NUREG/IA-0033

International

Agreement Report

Assessment of RELAP5/MOD2,

Cycle 36.04 Against LOFT

Small Break Experiment L3-6

Prepared by

John Eriksson

Swedish Nuclear Power Inspectorate

S-102 52 Stockholm, Sweden

Office of Nuclear Regulatory Research

U.S. Nuclear Regulatory Commission

Washington, DC 20555

July 1990

Prepared as part of

The Agreement on Research Participation and Technical Exchange

under the International Thermal-Hydraulic Code Assessment

and Application Program (ICAP)

Published by

U.S. Nuclear Regulatory Commission
NOTICE

This report was prepared under an international cooperative

agreement for the exchange of technical information. Neither

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

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

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

use, or the results of such use, of any information, apparatus product or process disclosed in this report, or represents that its use

by such third party Would not infringe privately owned rights.

Available from

Superintendent of Documents

U.S. Government Printing Office

P.O. Box 37082

Washington, D.C. 20013-7082

and

National Technical Information Service

Springfield, VA 22161
NUREG/IA-0033

International

Agreement Report

Assessment of RELAP5/MOD2,

Cycle 36.04 Against LOFT

Small Break Experiment L3-6

Prepared by

John Eriksson

Swedish Nuclear Power Inspectorate

S-102 52 Stockholm, Sweden

Office of Nuclear Regulatory Research

U.S. Nuclear Regulatory Commission

Washington, DC 20555

July 1990

Prepared as part of

The Agreement on Research Participation and Technical Exchange

under the International Thermal-Hydraulic Code Assessment

and Application Program (ICAP)

Published by

U.S. Nuclear Regulatory Commission
NOTICE

This report documents work performed Under the sponsorship of the SKI/STUDSVIK

of Sweden. The information in this report has been provided to the USNRC

under the terms of an information exchange agreement between the United States

and Sweden (Technical Exchange and Cooperation Arrangement Between the United

States Nuclear Regulatory Commission and the Swedish Nuclear Power

Inspectorate and Studsvik Enerigiteknik AB of Sweden in the field of reactor

safety research and development, February 1985). Sweden has consented to the

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

the widest possible circulation among the reactor safety community. Neither

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

employees, makes any warranty, expressed or implied, or assumes any legal

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

use, or any information, apparatus, product or process disclosed in this

report, or represents that its use by such third party would not infringe

privately owned rights.
STUDSVIK ENERGITEKNIK AB STUDSVIK/NP-87/128

1987-11-03

John Eriksson

ICAP

ASSESSMENT OF RELAP5/MOD2, CYCLE 36.04,

AGAINST LOFT SMALL BREAK EXPERIMENT L3-6

ABSTRACT

The LOFT small break experiment L3-6 has been

analyzed as part of Sweden's contribution to the

International Thermal-Hydraulic Code Assessment

and Applications Program (ICAP).

Three calculations, of which two were sensitivity

studies, were carried out. The following quantities were varied:

the content of secondary side fluid and

the feed water valve closure

the two-phase characteristics of the

main pumps

All three predictions agreed reasonably well

with most of the measured data. The sensitivity

calculations resulted only in marginal improvements.

The predicted and measured data are compared on

plots and their differences are quantified over

intervals in real time.

Approved by97

STUDSVIK ENERGITEKNIX AB STUDSVIK/NP-87/128

1987-11-03

LIST OF CONTENTS

Page

1 INTRODUCTION 1

2 FACILITY AND TEST DESCRIPTION 3

2.1 Test Facility 3

2.2 The Experiment 4

2.3 Assessment Parameters 5

2.4 Measurement Uncertainty 5

2.5 Experimental Data Preparation 6

3 CODE AND MODEL DESCRIPTION 7

3.1 Code Features 7

3.2 Input Model 7

3.2.1 Initial system

pressure 8

3.2.2 Primary fluid temperatures 9

3.2.3 Core flow bypass 9

3.2.4 Environmental heat

losses 10

3.2.5 Break discharge

coefficient 10

3.2.6 Pump model 11

3.2.7 Steam generator 11

4 THE BASE CASE CALCULATION 13

5 SENSITIVITY RESULTS AND DISCUSSION 17

5.1 Case B 17

5.2 Case C 18

6 RUN STATISTICS 20

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7 CONCLUSIONS

REFERENCES

TABLES

FIGURES

APPENDICES

A Input Listings

B Data Comparison Plots

C Calculation of Data Uncertainties

D Description of the Accompanying Data'

Package

21

23

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1 INTRODUCTION

An International Thermal-Hydraulic Code Assessment and Applications Program (ICAP) is at

present being conducted by several countries

under the auspices of the USNRC (Ref 1). The

goal of the program is to make quantitative

statements regarding the prediction capabilities

of current best-estimate thermal-hydraulic

computer codes. Such codes have been used for

many years as state-of-the-art instruments to

study and verify numerical and correlative

computational models with experimental results.

Some of these codes have reached a high degree

of sophistication. They include models for all

processes which are essential to thermalhydraulic scenarios in the nuclear power reactor

application. So far, however, these codes have

not achieved status as reactor licensing tools,

i.e. they do not fulfil the Appendix K rules

(Ref 2), although they are often applied to other

calculations. The present ICAP aims to quantify

uncertainties in the codes so that the codes may

be used for licensing purposes.

Sweden's contributions to ICAP encompass assessment calculations using the two thermal-hydraulic

codes TRAC-PFl/MODl (Ref 3) and RELAP5/MOD2

(Ref 4). The work is conducted by Studsvik

Energiteknik AB and is sponsored by the Swedish

Nuclear Power Inspectorate.

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A brief description of the LOFT test facility

and the L3-6 experiment is given in Chapter 2.

In Chapter 3 the model and procedures used in

the calculations are discussed. The base case

and sensitivity predictions are discussed and

compared in Chapters 4 and 5 and in the plots,

Appendix B. The run statistics is presented in

Chapter 6 and Appendix C. Chapter 7 gives some

conclusions from the code assessment. The input

listings of the calculations are collected in

Appendix A.

A data package on tape containing input files

and predicted data has been produced. The content

is described in Appendix D. A copy of this tape

is submitted to USNRC as a part of the ICAP

agreement.

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2 FACILITY AND TEST DESCRIPTION

The LOFT-experiment series L3 was intended to

provide large-scale blowdown system data for PWR

small break transients. To the Swedish ICAP

contribution two experiments of the L3 series

were assigned. In the experiment LOFT L3-5,

treated earlier in Ref 15, the main circulation

pumps were stopped shortly after the break had

been opened. In the experiment, LOFT L3-6,

treated in this report, the pumps were allowed

to operate at normal speed throughout the test

in order to provide data for analyzing the

differences in the two-phase scenarios between

the two tests. Apart from the difference in pump

operational mode the two experiments were nominally identical.

This chapter shall briefly describe the test

facility, the L3-6 experiment, the assessment

parameters used and some aspects of the measurement uncertainties.

2.1 Test Facility

The objective of the LOFT experiments was to

demonstrate thermal-hydraulic phenomena which

might occur in commercial PWR systems during

abnormal situations. The facility is capable of

performing a variety of operational transients

and LOCAs. Brief descriptions of LOFT are given

in a number of experiment reports such as Ref 5.

The most thorough description is provided by

Reeder (Ref 6). Only particular design features

and characteristics relevant to the L3-6 experiment will be discussed in the following sections.

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A general view of LOFT is shown in Figure 1. In

the L3-6 small break experiment the two isolation

valves on the broken loop legs were closed so as

to prevent the passage of fluid via the header

to the suppression vessel.

The break was simulated by a 205.9 mm2 orifice

in a T-branch line from the intact loop cold leg

near the reactor vessel. The aim of the break

configuration was to simulate an equally placed

4-in diameter small break on a four-loop

1000 MW(e) PWR.

During the L3-6 experiment the only primary

coolant injection was carried out by the HPIS

into the reactor vessel downcomer. The experiment was terminated before the LPIS pressure set

point was reached.

2.2 The Experiment

After approximately 99 h of nuclear heating the

initial conditions listed in Table 1 were obtained. The sequence of events which occurred

during this experiment is listed in Table 2.

Main imposed actions during the experiment were:

a. At the time of reactor scram (which for

safety reasons had to be verified before the break) the steam generator

feed water and steam line valves started to close.

b. LOCA initiated 5.8 s after the scram.

c. The HPIS injection started at 13.2 MPa.

d. The steam generator auxiliary feed was

initiated and terminated manually.

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2.3 Assessment Parameters

The selection of the appropriate assessment parameters for the LOFT L3-6 experiment, Table 3,

followed the recommendations of the ICAP Guidelines (Ref 1). The selection was made during the

input preparation since a number of expanded

Edit/Plot variables from RELAP5/MOD2 calculations are not available from the restart file

but must be collected as control variables.

In some cases liquid level data are compared as

pressure differences. For the upper plenum and

downcomer levels only bubble plot data shown in

Ref 5 were available. These plots were converted

into slightly smoothed elevation histories. Due

to ambiguous plot'data the resulting level behaviour is rather uncertain (Plots B.15 and B.16).

