rho

20501316 1.6200000-3 rho

20501317 1.709792e-3 rho

0.1

430010000

430020000

430030000

430040000

43005000

430060000

430070000

430080000

430090000

430100000

430110000

430120000

430130000

430140000

440010000

440020000

450010000

0. 1

46010000

46020000

460030000

460040000

46050OOOO

460060000

460070000

470010000

430010000

490010000

475010000

485010000

20501500 tn6 su 1.

20501501 0. 1.63536c-3 rho

20501502 1.943984c.3 rho

20500103 0.9290000-3 rho

20501504 1943994c-3 sho

20501505 1.38420o--3 rho

205016 2.61712.3 rho

20501507 2.284800.3 rho

20501508 4.340000e-3 rho

20.501509 1978098e-3 rho

20501510 1.97309&a-3 rho

20501511 2.728398o-3 rho

20501512 2.724909.-3 rho

20501513 3.065086-3 rho

20501514 3.065086e.3 rho

20501515 1.92541e-3 rho

20501516 2.690000c-3 rho

20501517 1.9780000-3 rho

2050151 1.978000o.3 rho

20501600 tm7 am= 1.

20501601 0. 1.21350e-3 rho

20501602 1.213850•-3 rho

20501603 2.4277000-3 rho

20501604 2.4277000-3 rho

20501605 2.427700e-3 sro

20501606 2.427700*-3 rho

0. 1

260010000

260020000

260030000

260040000

260050000

260060000

260070000

270010000

280010000

290010000

300010000

310010000

320010000

320020000

320030000

320040000

275010000

285010000

0. 1

330010000

330020000

330030000

330040000

33005M000

330060000

20501900 ttl0 M 1.

20501901 0. 1.635536o-3 rho

20501902 1.943984o-3 rho

20501903 0.929000-3 zho

20501904 1.943984o-3 tho

20501905 1.394208-3 dro

20501906 2.361712o-3 Rho

20501907 2.284800e-3 dho

20501908 43400003 rho

20501909 1.9l78098-3 rho

20501910 1.978098*-3 rho

20501911 1.978098e-3 rho

20501912 1.978098g-3 rho *t

0toAd mana prrrnazy ad&

20502000 tmum.p

20502001 0. 1. cafr•h20502002 1. cafta

20502003 1. cztdvar

20502004 1. acdrlva

20502005 1. cnM=

20502006 1. cairlvar

20502007 1. artia

20502008 1. corrvar

20502009 1. cartrva

1.0. 1

010

011

012

013

014

015

016

017

018

137
20502010 1. aitlrv 019 *

bhoatafrr s.gI

20502100 &W

20502101 0. L

20502102 1.

20502103 L

20502104 1.

20502105 1.

20502106 1.

20502107 1.

20502108 L

20502109 1.

20502110 1.

205M02111 1.

20502112 1.

20502113 1.

20502114 1.

20502200 bbo

20502201 0. L

20502202 1.

20502203 1.

20502204 1.

20502205 1.

20"52206 1.

20502207 1.

20502"20 1.

20502209 1.

20502210 1.

20502211 1.

20502212 1.

20502213 1.

20502214 1.

* hcat mtwfatg.g3

20502300 btst3

20502301 0. 1.

20"502302 1.

20502303 1.

20502304 1.

20502305 1.

20502306 1.

20"502307 1.

20502302 1.

20502309 1.

20502310 1.

20502311 1.

20"502312 1.

20"50=13 L

20502314 1.

sum 1.0.1

q 230010000

q 230020000

q 230030000

q 230040000

q 230050000"