The early break flow was not qualified by the

experiment until 50 s after the break, and showed

rather large errors during the remainder of the

transient. Predictions of mass inventory obtained

through flow integration were therefore not

carried out. For the energy balance, the steam

generator heat transfer was not known, and could

not be estimated by the steam produced.

2.4 Measurement Uncertainty

The experiment instrumentation involves a variety

of transducers which may have different accuracies for the same kinds of quantities (Refs 5, 6).

Table 4 is a summary of the accuracies of the

measured quantities.

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2.5 Experimental Data Preparation

The preparation of the experimental data for

plotting and uncertainty analysis required

several steps of manipulation of the information. First of all, the data were copied from

the original blocked tape files to the CDC

standard display code.

A program, LOFTDEC, was developed to sort out

the keyword and channel information to be used

in the assessment work. The program also decimated the channel data by averaging over time

intervals so that information was copied to an

intermediate channel information file only every

2nd second up to 200 s after the break, and then

every 5th second.

A program, R5SILFT, was developed to select data

for desired channels from the intermediate data

file. These data were transformed into a new

file with the same format as a RELAP5 restart

file. Experimental and predicted data could later

on be similarly used in plotting and assessment.

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3 CODE AND MODEL DESCRIPTION

The assessment calculations with RELAP5/MOD2 for

the LOFT L3-6 experiment were carried out using

the cycle 36.04 code version. The code was implemented in June 1986 on a CDC 170-810 computer.

The calculational model was based on available

LOFT input files and listings, among those the

L3-5 input (Ref 15). A number of geometrical

model features were introduced as a result of

findings in the L3-6 experiment.

3.1 Code Features

The descriptive document available for the

RELAP5/MOD2 code is a rather detailed code manual

(Ref 4). The main characteristics of the code

are summarised in Table 5. A new feature of

RELAP5/MOD2 is the cross junction which, according to code manual recommendations, was applied

at the steam separator upstream volume and at

the hot leg and cold leg vessel junctions.

3.2 Input Model

The preparation of the LOFT L3-6 input proceeded

from an input of the closely similar L3-5 experiment which had earlier been assessed for ICAP

(Ref 15). In its turn this input had been set up

from a LOFT fast transient input and with additional updates from other available input listings

(Refs 7, 8, 9).

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Changes introduced for the L3-6 calculations,

compared with those of the L3-5 case, include

new initial conditions, other trip times and a

continuous operation of the main recirculation

pumps. However, some changes in the calculation

model are due to experiences gained during the

L3-5 assessment. Reasons for particular approaches

used in the calculation model are presented below.

Figure 2 shows the nodalization used. The input

files are given in Appendix A.

3.2.1 Initialsystempressure

To avoid an explicit steady-state pressurizer

pressure and level control, the surge line

junction was modeled as a trip valve which was

closed until scram. The pressurizer initial

conditions were satisfied with the correct fluid

content and saturated water. Pressurizer heat

structures were modeled with the outer surface

at saturation temperature until scram and then

at room temperature.

A time dependent volume was connected to the

pressurizer surge line by a trip valve adjacent

to the pressurizer bottom in order to maintain

the initial primary pressure constant during the

steady state calculation. During steady state

the pressurizer was isolated from the surge line.

The pressure of the time dependent volume was

equal that of the pressurizer bottom volume. At

scram the trip valve closed at the same time as

the pressurizer isolation ceased.

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3.2.2 Primary fluid temperatures

The measured temperatures of the coolant circulating through the core and the steam generator

show considerable variations from the standpoint

of heat balance. This is particularly the case

in the vessel downstream of the core. The same

situation was also noticed during the L3-5

assessment (Ref 5). However, the L3-6 measurements of 577.1 K in the hot leg and 557.9 K in

the cold leg fulfil the conservation of energy

and are consequently accepted for the steady

state. In the calculation the primary fluid

temperatures are controlled through the steam

generator operation and feed water temperature,

see Section 3.2.7.

3.2.3 Core flow bvass

Several core bypass flows exist. Two of these

(Ref 7) were modelled by servo valves adjusted

for the correct flows until scram:

the inlet annulus to upper plenum with

6.6 % o± primary loop flow

the lower plenum to upper plenum with

3.6 % of primary loop flow

the reflood assist bypass valve leakage with 1.3 % of primary loop flows.

The leakage from the vessel cold leg inlet annulus to the upper plenum is caused by a flow path

in the narrow gap between the filler blocks and

the vessel wall. This leakage has a vertical

extension equal to the cold leg nozzle diameter.

To achieve a more realistic description in the

case of stratification the leakage has been divided into two flow path junctions. One low path

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connects the volumes below the inlet and outlet

at their upper ends, junction 297 in Figure 2.

Similarly, the higher level volumes are connected

at their bottom ends by a second junction,

junction 296. This second leakage junction will

preferrably bypass steam in the case of void

thus promoting a reduced leakage pressure difference.

3.2.4 Environmental heat losses

The exchange of heat with structure material is

important in small break analysis. Since the

initial input had only restricted material included, structures had to be added to the input.

The bulk structures of the facility were modeled

to represent the correct structural masses.

RELAP5/MOD2 does not facilitate an exterior

surface heat transfer control during calculation. An environmental heat transfer coefficient had to be found by test calculations to

obtain approximately the total heat loss of

250 kW as found in the experiment (Ref 7).

3.2.5 Break discharge coefficient

Test calculations show a too rapid decrease in

the pressurizer inventory when the default subcooled discharge coetZicient of unity was used.

Applying a coefficient o± .85 the rates of emptying the pressurizer and of the early system.

depressurization turned out close to the experimental values. The assumption that the pressurizer emptying rate is an indicator of the break

discharge flow is only applicable for a low flow

pressure drop in the surge line as it occurs in

small break experiments. The pressurizer level

during the emptying period is shown on Plot B.54.

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3.2.6 Pum2 model

The main circulation pumps were allowed to run

at the constant initial speed during the L3-6

transient. The pump characteristics applied in

the previous L3-5 calculation, which originated

from an early LOFT base input (Ref 16), were

also applied in the first two calculations,

whereas modified two-phase characteristics were

applied in the last calculation, Case C.

3.2.7 Steam generator

A RELAP5/MOD2 separator component is contained

in the steam generator, see Figure 2 volume 520.

The vapor outlet space above that volume is

divided into two parallel and vertical volumes

according to the recommendations of the code

manual (Ref 4). Of these the one with the larger

cross section area, volume 525, receives the

steam from the separator component. This volume

is connected by a cross-junction to the parallel

volume 526, which has a smaller cross section

area and which formally represents the downcomer

top.

The steam generator initial conditions were

established by using auxiliary components for

the control of

- dome pressure

- downcomer water level

- rate of feedwater and steam mass flows

- recirculation ratio

- feedwater internal energy.

The dome pressure was controlled by a time dependent volume at the correct pressure and connected by an open junction to the steam dome. The

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downcomer level was regulated by the direction

and flow rate through a time dependent junction

connecting a time dependent volume with saturated water.

The initial feedwater mass flow rate, 27.8 kg/s,

was obtained by using a time dependent junction.

Moreover, the internal energy of the fluid in

the time dependent volume, which delivers the

feed water, was regulated by the steam flow

generation rate which in its turn must be equal

to the feedwater flow rate.

The initial main steam mass flow rate being

equal to the feedwater mass flow rate is controlled by a time dependent junction. The flow

rate during the valve closure, which starts at

scram, is obtained from the valve characteristics (Ref 6) and a valve stem closure rate

of 5 % per second. The reason for using this

model is the simplicity by which the closed

valve leakage can be calculated. Condie et al

(Ref 7) estimated this leakage to be .120 kg/s

at 4.5 MPa in the L3-6 experiment. At other

pressures a linear dependence is assumed.

Uninitionally the steam valve partly let steam

through from 89 s to 99 s after the break. The

flow rate during this time interval was assumed

to be correct by adjusting the steam lift so

that a pressure drop rate close to the measured

one (see Plot B.51) was found. The steam mass

flow was during these 10 seconds only a few per

cent of that for a fully opened valve.

The junction 516, Figure 2, at the bottom of the

downcomer is modelled as a regulated valve to

achieve an initial recirculation ratio of 4.7.

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4 THE BASE CASE CALCULATION

The base case (Case A) calculation could be carried without any urgent code problems. Thus a

very limited computation mass error, Plot B.62,

was saved up by the code. Still, however, the

computation CPU time required was very extensive, Plot B.61, as a consequence of time step

transport limit caused by the continuous main

pump operation. Thus one separate calculation

consumed about 18 h CPU time .on a Cyber 170-810.

The system heat balance was initially dominated

by the reactor power, Plot B.2, which was mainly

carried over to the steam generator secondary,

Plot B.53. The predicted initial heat loss to

the environments, was 260 kW, which is close to

the 250 kW estimated in the experiment (Ref 7).

The heat generated in the core after scram was

determinated by the space independent reactor

kinetics option of the code. The predicted decay

heat, Plot B.2, compares well with the decay

heat curve given in Ref 5.

The mass flow rates predicted in the hot leg,

Plot B.25, and at the core inlet, Plot B.11,

show a smooth decrease during the transient

which is mainly a result of the decrease of the

fluid density. Unfortunately no internal flow

rates in the experiment are qualified for comparisons after the break opened.

The predicted break mass flow rate, Plot B.39,

is within the uncertainty band of the measured

flow rate from 100 s on, see Ref 5. The experimental flow rate is qualified from 50 s. In the

interval from 50 s to 100 s after the break the

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predicted break mass flow rate is apparently

overestimated, however, some doubt may also be

put on the experimental flow rate. During this

time interval there is good agreement between

the predicted break fluid density and the chordal density measurement, Plot B.38. Whereas the

break fluid subcooled period ends at 44 s in the

experiment, it is predicted to occur much later,

at about 200 s, in the calculation, Table 2.

The behaviour of the main recirculation pumps is

showing up in the pressure head, Plot B.36. An

obvious cavitation in the experiment occurs at

290 s at which time also the loop seal becomes

filled with water, Plot B.31, and the steam

generator pressure difference, Plot B.46, rapidly diminishes (Ref 12). In addition effects from

the cavitation in the experiment can be seen in

the pump speed, Plot B.37, in the cold leg fluid

density, Plot B.28, and in the break fluid density, Plot B.38. A pump cavitation is not predicted at the time it occurred in the experiment. On the other hand the prediction shows an

earlier pump head loss when the two-phase fluid

starts to appear in the suction line, Plot B.36.

The primary side depressurization, as in the hot

leg, Plot B.27, is sligthly underpredicted from

300 s on. Pressures at high elevations, Plots B.21

and B.57, compare similarly. System pressures at

low elevations as in the lower plenum, Plot B.22,

and also in the cold legs, Plots.B.34 and B.35,

are still more underpredicted. As seen, there

might be a systematic error in the prediction.

However, the discrepancies are within the measurement errors, Table 4.

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After the fast depressurization has ceased the

primary fluid temperatures remain close to the

saturation temperature, Plots B.9, B.17, B.18,

B.20, B.26, B.33 and B.44. Minor deviations from

this situation are due to errors in the measured

temperatures, Table 4, and by the HPIS coolant

injection.

As for the pressure, the predicted underestimate

of primary temperatures for the rods, Plots B.3

through B.8, and for the fluid, Plots B.9, B.17,

B.18, B.20, B.26, B.33, B.41 and B.44, increase

in time. A possible reason for that is the uncertainty, 15 % up to 1 435 s, in the measured

break flow and consequently also in the primary

enthalphy content.

There is one plainly seen inconsistency in the

secondary side prediction of Case A. The downcomer collapsed level, Plot B.49, falls about

.6 m too low until the level starts to recover

due to the injected auxilliary feedwater. This

early level error, which corresponds to about

150 kg of fluid mass, then remains during all

the transient. Secondly, too fast a depressurization particularly at the end of the transient

is predicted, Plot B.51. Similar predicted pressure behaviours were obtained by the participants

of the ISPl1 (Ref 13) which also dealt with the

L3-6 experiment. Consequently there are reasons

to assume some inadequacy to be found in the

commonly used steam generator models.

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Several causes for the low fluid content may be

suggested, including errors in the feedwater

valve operation timing and the steam valve leakage. The void distribution in the boiling section

may be wrong due to the geometric model used.

Moreover, a non-negligible amount of water droplets may initially reside in the dome space above

the fluid level of the steam separator volume.

The predicted pressurizer fiuid temperatures in

the liquid space, Plot B.55, and in the vapor

space, Plot B.56, show substantial deviations

from the experiment. In the liquid space. the

computed water temperature, close to the saturation line, was compared with apperently superheated steam sensed in the experiment. The computed steam superheating, Plot B.56, was not

large enough. An other possible explanation,

would be some direct influence from the pressurizer vessel wall in the experiment.

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5 SENSITIVITY CALCULATIONS

The base case prediction displayed some deviations from the experiment which provide arguments for the sensitivity studies. A fluid

temperature and system pressure decrease faster

than in the experiment is in the first place

assumed to be a consequence of the steam generator behaviour or simply of the choice of break

discharge coefficient. In the Case B predictions

the steam generator model is changed. The sudden

pump cavitation in the experiment was not predicted. Consequently one calculation, Case C,

applied other pump characteristics.

5.1 Case B

Steam generators are supposed to act as the dominant heat sinks during small break transients.

However, the 4-in. diameter equivalent L3-6 experiment shows an substantial depletion of

coolant through the break so the steam generators become less important as heat sinks, ref

5. Actually the steam generator heat transfer

rate, Plot B.53, compared with the break energy

release, Plot B.40, and the structure heat

losses, Plot B.2, confirms that. Thus, the behaviour of the steam generator will be of less

importance for the primary side cooling.

The steam generator design, Figure 3, exhibits a

package of U-tubes which are supported by horizontal plates at equidistant heights. These plates,'

have possibly been understood to be inpgnetratable

for fluid thus bringing the geometry found in

the .Case A input. Then the boiler flow is forced

to a zigzaged flow path directed by the plates.

In reality the tube support plates are ported to

permit penetration of steam and water (Ref 6).

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Consequently the boiling section flow was directed

vertically in the Case B calculations. A more

efficient void rise indeed increased the initial

fluid mass by 90 kg. Further division of the

boiler flow into two parallel paths, one with

the ascending primary flow and one with the descending flow, added another 50 kg initial fluid

mass. Although the changes in the boiler geometry

increased the amount of initial water a lot, it

accounted only for part of the fluid mass missing

in the Case A calculation. According to Plot B.49

the discrepancy in liquid level between prediction and experiment increased with time in Case B

contrary to Case A.

The transport time from the feedwater inlet to

the downcomer bottom is quite short in the initial state. The liquid temperature at the downcomer bottom, Plot B.50, indicates that the feedwater valve closure starts later than at the

scram. Consequently in the Case B calculation a

feedwater valve closure starting at the HPIS

trip signal was additionally applied. As a

result another 70 kg of water was added to the

fluid mass, Plot B.49.

5.2 Case C

The previous two calculations predicted from

300 s on a slightly faster decrease in primary

system pressure and in fluid temperature than

measured. On the other hand were fluid densities,

Plots B.23, B.24, B.28, B.29, B.30 and B.38,

reasonably well predicted. Discrepancies from

the experiment starting at 290 s are more evident in the loop seal liquid level, Plot B.31,

and in the downcomer liquid level, Plot B.15, as

the pumps start to cavitate, Plot B.36. Obviously,

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the accumulation of water in low elevation areas

ot the loop starts with the cavitation. This is

the time at which the discrepancy in the depressurization rate starts oft.

The two-phase pump head, Plot B.36, was underpredicted in the Cases A and B. Chen (Ref 12)

and Modro and Chen (Ref 14) found less degradation for mainly all void fractions compared with

the pump characteristics of the LOFT base case

input (Ref 16) so far assumed. Because of that

the same pump data as those used by Grush et al.

(Ref 8) were applied in the sensitivity calculation Case C. These data had been obtained from

Chen's and Modros' works. In Case C also the updates of Case B were included.

The new two-phase pump characteristics resulted

in a better prediction of the pump head, Plots

B.36 and B.46. At the time of the pump cavitation, at 290 s, a rapid head loss appeared in

Case C too. However, as before in the Cases A

and B, the pump head turned out underpredicted

during almost all the transient. In the same way

the liquid levels in the downcomer, Plot B.15,

and in the loop seal, Plot B.31, did not show

any better agreement with the experiment.

NP80 AH
STUDSVIK ENERGITEKNIK AB STULSVIK/NP-87/128 20

1987-11-03

6 RUN STATISTICS

The input model for the base case RELAP5/MOD2

calculation for LOFT L3-5 encompassed:

113

122

99

volumes

junctions

heat structures

The volumes include two pump components, one

separator component and nine time dependent volumes of which three were involved for the steady

state. Among the junctions there are totally

tive valve components and four time dependent

junctions which are connected during steady

state.

During the transient calculation the following

resources were used:

computer time CPU = 58 675 s

number of time steps DT = 36 920

number of volumes C = 113

transient real time RT = 2 150 s

resulting in the following code efficiency factor (Ref 1)

CPU * 103=140

C * DT

The computer used was a Cyber 170-810.

NP?') AH
STUDSVIK ENERGITEKNIK ABSTDV/P-/281STUDSVIK/NP-87/128 21

1987-11-03

7 CONCLUSIONS

The LOFT L3-6 small break experiment has been

calculated using the RELAP5/MOD2 code as part of

Sweden's contribution to ICAP. The results from

the three-calculations done compare reasonably

well with most of the experimental data. None of

the sensitivity calculations has the capacity of

considerably increasing the prediction quality.

Consequently all three calculations show mostly

rather similar curves jointly away from the

measurements. Some more calculations had been

desirable but could not be afforded.

The steady state calculation was done in the

common way of applying auxiliary components and

regulators to speed up and stabilize. Acceptance

of a steady state followed when all the auxiliaries had lost importance for the subsequent calculations. Of a particular significance was the

temperature regulation of the feedwater to achieve

the correct steam generation rate.

One sensitivity calculation, Case B, addressed

the question of why initial secondary side fluid

content had been considerably underestimated in

the base case calculation. The two updates of a

vertical boiler flow and o± a delayed feed water

valve closure were not capable to fully rise the

low downcomer liquid level up to the measured

value. Actually, the reason for the low predicted fluid content of the secondary side was not

fully understood.