q 230060000

q 230070000

q 230080000

q 230090000

q 230100000

q 230110000

q 230120000

q 230130000

q 230140000

s-n LO.1

q 330010000

q 330020000

q 330030000

q 330040000

q 330050000

q 330060000

q 330070000

q 330080000

q 330090000

q 330100000

q 330110000

q 330120000

q 330130000

q 330140000

swn 1.0.1

q 430010000

q 430020000

q 430030000

q 430040000

q 430050000

q 430060000

q 430070000

q 430080000

q 430090000

q 430100000

q 430110000

q 430120000

q 430130000

q 430140000

20503102

20503103

20503104

20503105

20503106

20503107

*

0183960o03 dho

6183960o-3 rho

6.183960o-3 Aho

7.412000o.3 zho

3.415400o.-2 ho

1.166000o-2 rho

570020000

570030000

570040000

570050000

525010000

565010000

20503200 s x3 _ . 0. 1

20503201 0. 2.820000o-3 rho 600010000

20503202 &220000a.3 rho 600020000

205M3203 1.764000o-2 rho 600030000

20503204 1.764000*-2 rho 600040000

20503205 1.164000o.2 rho 600050000

20503206 1.164000.-2 rho 600060000

20503207 1.1640000-2 rho 600070000

20503202 1.164000o.2 rho 600080000

20503209 1.487592o-2 rho 600090000

20503210 2.296200a-2 rho 600100000

20503211 2.296200c-2 rho 600110000

20503212 7.775536.-3 dho 600120000

20503213 6.211000@-3 rho 610010000

20503214 1.370000.-1 rho 620010000

20503215 1.765453o-2 rho 630010000

20503216 1.937100c-2 rhdo 640010000

20503217 1.914300@-2 rho 660010000

20503212 7.08=000.-3 rho 605010000

20503300 t=4 sum L

20503301 0. 7.412000o-3 rho

20503302 6.193960o-3 rho

20503303 6.183960o.-3 rho

20503304 6.123960o.3 ro 20503305 7.412000c-3 rho

20503306 &028000o.-2 rho

20503307 1.166000e-2 rho s

0. 1

670010000

67002OOOO

670030000

670040000

670050000

625010000

665010000

20503400 brnS sum L 0. 1

20503401 0. 2.820000o-3 rho 700010000

20503402 &.20000o.-3 rho 700020000

20503403 1.764000.-2 rho 700030000

20503404 1.764000o-2 rho 700040000

20503405 1.164000s-2 rho 700050000

20503406 1.164000o-2 rho 700060000

20503407 1.164000o-2 rho 700070000

20503402 1.164000.-2 tho 700080000

20503409 1.487592o-2 rho 700090000

20503410 2.296200.,2 rho 700100000

20503411 2.296200.-2 rho 700110000

20503412 7.775536.3 rho 700120000

20503413 6.811000o-3 rho 710010000

20503414 1.370000o.-i rho 720010000

20503415 1.765453o.2 do 730010000

20503416 1.837100a.2 rh 740010000

20503417 1.914300o-2 rho 760010000

20503418 7.088000o-3 rho 705010000

* total man (scaiay side)

20503000 Mal su 1. 0. 1

20503001 0. &.820000o-3 rho 500010000

205O3OO2 U.2200000.3 rho 500020000

20503003 1.764000*-2 rho 500030000

20503004 1.764000*.2 rho 500040000

20503005 1.164000.-2 rho 500050000

20503006 1.164000.-2 rho 500060000

20503007 1.164000.-2 rho 500070000

20503002 1.1640000-2 rho 50008M000

20503009 1.487592.-2 rho 500090000

20503010 1296200.-2 rho 50100000

20503011 2296200o.2 rho 5WI10000

20503012 7.775536o.3 rho 500120000

20503013 6.211000o-3 zho 510010000

20503014 1370000s-1 rho 520010000

20503015 1.765453o-2 rho 530010000

205M3016 1.837100-2 rho 5M4001000

20503017 1314300c.2 rho 560010000

20503012 7.0880000.3 tho 505010000

20503100 sua mm2 1. 0. 1

20503101 0. 7.412000o-3 rho 570010000

20503500 tms6 sum 1.

20503501 0. 7.412000c-3 zho

20503502 6.183960o-3 zho

20503503 6.183960o-3 rho

20503504 6.183960*-3 rho

20503505 7.4120000-3 rho

20503506 3.415400o.-2 ho

20503507 1.1660000-2 rho

0. 1

770010000

770020000

77030000

770040000

7700W50000

725010000

765010000

* towal m ss eg

205M03600 tmsgl

20503601 0. L

20503602 1.

*total man as s&2

20503700 trsg2

20503701 0. 1.

20503702 1.