NP80 AH
STUDSVIK ENERGITEKNIK AB STUDSVIK/NP-87/128 22

1987-11-03

The other sensitivity calculation, Case C, focused on the behaviour of the main recirculation

pumps which were allowed to run at a constant

speed during the experiment. Updates in the

two-phase characteristics improved the prediction of the pump head in the crucial degradation region.. However, no other substantial improvements obviously turned out from this calculation.

The RELAP5/MOD2 code worked well during the calculations. The computer resources, made available by the Swedish Nuclear Power Inspectorate,

were quite extensive for this assessment test

case.

NPSO AH
STUDSVIK ENERGITEKNIK AB STUDSVIX/NP-87/128 23

1987-11-03

REFERENCES

I ODAR, F and BESSETTE D E

Guidelines and Procedures for the International Thermal-Hydraulic Code Assessment and Applications Program (Draft)

U.S. Nuclear Regulatory Commission,

1985

2 Acceptance Criteria for Emergency Core

Cooling Systems for Light-Water Cooled

Nuclear Power Reactors, 10 CFR, Part 50

(Appendix K), Fed Regist, 39(3).

(January 1974)

3 TRAC-PF1/MOD1:

An Advanced Best-Estimate Computer

Program for Pressurized Water Reactor

Thermal-Hydraulic Analysis.

NUREG/CR-3858

4 RANSOM, V H et al

RELAPS/MOD2 Code Manual

Volume 1: Code Structure, Systems

Models, and Solution Methods

Volume 2: Users Guide and Input

Requirements (Draft)

EG&G Idaho, Inc.

NUREG(CR-4312, EGG-2396)

(August 1985)

5 BAYLESS P D and CARPENTER, J M

Experimental Data Report for LOFT

Nuclear Small Break Experiment

L3-6 and Severe Core Transient

Experiment L8-1.

NUREG/CR-1868, EGG-2075 (Jan 1980)

6 REEDER D L

LOFT System and Test Description

(5.5-ft Nuclear Core 1 Loces)

NUREG/CR-DR47

TREE-1208

7 CONDIE, K G et al

Four-Inch Equivalent Break

Loss-of-Coolant Experiments:

Posttest Analysis of LOFT

Experiments L3-1, L3-5 (Pumps off),

and L3-6 (Pumps on)

EGG-LOFT-5480.

8 GRUSH WM, TANAKA M and MARSILI P

Best estimate predictions for the OECD

LOFT

Project Small Cold Leg Break Experiment

LP-SB-3

OECD LOFT-T-3603 (Febr 1984)

EGG-LOFT-5480 (Oct 1980)

NP80 AH
STUDSVIK ENERGITEKNIK AB STUDSVIR/NP-87/128 24

1987-11-03

9 KMETYK L N

RELAP5 Assessment: LOFT Small Break

L3-6/L8-1.

NUREG/CR-3163, SAND83-0245 (March 1983)

10 MODRO, S M and CONDIE, K G

Best Estimate Prediction for LOFT

Nuclear Experiment L3-5/L3-SA

EGG-LOFT-5240 (Sept 1980)

11 WHITE J R et al

Experiment Prediction for LOFT NonNuclear Experiment L1-4.

TREE-NUREG-1086 (April 1977)

12 CHEN, TH

Primary Coolant Pump Performance During

LOFT L3-6 Experiment.

EGG-LOFT-5414.

13 PETERSON, A C and COOK, C

International Standard Problem 11.

(LOFT Experiment L3-6/L8-1).

Final Comparison Report.

EGG-NTAP-6112.

14 CHEN, T H and MODRO, S M

Transient Two-Phase Performance of LOFT

Reactor Coolant Pumps.

ASME Winter Annual Meeting

Nov 13-18, 1983.

CONF-831111-16.

15 ERIKSSON, J

ICAP, Assessment of RELAP5/MOD2,

Cycle 36.04, Against LOFT Small Break

Experiment L3-5.

STUDSVIK Technical Note NP-87/63.

16 KEE, E J et al

Base Input for LOFT RELAP5 Calculations.

EGG-LOFT-5199.

NP80 AH
STUDSVIK ENERGITEKNIK AB NP-87/128 25

1987-11-03

Table 1

Initial conditions.

Predicted

Quantity Measured Case A Case B Case C

Primary coolant system

Mass flow rate (kg/s) 483.3 483.3 483.3 483.3

Hot leg pressure (MPa) 14.87 14.88 14.88 14.88

Cold leg temperature (K) 557.9 559.7 560.4 560.4

Hot leg temperature (K) 577.1 578.6 579.3 579.4

Reactor vessel

Power level (MW) 50. 50. 50. 50.

Pressurizer

Water temperature (K) 614.7 614.8 614.8 614.8

Pressure (MPa) 14.90 14.90 14.90 14.90

Liquid level (m) 1.18 1.18 1.18 1.18

Broken loop

Cold leg temperature (K) 557.6 559.6 560.6 560.6

Hot leg temperature (K) 561.4 557.8 556.1 556.1

SG secondary side

Water level (i) 0.22 0.22 0.22 0.22

Water temperature (K) 542.8 534.4 536.0 535.9

Pressure (MPa) 5.57 5.57 5.57 5.57

Mass flow rate (kg/a) 27.8 27.8 27.8 27.8

Table 2

Sequence of events.

Time (a)

Event Imposed System Predicted

action reaction Case A Case B Case C

Reactor scrammed -5.8 -5.8 -5.8 -5.8

LOCA initiated 0. 0. 0. 0.

HPIS Injection Initiated 3.6 2.3 2.6 2.6

Prssurizer emptied 20.2 25.4 25.4 25.4

Upper plenum reached saturation 28.5 40. 40. 40.

Intact loop hot leg voiding begin 29.4 38.7 38.9 39.1

Intact loop cold leg voldin begin 31.4 35. 35. 35.

End of subcooled break flow 44.2 91.6 91.6 91.6

SCS auxiliary feed initiated 73.4 73.4 73.4 73.4

SCS pressure exceeds primary pressure 930. 1925. 1720. 1740.

SCS auxiliary feed terminated 1856. 1856. 1856. 1856.
STUDSVIK ENERGITEKNIK AB NP-87/128 26

1987-11-03

Table 3

Parameters plotted and used in assessment comparisons.

COMPONENT CONTINOUS PARAMETER * EXPERIMENT

(IDENTIFIER)

PREDICTION

(MINOR EDIT)

PLOT IDENTIF.

EXP. CALC.

PLOT NO. - - ---- - ---------------- - - ----

CORE FLUID DENSITY (INLET)

HEATING POWER

CLAD TEMPERATURE. VOLUME I

(BOTTOM)

_ _ . oVOLUME 2

- " - * VOLUME 3

- VOLUME 4

. VOLUME 5

-VOLUME 6

(TOP)

TEMPERTURE (OUTLET)

TEMP. DIFF. (OUTLET-INLET)

CORE FLOW (INLET)

CORE INVENTORY

DOWNCOMER MASS INVENTORY

MASS INVENTORY (TOTAL VESSEL)

DOWNCOMER LIOUID LEVEL

UPPER PLENUM LIQUID LEVEL

DOWNCOMER TEMPERATURE (INLET)

UPPER PLENUM TEMPERATURE

UPPER PLENUM FLUID SUBCOOLINO

LOWER PLENUM TEMPERATURE

UPPER PLENUM PRESSURE

LOWER PLENUM PRESSURE

•S

TE-2G14-011

TE-SG6-O1

TE-516-005

TE-1F7-015

TE-1 F7-021

TE-2G08-021

TE-4114-021

TE-SF4-01S

TE-516-021

TE- F7-026

TE-t F7-030

TE-2GI4-030

TE-2H02-032

TE-4H14-028

TE-4H14-032

TE-SH7-026

TE-2G08°039

TE-2H01-037

TE-3CI1-039

TE-4114-039

TE-SH6-037

TE-2G14-045

TE-4G14-045

TE-5F9-045

TE-SG6-045

TE-SHS-049

TE-5H7-058

TE-SG6-062

TE-IUP-0O01

TE-SUP-001

TE-SUP-003

TE-I UP-001

TE-ILP-001

POE-RV-002

CNTRLVAR 901

RKTPOW 0

CNTRLVAR 903

CNTRLVAR 903

CNTRLVAR 905

CNTLRVAR 906

CNTRLVAR 907

CNTRLVAR 908

CNTRLVAR 909

CNTRLVAR 910

MFLOWJ 225.01

CNTRLVAR 912

CNTRLVAR 913

CNTRLVAR 914

CNTRLVAR 915

CNTRLVAR 916

TEMUPF 205

TEMPF 240

CNTRLVAR 919

TENPF 225

P 245

P 225

RHO 105

RHO 305

MFLOWJ 110

TEMPF 105

P 105

C1? 8. 1

C2? B. 2

C 3X C 37 B. 3

C4X C47 8.4

C SX C S? 8. 5

C 6X C 6? B. 6

C7X C7? B. 7

C eX C a? B. 8

C 9X C 9? B. 9

C AX C A? 8.10

C B? B.11

C C? 8.12

V 1? 8.13

V 2? 8.14

V 3X V 3? 8.15

V 4X V 4? 8.16

V 5X V 5? 8.17

**

VESSEL POE-RV-003 S

LE-IST-0O01

LE-3UP-O01 *5

TE-IST-O01

TE-25T-0O01

TE-IUP-O01

TE-4UP-001

TE-SUP-001

SC-SUP-102

TE-1LP-001

PE-IUP-OO1A1

PE-IST-OO1A

PE-2ST-OO1A

DE-PC-205 ** DE-PC-002A

DE-PC-0028 * DE-PC-002C 5*

DE-BL-0028

FT-P139-27-1

FT-P139-27-2 *5

FT-P139-27-3 **

TE-PC-0026

PE-PC-002

V eX V 6?