* total mmas as

sum 1. 0. 1

afmvar 030

arbtvr 031

sum 1.0.1

catlvar 032

ar'ifar 033

138
20503800 Uwg m 1. 0. 1

20503801 0. 1. aktvz 034

20503802 1. ctr 035 0

* mn~ beat t~fcr

20504000 Itz:eOl s 1. 0. 1

20504001 0. 0.1377136 bb= 010100100

20504002 0.1422227 hlbm- 010100200

20504003 0.19848M5 btu' 010100300

20504004 0.1526814 hbw 010100400

20504005 0.1526814 bM~r 010100500

20504006 0.1574145 hftw 010100600

20504007 0.2869075 hbm" 015100100

20504008 0.2869075 hfra 015100200

20504009 0.2869075 frm 015100300

20504010 02869075 hzr 015100400

20504011 0.2869075 hlm- 015100500

20504012 0.2869075 htmr 015100600

20504013 0.2869075 t 015100700

20504014 023605 ht= 015100800

20504015 0.2869075 htzra 015100900

20504016 0.26M5 bftw 015101000 0

205N4100

205N4101

20504102

205M4103

20504104

20504105

20504106

20504107

205•04108

205N4109

20504110

20504111

2054200

20504201

20504202

20504203

20504204

20504205

205W4206

2054207

2054208

20504209

20504210

20504211

20504212

20504213

20504214

20504215

20504300

20504301

20504302

20504303

20504304

20504305

20504307

20504307

20504308

20504309

20504310

20504311

20504312

20504313

20504314

20504315

20504316

20504317

20504319

20504319

lezc02 sm 1. 0. 1

0. 0.0142000 hhw 015200100

0.0142000 btxr 015300100

0.2318000 lm'r 100100100

0.9175587 hbnz" 100200100

9.948997e-2 kw 105100100

0.2380240 hbrb- 105100200

0.2380240 hr 105100300

0.2380240 hMw 105100400

0.2380240 hta" 105100500

0.2330240 btm- 105100600

0.2380240 hima- 105100700

htcz03 sm 1. 0. 1

0. 0.2380240 hfnw 105100800

9.948997.-2 htza 105100900

0.1260658 bbw 110100100

0.3595741 bum 110100200

0.2320757 ht= 110100300

0.2732092 hu 112100100

0.2732092 hfm 112100200

03698418 htrw 112100300

03698418 hum 112100400

0.2909746 bMr 112100500

0.2909746 hMr 112100600

0.2732092 bm 112100700

0.2732092 htm 112100800

5.1443582-2 btmr 125100100

5.lt3628e-2 bum 125100200

htcxc04 sm 1. 0. 1

0. 8.563881c-2 hum 130100100

L563881e-2 hbt 130100200

0.1712776 hum" 130100300

0.1712776 ht=m 130100400

0.1712776 hbt 130100500

0.1712776 humr 130100600

0.1712776 htu 130100700

0.1712776 htnm- 130100800

0.1712776 htmr 130100900

0.1712776 hkm= 130101000

$.563881e-2 htum 130101100

8.563881e-2 htmr 130101200

0.1787652 htm" 130101300

0.0122000 hbmr 135100100

9.168518-2 hrm 145100100

3.534574e-2 ku 145100200

3.534574c.2 kmw 145100300

3.168139c.2 bum 145100400

4.443029o-2 hf= 145100500

20504402

20504403

20504404

20504405

20504406

20504407

20504408

20504409

20504410

20504411

20504412

20504413

20504414

20504415

20504416

20504417

20504418

20504500

20504501

20504502

20504503

2050450

20504504 20504505

20504507

20504508

20504509

20504510

20504511

20504512

20504513

20504514

20504515

20504516

20504517

20504517 20504518

20504600

20504601

20504602

20504603

20504604

20504605 20504606

20504607

20"54608

20504609

20504610

20504611

20504612

20504613

20504614

20504615

20504616

20504617

20504618

20504702 20504703

20504700

20504701

20504706

20504707

20504708

205U4709

20504710

20504711

20504712

20504800

205047

20504807

20504809

0.3415037 bta' 150100200

0.4646039 Ikw' 150100300

0.5498793 hm'" 180100100

03771608 hbw 180100200

0.3771608 h•r 1U0100300

0.1636179 hum' 200100100

0.1634087 b 200100200

0.1938086 tum- 200100300

0.1338086 htnm 200100400

0.1190519 b 200100500

3233327.-2 hbtu 220100100

3.233327o-2 hum" 220100200

3.732212o-2 hbr 220200100

3.732212-2 bhmr 220200200

0.047700 htm 220300100

0.071000 hena 220400100

0.071000 h1ur 220400200

btcm:06 sum 1. 0. 1

0. 03148813 kim 230100100

03148818 htn 230100200

0.6297637 t 230100300

0.6297637 hMr 230100400

0.6297637 htnm 230100500

0.6297637 humr 230100600

0.6297637 hum 230100700

0.6297637 btmr 230100800

0.1048380 bfm' 230100900

0.2048380 hhm' 230101000

0.6297637 btm' 230101100

0.6297637 hfm 230101200

0.6297637 hm'- 230101300

0.6297637 hbm 230101400

0.6297637 t 230101500

0.6297637 kim 230101600

0314881S humt 230101700

03148818 him' 230101800

httzc07 sm 1. 0. 1

0. 03148818 htr- 230100101

03148818 htrm' 230100201

0.6297637 bbw 230100301

0.6W297637 hfm' 230100401

0.6297637 hum' 230100501

0.6297637 hfmr 230100601

0.6297637 btnr 230100701

0.6297637 hUir 230100801

0.3048380 htnm" 230100901

0.8048380 hftw 230101001

0.6297637 htrmr 230101101

0.6297637 k 230101201

0.6297637 humr 230101301

0.6297637 bth" 230101401

0.6297637 tum- 230101501

0.6297637 htm 230101601

03148818 bhm 230101701

0.3148818 htm' 230101801

lMe0 m n= 1. 0. 1

0. 3.794826*-2 ktm" 240100100

0.1388006 hUm" 240100200

0.13277225 hfm' 240100300

0.1578123 hum 240100400

0.1578123 bhn.' 240100500

0.1578123 hum' 240100600

0.1123697 bkm 240100700

0.2323132 hm 24010080

0.1154796 um'm 240100900

0.1078195 htmr 270100100

0.2682072 hftm 280100100

0.2682072 tmr 280100200

het•.09 s 1. 0. 1

0. 0.1636179 ltmr 300100100

0.1634087 bbn 300100200

0.1938086 hWm 300100300

20504400 hteixOS sum 1. 0. 1

20504401 0. 0.1O6140 hltw 150100100

139
20504810

20504811

20504812

20504813

20504814

20504815

20504816

20504817

20504812 S

20504900

20504901

20504.902

20504903

20504904

20504905

20504906

20504907

20504902

20504909

20504910

20504911

20504912

20504913

20504914

20504915

20504916

20504917

20504912

2505000

20505001

20505001

20505003

20505004

20505005

20505006

20505007

20505008

20505009

20505010

20505011

20505012

20505013

20505014

20505015

20505016

20505017

20505017

20505100 20505101

20505102

20505103

20505104

20505105

20505106

20505107

20505108

20505109

20505110

20505111

20505112

20505200

20505207

20505205

20505209

20505210

20505211

20505212

20505213

20505214

20505215

20505216

20505217

0.1833036 l•m 300100400

0.1190519 bidr 300100500

3.233327o-2 birw 320100100

3.233327o-2 bhw 320100200

3.732212o-2 htw 320200100

3.732212..2 hbzt 320200200

0.047700 htr 320300100

0.071000 hbw 320400100

0.071000 htmw 320400200

htez10 sum 1. 0. 

1

0. 0.3148313 hfm 330100100

0.3148818 hftr 330100200

0.6297637 hbm 330100300

0.6297637 lztnr 330100400

0.6297637 bb= 330100500

0.6297637 htm 330100600

0.6297637 htar 330100700

0.6297637 ht 330100300

0.3048380 b 330100900

0.8048380 * 330101000

0.6297637 bhnn" 330101100

0.6297637 htm 330101200

0.6297637 htm 330101300

0.6297637 t 330101400

0.6297637 1t 330101500

0.6297637 hbm 330101600

0.3148813 htnm 330101700

03149818 hfm 330101300

20505213 0.071000 htm 420400200

20505300

20505301

20505302

20505303

20505304

20505305

20505306

20505307

20505302

20505309

20505310

20505311

20505312

20505313

20505314

20505315

20505316

20505317

20505312

S505400

20505401

20505402

20505402

20505404

20505405

20505406

20505407

20505407

20505409

20505410

20505411

20505412

20505413

20505414

20505415

20505416

20505417

20505418

20505501

20505500

20505501

20505502

20505503

20505504

20505505

20505506

20505507

20505509

20505510

20505511

20505512 0

btczc14 mm 1. & 

1

0. 0.3148812 hbw 430100100

03148218 blm 430100200

0.6297637 bbm 430100300

0.629•637 hbb 430100400

0.6297637 hbm 430100500

0.6297"637 *b 430100600

0.6297637 h 430100700

0.6297637 * 430100800

0.8048380 hbm 430100900

0.9048380 htm 430101000

0.6297637 bbm 430101100

0.6297637 hm 430101200

0.6297637 bht 430101300

0.6297637 * 430101400

0.6297637 btm 430101500

0.6297637 btm 430101600

0.3148813 htmw 430101700

0.3148818 hfm 430101W00

bt~xl I m=

0. 0.3148213

03148213

0.6297637

0.6297637

0.6297637

0.6297637

0.6297637

0.6297637

0.8048390

0.3048330

0.6297637

0.6297637

0.6297637

0.6297637

0.6297637

0.6297637

0.3148212

03148812

1. 0. 1

hfm 330100101

1b 330100201

h= 330100301

hUm" 330100401

bbm 330100501

hUm 330100601

bZmr 330100701

htm 330100801

1z 330100901

htm 330101001

btm 330101101

bmr 330101201

hfm 330101301

hbm 330101401

hbm 330101501

htui 330101601

btm 330101701

hbt 330101801

0. 03148812

0.3148318

0.6297637

0.6297637

0.6297637

0.6297637

0.6297637

0.6297637

0.048380

O.8O48380

0.6297637

0.6297637

M6297637

0.6297637

0.6297637

0.6297637

03148813

0.3148818

1. 0. 1

htm 430100101

b~m 430100201

bbm 430100301

bt• 430100401

bbm 430100501

htmr 430100601

bhm 430100701

hmr 430100801

*tar 430100901

*ft 430101001

btm 430101101

htm 430101201

b 430101301

hfm 430101401

hbm 430101501

hbm 430101601

lt 430101701

htm 430101301

htez16 sum 1. 0. 

1

0. 2.794826*-2 htm 440100100

0.1388006 htm 440100200

0.13277252 bhm 440100300

0.157223 hfm 440100400

0.1578123 hbm 440100500

0.1578123 htmr 440100600

0.1123697 ht= 440100700

0.2323132 ht*r 440100800

0.1354796 bhm 440100900

0.1073195 bfUm 470100100

0.2682072 * 480100100

0.2682072 bhm 480100200

htbm12 mm 1. 0. 

1

0. &.794826o-2 hbb 340100100

0.1338006 hbmr 340100200

0.13277252 htm 340100300

0.1573123 htm 340100400

0.1573123 ht*r 340100500

0.157M123 htm 340100600

0.1123697 btrm 340100700

0.2323132 bm- 340100800

0.13547%• htw 340100900

0.1073195 hlm 370100100

0.2617192 bhm 330100100

0.2617198 * 3W0100200

btcz13 su= L 0. 