V 7X

V IX

V 9X

V AX

V 77

V a?

V 9?

V A?

8.18

0.19

9.20

0.21

0.22

HOT LEG FLUID DENSITY (I.L.)

FLUID DENSITY (B.L.)

MASS FLOW RATE

HLIX HLI? 8.23

HL2X HL2? 8.24

HL3? 8.25

TEMPERATURE (I.L.)

PRESSURE (I.L.)

HL4X HL4?

HL$X HLS?

8.26

8.27
bTUDSVIK ENERGITEKNIX AB NP-87/128

1987-11-03

27

Table 3 (cont'd)

COLD LEG FLUID DENSITY (1.L)

FLUID DENSITY (I.L. PUMP SUCTION)

FLUID DENSITY (B.L.)

LIOUID LEVEL CI.L. LOOP SEAL)

- 0 - (8.L.)

TEMPERATURE (I.L. NEAR VESSEL)

PRESSURE (I.L.)

- " - (S.L.)

PRESS. DIFF. (ACROSS THE PUMPS)

PUMP SPEED (PUMP 1 )

DE-PC-1IS 15

DE-PC-OOIA

DE-PC-DOtC

DE-PC-305

/DE-PC-003A/

/DE-PC-0038/

/DE-PC-003C/

DE-8L-105 a. DE-L-COO1A

DE-eL-O0IB

OE-DL-OOIC **

LEPDE-PC-028

LEPDE-BL-014 **

TE-PC-004

PE-PC-OOS

PE-SL-DOI

PDE-PC-001

RPE-PC-O01

BREAK FLUID DENSITY

MASS FLOW RATE

ENERGY RELEASE

INLET TEMPERATURE

INLET SUSCOOLING

INLET PRESSURE

So PRI. SIDE TEMPERATURE (INLET)

TEMP. DIFF. (INLET-OUTLET)

PRESSURE DIFF.

SG SEC. SIDE FLUID DENSITY

MASS FLOW RATE

LIOUID LEVEL

LIOUID TEMPERATURE

PRESSURE

DE-PC-SO2A

FR-PC-SBRK

a.

TE-PC-SOIC

ST-PC-S101

- TE-PC-SOIC

PE-PC-SOI

TE-SG-DOI

TE-SG-O01 - TE-SG-0O2

PDE-PC-002

LD-PO04-0088

TE-SG-003

PE-SGS-O01

RHO 185

RHO 115.13

RHO 345

CNTRLVAR 931

CNTRLVAR 932

TEMPF 185

P 120

P 345

CNTRLVAR 936

PMPVEL 135

RHO 800

MFLOWJ 805

CNTRLVAR 940

TEMPF 800

CNTRLVAR 942

P 800

TEMPF 115.03

CNTRLVAR 945

CNTRLVAR 946

RHO 515.03

MFLOWJ 516

CNTRLVAR 949

TEMPF 515.03

P 530.01

CNTRLVAR 952

CNTRLVAR 953

CNTRLVAR 954

TEMPF 415.02

TEMPG 415.07

P 415.08

CNTRLVAR 958

CNTRLVAR 959

CNTRLVAR 960

CNTRLVAR 982

BRIX SRI?

BR2X BR2?

8R3?

SR4X 8R4?

8RSX BRS?

BRSX 8R6?

CLIX CLI? 8.28

CL2X CL2? 9.29

CL3X CL3? 9.30

CL4X CL4? B.31

CLS? B.32

CL6X CL6? 8.33

CL7X CL7? 8.34

CL5X CLS? 8.35

CL9X CLS? 8.36

CLAX CLA? B.37

SPIX SPI? 0.44

SP2X SP27 8.45

SP3X SP3? 1.46

9.38

8.39

8.40

8.41

9.42

8.43

SSI?

SS2?

SS3X SS37

SS4X SS4?

S5SX SS5?

S IX S I?

S 2?

SG PRIMARY-SECONDARY TEJ.P.-DIFF. TE-SG-O01

(AT INLET) - TE-SG-003

HEAT TRANSFER RATE a.

8.47

0.48

8.49

8.50

8.52

8.53

8.54

5.55

9.56

8.57

PRESSURIZER LIOUID LEVEL

LIOUID TEMPERATURE

STEM TE]MPERATURE

PRESSURE

LT-PI39-006

TE-PI39-020

TE-PI39-019

PE-PC-004

FT-P128-104

P 1x

P 2X

P 3X

P 4X

P 1?

P 2?

P 3?

P 4?

ECCS

SYSTEM

RELAP5

HPZS VOLYMETRIC FLOW RATE

MASS BALANCE

COOLANT EGY. BALANCE (INTEGR.)

PRIM. EXTERNALS HEATFLOW

ECIX EdI? 9.S8

a.l

a.

a.

**

SYI?

SY2?

SY37

0.s9

9.60

S. 2

CCOMPUTATION CPU TIME

COMPUTATION MASS ERROR

CPUTIME 0

ElMASS 0

R 1? 8.61

R 27 8.62

* THE COMPARISON PARAMETERS ARE THOSE REPORTED AS DIRECTLY MEASURED

OR AS CCMPUTED RESULTS FROM THE EXPERIMENT

a. NO DATA AVAILABEL FROM THE EXPERIMENT

a.. DATA OBTAINED FROM BUBBLE PLOT IN EXPERIMENT REPORT

/ / EXPERIMENT DATA AVAILABLE BUT NOT USED IN COMPARISONS

? CALCULATION CASE (A. 8 OR C)
E 'Ail<K .3 NP-87/128

1987-11-03

Table 4

Measurement errors

28

Quality Uncertainty Comment

Pressure

Fluid temp

Fluid density

251-282 kPa

120 kPa

2.7-3.1 K

.5 K

5.9 K

10.4 K

78-82 kg/m3

129-131 kg/m3

Primary side

Secondary

side

Mostly

TE-P139-019,

steam

TE-SG-001,

TE-SG-002

TE-PC-004

Many measure

DE-BL-001A,

DE-BL-001C

DE-PC-002B,

DE-PC-002C

Cladding temp

Diff Pressure

Mass flow

3.1-3.2 K All

.49 k Pa PDE-RV-003

1. kPa PDE-PC-002

1.3 kPa PDE-RV-002

1.8 kPa PDE-PC-001

.02 L/s HPIS

6.3 kg/s I.L. init

condition

17 kg/s I.L. hot leg

25 percent Break,

40-750 s

1 kg/s Break,

750-2100 s

Liq level .04 m

.05 m

.099-.137 m

Bubble plot

1.22 rad/s

Pressurizer

SG secondary

Cold legs

Upper plen,

downcomer

Main recirc

pumps

Speed
S ouVSV. :~. T:EINI2 AB NP-87/128 29

1987-11-03

Table 5

RELAP5/MOD2 code features.

COMPUTATION PROCESSING FEATURES

- Several problem type and execution control options as

a. steady state initiallsation using fictitious structure heat

capacities for faster convergence

b. transient calculation

c. strip type execution, to select requested parameters from a

restart file

d. trip system, to decide on actions during calculation due

to reaching specified conditions in calculation parameters.

a. ability to delete or add hydrodynamic components, structure components and control variables at a restart of

calculation.

CLASSIFICATION OF HYDRODYNAMIC MODEL

- One-dimensionil, with provisions for

a. choked flow model

b. abrupt area change model

c. cross flow junctions.

- Two-fluid, six equation, space-time numerical solution scheme.

- flow regime oriented field characteristics depending on mass

flux and void fraction for

a. horizontal flow with bubbly, slug, mist and stratified

fields

b. vertical flow with bubbly, slug, annular-mist (and stratified) fields

c. high mixing flow with bubbly and mist fields (for pumps).
STUDSVIK ENERGITEKNIK AB NP-87/128 30

1987-11-03

Table 5 cont'd

HYDRODYNAHIC COMPONENENTS (Input systemat1cs)

- Volume type components

a. single volume

b. pipe and annulus, for condensed input of several similar

single volumes

c. time dependent volume, for defining a boundary source with

a time dependent fluid state

d. branch, a volume capable of two or more connecting junctions at either end

e. pump, characterized by rated values for flow, head. torque.

density and moment of inertia. The single phase homologous

curve, two-phase multipliers and phase difference tables to

model the dynamic pump behaviour

f. special system components for steam separator, jetmixer.

turbine and accumulator.

- Junction type components

a. single Junction

b. time dependent junction, for a time dependent Junction

flow whith a time dependent or controlled flow state

c. cross-flow Junction, to model a small cross flow, a tee

branch or a small leak flow

d. valve, various operation characteristics available for

check valve, trip valve, inertial valve and relief valve.