1

0. 0.1636179 hlm 400100100

0.1634087 hlm 400100200

0.1833086 bbm 400100300

0.1833086 b9m 400100400

0.1190519 hwm 400100500

3.233327o.2 htmr 420100100

3.233327.-2 hrmr 420100200

3.732212c.2 htm 420200100

3.732212A-2 h=m 420200200

0.047700 htnm 420300100

0.071000 htm 420400100

* ovcad atimsfluid-o4tnct

20505600 ulit sum L M. 1

20505601 0. 1. cutvuy 040

20505M02 1. aiv 041

20505M03 L altdvu 042

20505604 L cadtvr 043

20505605 L cnUlv 044

20505606 L auktvar 047

20505607 L cakhw 048

20505608 1. catk, 051

20505609 1. ccbvr 052

20505610 1. cnvar 055

*r fiztemolhesaau

20506000 puzc sum 1. 0. 

1

20506001 0. 0.1638026 htrm 020100101

20506002 2.094196o-2 htm 020100201

0 560 powe1 20506100 copowl mum 1. 0. 

1

140
20506101

20506102

20506103

20506104

20506105

20506106

20506107

20506108

20506109

20506110

20506111

20506112

205060

20506301

20506302

20506302

20506304

20506304

20506305

20506307

20506307

20506308

2050609

20506310

20506311

20506312

*

0. 0.5133959

0.5133959

1.0267920

1.0267920

1.0267920

1.0267920

1.0267920

' 1.0267920

1.0267920

1.0267920

0.5133959

0.5133959

klz 900000101

li'ur 900000201

him- 900000301

htnr 900000401

bN 90000501

kicr 900000601

htmr 900000701

hlmr 900000801

hmfr 900000901

kInr 900001001

him 900001101

hir 900001201

20507113

20507114

20507115

20507116

20507117

20507118

20507119

03000022 htr

0.2460181 MlNm

0.4430903 kzw

0.6028088 btlr

0.7204301 btr

0.4941412 hhur

0.4941412 hm

130101301

150100101

150100201

150100301

180100101

180100201

180100301

co.pow3 smn 1. 0. 1

0. 1.638498o-2 htm" 950000101

1.6384980-2 War 950000201

3.276996o-2 Ih= 950000301

3.276996o-2 hbmr 950000401

3.276996e-2 hWa 950000501

3.276996&2 hbm 950000601

3.276996"2 btu" 950000701

3M76996e-2 hmr 950000801

3.276996e-2 hlmr 950000901

3.276996e.2 h~r 950001001

1.638498-2 kmr 950001101

1.638498e-2 hmr 950001201

* ovaafl coe powe

20306400 copowt

20506401 0. 1.

20506402 1. a

mm 1. 0. 1

aOlvar 061

mtrvar 063

Suxzdloing at Pmpl ht

20506700 sbc.pul aur 1. 0. 1

20506701 0. 1. a2 260070000

20506702 -1. tmcpf 260070000

* whooa ing atpump2 inlet

20506800 sbcu2 a2un 1. 0. 1

20506801 0. 1. uin 360070000

20506802 -1. tempf 360070000

* subcooling atpump3 inlet

20506900 bc43 sum 1. 0. 1

20506901 0. 1. ss±Zex 460070000

20506902 -1. taupf 460070000

h et losses to amviromued

20507000 hIlrpvl msnu 1. 0. 1

20507001 0. 0.1998503 hbtrc 105100101

20507002 0.4757377 htno" 105100201

20507003 0.4757377 hrm 105100301

20507004 0.4757377 hbmr 105100401

20507005 0.4757377 htmr 105100501

20507006 0.4757377 hMr 105100601

20507007 0.4757377 htm 105100701

20507008 0.4757377 hrm 105100801

20507009 0.1988503 k 105100901

20507o10 0.1492885 Umr 110100101

20507011 0.4258115 htrr 110100201

20507012 0.2748266 htmr 110100301

Sbedlosses v

20507100 ht.-pv2 sum 1. 0. 1

20507101 0. 0.1437279 tmr 130100101

20507102 0.1437279 h•m 130100201

20507103 0.2874557 hlm- 130100301

20507104 0.2874557 hMa 130100401

20507105 0.2874557 hfmz 130100501

20507106 0.74557 bhw 130100601

20507107 0.2874557 hmr 130100701

20507108 0.2874557 htm" 130100801

20507109 0.2874557 htrn 130100901

20507110 0.2874557 htIn- 130101001

20507111 0.1437279 htm 130101101

20507112 0.1437279 blr 130101201

4 Vesse heat losses

20507200 hlrpvt min 1. 0. 1

20507201 0. 1.0 cadvm- 070

20507202 1.0 afrl'var 071

20507203 1.0 aiUtvar 073

* bypass hed lames

20507300 up.dchl z 1. 0. 1

20507301 0. 0.125 ieur 145100101

20507302 0.048 bhm 145100201

20507303 0.048 hm 145100301

20507304 0.043 hUm" 145100401

20507305 0.061 hhn 145100501

* hIs beat losses

20507400 hlholeg a= 1. 0. 1

20507401 0. 0.2136486 hfm 200100101

20507402 0.2183690 htmr 200100201

20507403 0.2456301 hbm 200100301

20507404 0.2456301 hbm 200100401

20507405 0.1590934 h•m 200100501

20507406 0.2186486 hft 300100101

20507407 0.2183690 hma" 300100201

20507408 0.2456301 hm" 300100301

20507409 0.2456301 bhm" 300100401

20507410 0.1590934 hbtnu 300100501

20507411 0.2196486 htm 400100101

20507412 0.2183690 hbtt 400100201

20507413 0.2456301 knr 400100301

20507414 0.2456301 bta" 400100401

20507415 0.1590934 hrm- 400100501

a loop scall&2 heat losses

20507500 hWlosel2 sum 1. 0. 1

20507501 0. 0.1079690 bhm 240100101

20507502 0.1703975 im 240100201

20507503 0.1629972 hUm 240100301

20507504 0.1937370 khm 240100401

20507505 0.1937370 hum 240100501

20507506 0.1937370 ktmr 240100601

20507507 0.1379499 htmr 240100701

20507508 0.2851976 bhm 240100801

20507509 0.2277027 btm 240100901

20507510 0.1079690 mr 340100101

20507511 0.1703975 htw 340100201

20507512 0.1629972 hhw 340100301

20507513 0.1937370 b•m 340100401

20507514 0.1937370 htrm 340100501

20507515 0.1937370 htmr 340100601

20507516 0.1379499 hirm 340100701

20507517 0.2851976 htm 340100801

20507518 0.2277027 htm 340100901

*loop sea.l bead losses

20507600 bllos2 sum 1. 0. 1

20507601 0. 0.1079690 htm 440100101

20507602 0.1703975 hfm 440100201

20507603 0.1629972 htm 440100301

20507604 0.1937370 htn 440100401

20507605 0.1937370 htm 440100501

20507606 0.1937370 hnrom 440100601

20507607 0.1379499 Mw 440100701

20507608 0.2851976 hlrm 440100801

20507609 0.2277027 bum 440100901 0

* avend loop meal he losses

20507700 hfosea sum 1. 0. 1

20507701 0. 1.0 aidvar 075

141
20507702 1.0 azdvw' 076

• pumps heat losses

20507800 hbspump ms 1. 0. 1

20507801 0. 0.2711823 bftw 270100101

2050702 0.2711223 hm 370100101

20507803 0.2711223 hew 470100101 a

* cis bed losses

20507900 hlcoleg am 1. 0. 1

20507901 0. 0.3319496 t 280100101

20507902 03319496 12km 280100201

20507903 03238223 btar 380100101

20507904 03238222 hm" 380100201

20507905 0331496 htmr 480100101

20507906 0.3319496 btar 480100201 S

• sgl s heat lowa

20502000 bhgl mua 1. 0. 1

20508001 0. 03518594 lirw 500100101

2050M002 0.3512584 Mamr 500100201

20508003 0.7037167 htm 500100301

20508004 0.7037167 bbw 500100401

20508005 0.7037167 k 500100501

20508006 0.7037167 ftmr 500100601

2050807 0.7037167 htnw 500100701

20508008 0.7037167 12k 500100801

20502009 0.2993500 lhm 500100901

20502010 0.2194722 1t2k" 500101001

20502011 0M8194722 htrm 500101101

20508012 0.7719773 htmr 500101201

20508013 "030325 1km" 520100101