INTERPHASE CONSTZTUTVE BOUATIONS

- Interphase drag

a. steady drag due to viscous shear depending on flow regime.

Semi-empirical mechanisms to describe flow regime transitions

b. dynamic drag due to virtual mass effect.

- Interphase mass and heat transfer depending on flow regime and

the fluid fields to saturation temperature differences
STUDSVIK ENERGITEKNIK AB NP-8'1/128 31

1987-11-03

Table 5 cont'd

FLUID TO WALL CONSTITUTIVE EQUATIONS

- Wall friction due to wall shear effects formulated for flow

regimes and based on a two-phase multiplier approach.

- Wall

for

heat transfer depending on flow characteristics defined"

a. single-phase forced convection (Dittus-Doelter)

b. saturated nucleate boiling (Chen)

c. subcooled nucleate boiling (modified Chen)

d. critical heat flux (Blasi or modified Zuber)

e. transition film boiling (Chen)

f. film boiling (Bromley-Pomeranz and Dougall-Rohsenow)

g. condensation (partly Dittus-Doelter).

- Interfacial mass transfer at the wall depending on wall, fluid

and saturation temperatures for

a. subcooled and saturated boiling

b. transition film and film boiling

c. condensation.

HEAT STRUCTURES

These may be rectangular, cylindrical or spherical in shape.

The structure position is defined through component numbers of

left and right hand side hydraulic components. A structure is

physically defined by the geometry and the temperature dependent

conductivity and volumetric heat capacity data. The structure

model is further specified by the number of internal mesh points

in the direction of heat flow.

CONTROL COMPONENTS

By these new (control) variables are defined from calculated

parameters using algebra, standard functions, trip type operands or integrals.
STUDSVIK ENERGITEKNIK AB .,P-d 1/128

1987-11-03

32

Intact loop Broken loop

rA A

Reactor

vessel

Downcomet

C•re

Lower plenum

Figure 1

LOFT system configuration.
550 555

530

,En

tlj

z 415

560

519

517

115 '-a

~0

0

-4

I-I s-h

0

z

625

235

226

Figure 2

The nodalization diagram for

LOFT L3-6.

(AJ
STUDSVIK ENERGITEKNIK AB NP-87/128

1987-11-03

34

Figure 3'

The LOFT steam generator.
: 6. LOFT L.3; ANALYSIS (PRIJRY.SECODRY.KINTCS) *e

0MI0O00 NEW STOY-ST

0000101 Rm

0000102 WI S$

.000104 HOACTION

)000105 120. 200.0

0000120 100010000 0.0 WATER PRIMARY 0000121 117010000 0.0 WATER SECONDARY

T1IME ENDO IN STP MAX STP EDT OPT WON MAJR RST 000201 144.2 I.OE-6 .20 00001 25 4000 4000

MINNOR EI)T VARIABLES FOR THE ICAP ASSESSMENT

&000301 €XrRLVAR 901 0000302 RKTPOW 0 0000303 CNTRLVAR 903 0000304 CHTRLVAR 904 0000305 CHTRLVAR 905 0000306 CNTRLVAR 906 000030? CNTRLVAR 907 0000308 CHTRLVAR 908 0000309 CNTRLVAR 909 0000310 CHTRLVAR 910 0000311 MFLOWJ 225010000 0000312 CNTRLVAR 912

SS*****S*SS.SSS4SS*~94S**6454S640*4S64*e *3564**44,00 * VESSEL

0000314 CKT RLVAR 914 0000315 CNTRLVAR 915 0000316 CNTRLVAR 116

0000317 TEMPF 205010000 0000316 IEMPF 240010000 0000319 CNTRLVAR 919

0000320 TEMPF 225010000 0000321 P 245010000 0000322 P 225010000

e HOT LEG

0000323 RHO 105010000 0000324 RHO 305010000 000032S MFLOXJ 110010000 0000326 TEMPF 105010000 00003!7 P 105010000

* COLD LEO

0000328 RHO 1S5010000

0000221 o 11SO20000 0000330 R140 345010000O 0000331 C4TRLVAA 931 0000332 CNTRLVAR 932 0000333 TEM)F 135010000 0000334 P 120010000 0000335 P 345010000 0000336 OETRLVAR 936 0000337 FMPVEL 13S

* BREAK

000033: moO Is5010000 0000339 MFLOWJ 806000000 0000340 CN•RLVAR 940 0000341 IYEPF 300010000 0000342 CNTRLVAR S42 0000343 P IS5010000 0000344 TEMPF 116030000

0 STEAM GENERATOR 0

0000346 CNTRLVAR 545 0000346 CHTRLVAR 546 0000347 RIH SI030000 0000348 WNL09J 516000000 0000349 COTRLVAR 949 00003S0 1EMPF 1150300010 0000351 P 530010000 0000352 ConTALVAR 952 0000353 CTRALVAR 953 *s~teesss4eese*5e554*S**S5$535

e PRESSURIZER

0000354 CNTRLVAR 5S4 0000355 TEIMF 415020000 0000356 TEMPO 416070000 0000i37 P 41E060000

* EcCS

0000358 CKTALVAR 9S6

5 SYSTEM

0000359 COTRLVAR 255 0000360 C)TRLVAR 560 0000382 CHTRLVAR 932

* RELAPS

0000361 CIITIME 0 0000362 (MASS 0 *5*** eee e5o e 6 * 56*55 **SS 555. 4

* STEADY STATE CONTROLS

0000370 CTARLVAR 272 0000371 CN3RLVAR 296 0000372 CNTRLVAR 372 0000373 Ct RLVAR 291 0000374 CHITLVAR 216 000037S CNIRLVAR 601 0000376 CNTRLVAR 606 0000360 CHTRLVAR 960 0000352 CHIRLVAR S52

rtn

0

U)

i-4

t•l

H

66*I.**3563S5.6466065505664486565 p O*5548543S55533855546S518866S8S545666*54*094945658*56556 5650

[*T-TrT*5456*3 4 T46T**8o 43*S*54*56

T TRIP INPUT DATA

511 TRIP

9e 14 BRAK.N

SI m MLOW 641 ScAS

48

* • Ill 'TRIP

S 9t

S)

REACTIVITY. OEN. TABLE SS AUX PRESSUIIZ. VALVE ClOS MAIN STEM. VALVE. CLOSE FEED WATER VALVE. CLOSE

TIME

ALOX FEED WATER

P0•M9 2

CLOSE

AFTER EXPERIMENT EDO

DIRECTION OF FLON FROM ORE

mSP. BREAK PLOW OUALIFIED

STOP AIV. Of CALCURATION

BREAK OPEN

PRESS. VALVE OPEN. AFTER 55

INITIATED

PUMP COOLANT INJECTION

6011

410

550

560

548

135'SS

SOS

240

OS

SOS

435

640

901

***5**5~45666*5e'S5454SSSSS*S568l

6564544 *46446*66454*8*S*5*6654666

SSSSS*85665555S5#*53*665655545466*o

*.56565.0*S*S6*.*665*6548*6658S94*6

S6*$6.5646**6@S.*SS*S***5****54*650

S--h

00

cIS-'

eaga*~eeess.ae.~s.sms.556.545S*6e*56 £554554

:01 TIME 0 CE HULL 0 144.2 L 608 TIME 0 GE IJLL 0 0.0 L &10 TIME a GE TIMEOF 601 5.8 L Sil TIME 0 CE IIMEOF 510 10000. L 612 TIME a GE MILL 0 10000. L 613 P 100010000 LIE MILL 0 13.23& N 514 P 100010000 LE NULL 0 2.1516 L 515 TIME 0 GE TIMEOF S14 20. L $1i VELFJ 240010000 CE WULL 0 0.0 N4 520 P 530020000 CT HULL 0 S.63(6 N 521 P 630020000 LT MULL 0 S.51[& N 622 P 530020000 GT MULL 0 S.SSE6 N 623 P 530020000 LT MILL 0 5.53E6 N 0530 OETRLVAR 10 LT OILL 0 3.10 N 5131 CXTRLVAR 10 GC PULL 0 3.15 N 535 TIME 0 GE TIMEOR SIO 50. L 533 TIME 0 GT TIM(OF SI0 £3. N 561 P 1000o0000 GT P 530020000 0. N 562 TIME 0 GO TIMiOF 640 1800. L 600 St . A 660 514 AM I £61 $13 ANO -514 N 699 -614 AND .514 N 600 530 OR 502 N *602 -s31 ^NO 601 N 1603 562 AO 602 N

610 612 Oft 530 Nf

It

-4

S-a

CD

k1

I...

I-
L11

612

13

614 61 616S

64

633

$634

634

64S

S46

46

-521 611

616s

-522

-all

a's

533

633

510

510

-S01

AND NCO

O0

AND

AND

AND

AND

oft

AND

-610 

N 610 SI

523 

N 613 N 501 SI

614 

S

-660 SI 603 S too L

No -514 

S

NC -601 

S

* t o4e0044440~oo~.... 

. .. so .................... 0 

* INTWCT LOOP

G eS e0SsSSS655S5•46444S4emS04466S6*44eS044SS44444 0

SREACTOR VESSEL NOZZLE INTACT LOOP NOT LEG

1000OO0 RWI1a B6RAIC. 1000001 2 I 1000101 0.0634 1.5373 0.0 0.0 1000102 4.06-5 0.0 00 1001101 296010000 100000000 0.0634 0.1 1002101 100010000 I0SO000X 0.0 0.06S

* PRESSURJZER •ONNECTION TEE REACTOR VESSEL SIDE

1050000 PITRY'S BRANC4 S1060001 1 1 1050101 0.0634 1.634 0.0• 0.0 1050102 4.OE-6 0.0 00 1051101 10501000I 10000000 0.0 0.0s6

STEAM 7 GENERATOR INLET PIPING

1100000 SGII4LP BIKAMCI

1 00001 I 

I

1100101 0.0 1.1303 0.06204 0.0

1100 102 4.0E-5 0.0 00

1101101 110010000 I16000000 0.0 0.17

SSS*Soo**oSS**S*SSS04¢leeee*40SS4*SSS4,SSS44*,0444

11 60302 0 • 0 

2 1150303 0.63 3 1150304 1.0022 4 1150305 .7102 5 16SO306 0.7576 7 1150307 .7102 S 1150300 1.0022 a

eet44S8SoS*404*o 1160309 0.63 10 4*S95440004555*0 1150310 0.547 I1

1160311 0.669 12 1160313 0.535 12 11.0401 0.05426 1

eSSoeSee.S545S 1150402 0.057 

2 1150403 0.223 3 • 1150404 0.0 9 115040S 0.223 I0

1150406 0.0437 II 1150407 0.0462 12 0.0 0.0 1160408 0.0 13 1160501 0.0 13 0.1 0102 1150601 1.0 1 0.065 0l00 11 50602 90.0 6 1150603 -90.0 13 •*65e4545*455544 1160701- 0.0 I

* 1150702 0.246 2 11MM02 0.613 3 1150704 1.:322 4 115070S .7102 5 0.0 0.0 1160704 0.:576 6 1160707 -0.8574 7 O.06s 0100 1150700 -. 7102 0 1160709 -1.0022 • *..4ee44e440*ees 1150710 -0.513 10 S 11650•11 -0.494 if 1150712 -0.689 12 1150713 -0.356 13 1150801 4.00-S 0.0

0.0 0.0 1150802 4.0-5 0.02 11 S0•03 1.0E-3 0.0:,1013

0.17 0100 1160604 4.0E-5 0.0102 10 1150605 4.05-5 0.0 13

4*e**0**t44•44• 1150901 0.255 0.255 

t * 1150902 0.048 0.046 2 1150903 0.0 0.0 4 1150904 0.096 0.096 5 116090S 0.192 0.192 6 1 160906 0.096 0.096 ? 1150907 0.0 0.0 t 11 0904 0.046 0.045 to

1160909 0.096 0.096 12 1151001 00 13 1151101 0100 3 1151102 0000 2 1151103 0100 12

1151300 1

SPUMP SUCTION TEE 

6

1200000 PSTEE BSANCH 1200001 3 I 1200101 0.0634 0.76 0.0 0.0 0.0 0.0 1200102 4.0E-S 0.0 00 1201101 115010000 120000000 0. 0.096 0.096 0000 1202101 120010000 126000000 0.0317 0.2 0.2 0100

En

ti

1-4 W

1203101 120010000 165000000 0.0317 0.2 0.2 0100

o PIAIPI SUCTION TEE OUTLET

125O00 PISTOL BRANCH 1250001 2 1 1250101 0.0 1.003 0.0613 0.0 90.0 0.521

1250102 4.06-5 0 .0 00 1251101 126010000 130000000 0.0 0.1 0.1 0100

1252101 12500000 155000000 .012417 O.0 0.0 6010 0

: PtW I INLET 

S

1300000 PIINL SNCLV4L

1300101 0.0 0.457 0.0111. 0.0 40.0 0.467 1300102 4.06-6 0.0 00 S

e PRIMARY COOLAN PFLW I TRIP-511

13S0000 PCPI PIJ 1350101 0.0364 0.0 0.099 0.0 90.0 0.319 1360102 0 1350108 130010000 0.0 0.0 0.0 0100

1350109 140000000 0.0 0.05 0.04 0100

1350301 0 0 0 -I -1 S11 

C 1350302 369.0 0.911 0.31S$ 96.0 S00.6 1.431

1350303 613.6 0.0 207.4 0.004 11.698 0.0

1350308 .212465 0.0 -26. 29.6 6.28

1350310 0.0 0.0 0.0

* PUMP I OUTLET PUM SIDE

1400000 PIOTLPI $NGLVOL 1400101 0.0364 0.602 0.0 0.0 0.0 0.0 1400102 4.06-6 0.0 00

e COOLANT PUMP INJ. (JOINED ONE PUMP) 0

9010000 PCPINjI I1CPJUN 9010101 110000000 140000000 0.0 9010200 1 611 1010201 -1. 0.0 0.0 0.0 9010202 0.0 .096 0.0 0.0

9010203 10000. .094 0.0 0.0

;100000 PCPWATER 1SUVOL 9100101 7.E-3 1.0 0.0 0.0 0.0 0.0

:100102 0.0 0.0 00 100200 I 1100301 0.0 30S. 0.0 S100202 10000. 305. 0.0

* PUWI OUTLET PIPE TEE SIDE 

5

SSTEA.A GENERATOR PLUS PIPING

1160000 SAPS PIPE

1150001 13 1150101 0.0O

1150102 0.151 

9

1160103 0.0 12

IISO104 0.0634 13

11SO301 0.0 

1

1150202 0.0512 

2

1150203 0.0 

9

1150204 0.0512 10

1150205 0.0 12

1150301 0.93124 

1

I-A

co

1.4

I.-AI0

ti,

z

ID

No

co

(I)

10* ti•

I.-,-

x4

"tJ

14S0000 POPTS BRANCH

1450001 2 I

1450101 0.0 1.4004 0.0633 0.0

1450102 4.0E-6 0.0 00 1461101 140010000 145)00000 0.0 0.0

0.0 0.0

0.0 0100
1452101 1450I0000 1000000 .035073 0.0 0.0 0100

* P1t OUTLET TEE 0

1S300000 POTLTEE BRAWC.: 1I SO00 2 I 1500101 0.034 0.4966 0.0 0.0 0.0 0.0 1S00102 4.MO-M 0.0 00 1601101 170010000 150000000 .0271528 0.2 0.2 0100 1602101 10010000 175000000 0.0 0.134 0.134 0100

PUP 2 SUCTION TEE CUTLET

1550000 P25TO. SpkC4 IS•0001 I I 15SO101 0.0 1.003 0.0613 0.0 90.0 0.621 15St002 4.OE-s 0.0 00 1551101 155010000 160000000 0.0 0.05 O.OS 0100

P UP 2 INLET PIPE S

1WO600 P21N1 SNaOL1A. 1600101 0.0 0.465 0.0155 0.0 10.0 0.457 1600102 4.0GE- 0.0 00

S PR•IMAy COOLANIT PUMP 2 0

1610O0 PCP2 PUWM 1610101 0.0300 0.0 0.031 0.0 90.0 0.319 1610102 0 1650108 160010000 0.0 0.0 0.0 0100 1650109 110000000 0.0 - 0.05 O.Os 0100 1650301 135 136 135 -1 -1 S11 0 1650302 369.0 O.sl.1 0.31s5 96.0 500.6 1.431 1650303 613.6 0.0 207.4 0.004 19.598 0.0 1650308 .212465 0.0 -25. 29.5 S.26 1610310 0.0 0.0 0.0 0

*S*S• •• *• •** •lls*el• * 41•5*S*9405•549•• 9499e55•445•6,555

o PUM 2 OUTLET S

1700000 P2mnm. eutNm 1700001 1 I 1700101 0.0366 0.514 0.0 0.0 0.0 0.0 1700102 4.OE-S 0.0 00 1701101 145010000 170010000 0.009073 0.2 0.2 0100

* COLD LEG PIPE 10 IOC CONNECTION TEE

1o70000 PTECT PIPE 10S00I 2 1?sO101 0.O064 2 1750301 0.0 I 170301 0.553 I 11S0302 0.613 2 1710401 0.0 2 1I10101 0.0 2 1150601 0.0 2 1750701 0.0 2 175001 4.O6-5 0.0

1760901 0.15 0.15 1 1751001 00 2 1751101 0100 I

17,1300 I

* ECC CONNECTION TEE PUM SIDE

1800001 1 1 1500101 0.0634 .701 0.0 0.0 0.0 0.0

1500102 4.0-E3 0.0 00

1$01101 17.1010000 10000000 0.0 0.064 0.0664 0100

0

tij

z

1I-

'-4

LI-4

SCOLD LEO PIPE PAN6 ECC CHEECTIO0N TO REACTOR VESSEL S z 0

1550000 CLPRVS BRANCH 1:510001, 2.03 1 1050101 0.0634 1.461 0.0 0.0 0.0 0.0

1850102 4.06-S 0.0 00 1851101 155010000 29000000 0.0634 1. 1. 0101

1652101 180010000 155000000 0.0 0.0 0.0 0100

• .**..s.s.....*ee •*..*o o.o.os.•**.-*ss e~*..o.s••*•**.*os.*s..*.