* sgi inheat losses

20508100 hlsglus um 1. 0. 1

20502101 0. 0.6702337 h2=r 530100101

20508102 0.6974336 bM 530100201

20508103 0,7267252 1= 530100301

20508104 0.6705372 h= 570100101

20502105 0.6705373 22km 570100201

20508106 0.6705372 12w 570100301

20502107 0.6705378 bikm 570100401

20502102 0.6705378 12km 570100501

• sg2 ss het lossa

20508200 blsg2sa m 1. 0. 1

20502201 0. 03518524 b= 600100101

20502202 0351•3•4 1hkr 600100201

20508203 0.7037167 h= 600100301

20502204 0.7037167 hkmr 600100401

20508205 0.7037167 1kmtr 600100501

20508206 0.7037167 1kmr 600100601

20502207 0.7037167 htmr 600100701

20509201 0.7037167 irrm 600100801

2052209 0.2 500 hkw 600100901

20502210 0.8194782 bim 600101001

20508211 0.8194782 2tkm" 600101101

20502212 0.7719773 bumr 600101201

20508213 2.5030325 t2mr 620100101

g a heal losses

20503300 b sum 1. 0. 1

20503301 0. 0.6702337 12k 630100101

20502302 0.6974336 hrm 630100201

20508303 0.7267253 htm" 630100301

20508304 0.6705378 hrm 670100101

20508305 0.6705373 hum 670100201

20508306 0.6703378 12km 670100301

20508307 0.6705372 hum 670100401

20508302 0.6705373 hlaw 670100501

*sS3 ss heat losses

20508400 hlsguss sm 1. 0. 1

20508401 0. 0.351594 htm 700100101

20503402 0.3512514 hbim 700100201

20508403 0.7037167 hum 700100301

20509404

20509405

20509406

20509407

20503403

20508409

20509410

20509411

20508412

20503413

S

0.7037167

0.7037167

0.7037167

0.7037167

0.7037167

O.2993500

0.8194782

0.8194782

0.7719773

2.5030325

12kr

bum 12m"

baw"

btmr

bun"

bhw"

bgmr

700100401

700100501

700100601

700100701

700100801

700100901

700101001

700101101

700101201

720100101

0 sg3 us heat losses

20508500 hIsesi sum L 0. 1

20502501 0. 0.6702337 bikm 730100101

20509502 0.6974336 12mr 730100201

20508503 0.7267252 htmr 730100301

20509504 0.6705372 12mr 770100101

20508505 0.6705378 hftw 770100201

205089506 0.6705372 1tmir 770100301

20509507 0.6705373 taw 770100401

20508503 0.6705378 12k 770100501 0

* overall 1s heat losses

20509000 h su mm 1. 0. 1

20509001 0. 1.0 acnvyz 072

20509002 1.0 catrlvar 074

20509003 1.0 cavub 077

20509004 1.0 mfrlvar 078

20509005 1.0 c1vm 079 0

* loop M2&3 s au hea losses

20509100 hlspd mw 1. 0. 1

20509101 0. 1.0 caulvwa 080

20509102 1.0 =Iv= 081

20509103 1.0 atzlvar 082

20509104 1.0 c1var 083

20509105 1.0 acblv 024

20509106 1.0 cafrlvar 035 0

0 Vl pstctal dp

20510000 sgldpt sum 20510001 0. 1.0 p

20510002 -1.0 p

• 3g2 ps total

20510100 sg2dpt sum

20510101 0. 1.0 p

20510102 -1.0 p

0 g3 ps toWadp

20510200 sg3dpt

20510201 0. 1.0

20510202 -1.0

p

P

* loopl totaldp

20510300 Ildpt sum

20510301 0. 1.0 p

20510302 -1.0 p

loop2 toWal

20510400 l2p sum

20510401 0. 1.0 p

20510402 -1.0 p

looq3 total dp

205105W00 13dp1 sum

20510501 0. 1.0 p

20510502 -1.0 p

looplh 4Id

20510600 ll1l1 mm

20510601 0. 1.0 p

20510602 -1.0 p

1. 0. 1

220040000

240010000

1. 0. 1

320040000

340010000

1. 0. 1

420040000

440010000

1. 0. 1

290010000

200010000

1. 0. I

390010000

300010000

1. 0. 1

490010000

400010000

1. 0. 1

200010000

2200400OO

* loopl oop seadewleg dp

20510700 lllsddp sum 1. 0. 1

142
20510701 0. 1.0 p 240010000

20510702 -1.0 p 260050000 S

* loopl loop zed ascleg dp

20510800 Ulhadp v= 1. 0. 

1

20510801 0. 1.0 p 260050000

20510802 -1.0 p 260070000 a

20515002

20515003

20515004

20515005

20515006

20515007

20515008

20515009

20515010

20515011

20515012

.183

366

366

366

366 .366

.366

.183

.183

VOW 130020000

VoiWf 130030000"

voWdf 130040000

voW 130050000

Vdff 130060000

voidf 130070000

voWd 130080000

vodf 130090000

voidr 130100000

voWf 130110000

Vokdi 130120000

loopl UMp dp

20510900 llpudp

20510901 0. 1.0

20510902 -1.0 4

pp

1. 0. 1

260070000

280010000

*Ioop ci

20511000

20511001

20511002 a

dj,

11C14 Vm

0. 1.0 

p

-1.0 p

1. 0. 1

280010000

290010000

rpvdcl d40O1

20511100 spvdcl 

a 20511101 0. 1.0

20511102 -1.0

* rpvdc2 4p02

20511200 pvdc2

20511201 0. 1.0

20511202 -1.0

:rpv dclp dp003

20511300 zpd 

a

20511301 0. 1.0

20511302 -1.0

* tpv car inlet d4O05

20511400 min 

a 20511401 0. 1.0

20511402 -1.0

rpv core bot dpOI

20511500 rpvcobo

20511501 0. 1.0

20511502 -1.0

* rpvt colled level

20515100 xpvfvl 

- 1. 0. 

1

20515101 0. .798 voidf 100010000

20515102 .753 voW 110010000

20515103 .486 VOW 120010000

20515104 .382 vo" 140010000

20515105 .382 ofW 150010000

20515106 .688 woWf 160010000

20515107 .936 voidf 170010000

20515108 .936 voidf 130010000

20515109 .642 voidf 190010000

20515110 .642 Vo"df 190020000

20515111 1. cahva ISO

p

Umpppp

urnpppp

1. 0. 1

115070000

115040000

1. 0. 1

115040000

105010000

1. 0. 1

105010000

120010000

1. 0. I

120010000

130020000

1. 0. 1

130020000

130050000

rpvcormiddledp0l2

20511600 rpvme sum

20511601 0. 1.0 

p

20511602 -1.0 

p

*pv coretop dp013

20511700 apvooto

20511701 0. 1.0

20511702 -1.0 S

1. 0. 1

130050000

130080000

1. 0. 1

130080000

140010000

.npp

* camc outlet -upper plem dpO415

20511800 qnvaoup mn 1. 0. 

1

20511801 0. 1.0 p 140010000

20511802 -1.0 p 160010000 0

* sgl a riser lower part dplOl1

20512100 sglrilo mm 1. 0. 

1

20512101 0. 1.0 p 50010000

20512102 -1.0 p 500040000

*sgl usrisefr upp," part plO2s

20512200 glrdup mum 1. 0. 

1

20512201 0. 1.0 p 500040000

20512202 -1.0 p 500110000

Sasgl asriserto dome dplO3s + dplO4s

20512300 sglrmp mmi 1. 0. 

1

20512301 0. 1.0 p 500110000

20512302 -1.0 p 520010000

* cmre level

20515000 corM sum 1. 0. 

1

20515001 0. .183 voidf 130010000

143

NRC FORM 335 UAL NUCLEAR REGULATORY COMMISSION 1. REPORT NLUMER

(24M) PAmigP by NRC. Add VOL. S"w.. Rev. NRCM 110, OW Addendum Nmnbes, If' any.

MM, 3 BIBUOGRAPHIC DATA SHEET

(See h:•s..ceo•s one miUW)

2. rIT A sue"".' NUREG/IA-0154

RELAPSMOD3.2 Post Test Analysis and Accuracy Quantificaton of

SPES Test SP-SB-03 3. DATE REPORT PUBUSHED

MOT YEAR

February 1999

4. FIN OR GRANT NUMBER

D6227

5. AUTHOR(S) 6. TYPE OF REPORT

F.D'Auria, M. Froghen", W. Glannotli Technical

7. PERIOD COVERED pncAwu Daw)

6. PERFORMING ORGANIZATION - NAME AND ADDRESS NRCw, pwide Divwasx O•ce aRegor4 U.S. mx wR~p*'fty ca72m aw m&lVi adisa; iCW*=kr

p'ovke wnae Wnd mafn addess.)

University of Pisa *Univertty of Genova

Via DictisaM 2-56100 DITEC

Pisa, Italy Via all'Opera Pia 15a

16143 Genova, Italy

9. SPONSORING ORGANIZATION- NANE AND ADDRESS gmr, be Same as abowv, Icw'kra pmvde • M•C Dwax O r Ofaearftim U.S. a•egy CarnmissbM

o*nd s11nulg ad*-s.)

Office of Nudear Regulatory Research

U.S. Nuclear Regulatory Commission

Washington, DC 20555-0001

10. SUPPLEMENTARY NOTES

11. ABSTRACT r" wads r is)

The present document deals with the RELAP5/MOD3.2 analysis of the small break LOCA experiment SP-SB-03 performed in

SPES facaity. SPES is a PWR simulator (Integral Test Facility) installed at SIET center in Piacenza (IT). Volume scaling and core

power scaling factors are 1/427, with respect to the Westinghouse 900 MWe standard reactor. The experiment is originated by a

small break in the cold leg (2" equivalent break area in the plant) without the actuation of the high pressure injection system.

Low pressure injection system actuation occurs after core dry-out The RELAP5 code has been extensively used at University of

Pisa; the nodalztlion of SPES facility has been qualified through the application of the version RELAP5IMOD2 to the same

experiment and another testperformed in the same facility. Sensitivity analyses have been addressed to the influence of several

parameters (Ike discharge break coefficient, time of accumulators start, etc.) upon the predicted transient evolution. Qualitative

and quantitative code calculation accuracy evaluation has been performed.

12. KEY WORDSIDESCRIPTORS aUsk wads arhaes eat wiufsiWmeach inutbg te mpao,) 13. AVAJLABLIJY S"ATEMErr

RELAP5/MOD3.2 unlimited

LOCA 14. SE•URIY O..ASF.rnATIoN

PWR (Wh Pow)

unclassified

(11 Repav

unclassified

15. NUMBER OF PAGES

16. PRICE

NRC FORM 335 (24M)
Federal Recycling Program

UNITED STATES

NUCLEAR REGULATORY COMMISSION

WASHINGTON, DC 20555-0001

OFFICIAL BUSINESS

PENALTY FOR PRIVATE USE, $300

SPECIAL STANDARD MAIL

POSTAGE AND FEES PAID

USNRC

PERMIT NO. G-67

0