DISCHARGE VOLUME

:200000 BREARVOE. IIMDPVO 6200101 3.6E-3 I. 0.0 0.0 0.0 0.0 0200102 0.0 0.0 0.0 5200200 2 8200201 0.0 1 .S 1. 5200202 100OO. I.E5 I.

O 8REAK OUTLET LINE

6000000 8000001 SROUTL I BRANCH I

8000101 .00090! 1.6 0.0 0.0 0.0 0.0 8000102 I.E-S 0.0 00 6001101 18S010000 O00000000 0.0 .S .5 0102

o BRAKE VALVE (ORIFICE) 9010000 SJT~vLv VALVE 5050101 800010000 820000000 205.6-.6 .4 .4 0100 .$5 .85 5050300 1TRVLV 9030301 641 S14 S. 0.0

*.o,.e••s.o¢*..*•ooeooe~els.....*•*•e*oe.elole••*eleese*.ae.*•*s'

* REACTOR VESSEL

C00.D LEG INLET ANNULUS

• 2000000 INANLCVOI. BFAIC 2900001 I I 2900101 0.0 .30 .076 0.0 2W00I02 4.6-S .172 00 2901101 200010000 290000000 0.0 0.0 0.0

* INLET ANNULUS TOP VOLUME

2000000 'ZANLIVOL ORANO4 2000001 0 1 2000101 0.0 0.11 0.0445 0.0 2000102 4.0-5 0.178 00

2050101 0.0 0.274 0.07t 0.0 20SO102 4.O4-1S 0.172 o00 9I1101 20601000 210ROLI0 0.0 0.0

2100000 DWMIVCO4R PIPE

2100001 4 2100101 0.142 4

2100201 0.0 3 21 00301 O.9S4 4 210O401 0.0 4 2 100501 0.0 4 210¢601 -90.0 4 2100801 4.OE-5 0.102 0 21 00901 0.0 0.0 0 .0 2100001 O0 PE 2101101 0.0 3 2101300 0

• OWERt PLENUM• UPPER VOLUME

2150000 LPUVO BRANCH

2150001 3 4 2150101 0.740 0.34 0.0 0.0 2150102 4.0E-5 0.0 00 21051101 210010000 21S00000 0.0 0.0 2152101 21501000 220 0.0 0.0 2153010 215000000 225000000 0.16 0.0

• LOWER PLENUM LUWER VOLUIE 2200000 LPLOV04. RSNGLVO

2200101 0.790 0.360 0.0 0.0 2200102 4.O6-S 0.0 00

• LOWER COlRE SUPPORT STRU•CTURE[ 2510000 LCOS 20T 0. .

2250001 1 1 2•05101 O.25 0.0 2 0.0 0.0 2250102 4 0O2- 0 0 .19 0.0

90.0 0.10

-90. -. 30

0100

9S459905**S0SS**SSA

-90.0 -0.274

0.0 0100

005..SS.*.0S'*(S• ~00e0

I-A

ID

00

CA, w•

2:

I'

00

-90.0 -0.360

0.0 0100 0.0 0100 0.0 0100

-90.0 -0.370

'6*SSSS**S*••••*SSS*S .J.

x

(Si

00.0 0.32
2251101 22501OOO 220000000 0.097S 2.4 2.4 0100

* VALVE JUNCTION FOR CORE BYPASS FLOW

2260000 CBPVLV VALVE 2260101 226010000 235000000 .015 I. I, 0100 2260201 I 20. 0.0 0.0

2260300 S"WLV

2260301 226

* ACTIVE CORE 0

2300000 CORE PIPE 2300001 6

2300101 0.170S 6 2300201 0.1705 I 2300202 0.1440 2

2300203 0.1705 3 2300204 0.1440 4

2300205 O.1705 5

2300301 0.2795 a 2300302 0.3776 6 2300401 0.0 • 2300S01 0.0 6 2300601 90.0 6

2300801 4.O6-5 0.012 6 2300901 0.0 0.0 1 2300902 .6 .5 2

2300903 0.0 0.0 2 2300904 .5 .6 4 2300905 0.0 0.0 S 2301001 00 6 2301101 0O00 5

2301300 I

* BYPASS VOLUAME

23S0000 BYPVOL PIPE

2350001 3 2350101 0.01 3 2 2350201 0.0 2

2350301 0.559 2 2350302 0.657 3 2350401 0.0 3

2350501 0.0 3

2350601 90.0 3 2350801 4.OE-5 0.002 2 2350901 0.0 0.0 2

2351001 00 3 2351101 0000 2 23S1300 I

*S.*S*SSSSSS*SSSSSSSS.oe. oee~eoe••s....,.S*S**.*96eeSSS*S*SSooo**

* UPPER CORE SUPPORT STRUCTURE S

2400000 UCOSST BRANCH 2400001 2 I 2400101 0.297 1.I1a 0.0 0.0 90.0 1.118 2400102 4.06-5 0.145 00 2401101 230010000 240000000 0.12 2.O 2.40 0100 2402101 235010000 240000000 0.0 1.so 1.60 0100 0

• **S$SSeSooSS SSSSS*S•40S*S*S*SSS*e4S**S6SSSSSS*SSSS* SSS*SSo*Seee

* UPPER FLOW SKIRT REGION

2450000 UFOSRIE SRANIh 2450001 I I

2450101 0.114 0.693 0.0 0.0 90.0 0.093 2450102 4.0E-S 0.131 00 2461101 240010000 246000000 0.0 0.0, 0.0 0100

**4**S@******,4 *S* *9,6**•e*SS4,0*te6.4**94S,*S* ***S••eSS •0 s*SSSS**9SS

D EADF END OF FUEL MCOULES 0

2460000 FI 1. SRANWN 2460001 I I 2460101 0.153 0.700 0.0 0.0 90.0 0.700 2460102 4.OE-6 0.214 00 2461101 240010000 24600000O 0.0 0.0 0.0 Ot00

o**S*******SS*SoS6•*S@*oSSSSSSSSS*6o*S96oe**So~o*Se*o4**•),*•440.

* REACTOR VESSEL HOT LEG OUTLET

295OO00 WIUOUlr BIRANCH 2950001 1 1 2950101 .201 .30 0.0 0.0 s(d. .30 2990102 4.6-S 0.0 00 2951101 245010000 296000000 0.0 0.0 0.0 0100

• VALVE JUNCTION INLET ANM. TO UPPER PL[NUM.

2960000 IAUPVL.V VALVE 2960101 200010000 250000000 .01 I. 1. 0100 2960201 I 15.0 0.0 0.0 2960300 SRV.LV 2960301 296

****5454555*5565.46546455S6*se**s**66***..4e**.696..9..494.9

* VALVE JUNCTION4 INLET ANN. TO UPPER PLE5NM

2970000 IAUPVLI VALVE 2970101 205000000 245010000 .01 I. I. 0100 2970201 I 16.9 0.0 0.0 2970300 SRWLV 2970301 296

0 VALVE JUNCTION INLET ANM. TO OW4CCOWR

2910000 IAUOOM VALVE 2910101 290010000 205000000 0.269 I. 1. 0100 2910201 I 444.9 0.0 0.0 2910300 SRVVLV 2910301 291

**S*SSS*556 555e5t See5e5*ee~tS*S4SS*eSeeoS*SS*e*IsS.S**.*tS* 666.4

* UPPER PLENUM LOWER VOLUME .

2SO0000 UPLLVOL BAPNCH 2500001 2 I 2600101 0.2096 0.704 0.0 0.0 90.0 0.704 2500102 4.06-S 0.0 00 2501101 295010000 250O000000 0.0 0.0 0.0 0100 2502101 260010000 265000000 0.0 0.0 0.0 0100 S*e••e•~e•eeeoloeoee•eeeooeooeee,

1.-

En

H

tl,

H

: UPPER PL5NIA UPPER VOLUMt

265O000 UPLUVO. SNGLVO.L 2650101 0.244 0.712 0.0 2650102 4.06-1 0.0 00

0

0.0 90.0 0.712

*,**9*olaf*SSS*SSooqs*•ebS*6,*S*S4*Se*6SSS oSS S96•66966*S*6S66o*SS•

S* PRESSURIZER

SSURGE LINE PC$ SI0E 9

4000000 SPCS BRANICH 4000001 2 I 4000101 O.0O146 3.45 0.0 0.0 90.0 0.64 4000102 4.06-6 0.0 00 4001101 110000000 400000000 0.0 0.93 0.93 0100 4002101 400010000 405000000 0.0 0.93 0.93 0000 S*e *SS t oo 4 ooeSS.S.SS6S..,*S66*•.•om**6•S*SSS*66944446696SSS66S

0 SURGE LINE PRESSURIZER VESSEL S

4050000 SLPRV SNGLVOIL 4050101 0.00145 3.45 0.0 0.0 90.0 0.60

4060102 4.O0-6 0.0 00

* PRESSURIZER SURGE LINE VALVE S

4100000 SLVALV VALVE 4100101 405010000 416000000 0.0 0.93 0.93 0100

4100300 TRPVLV 4100301 b01

* PRESSURIZER VESSEL 6

4150000 PRESSV PIPE 4150001 a 4150101 0.362 I 4150102 0.665 5 4150103 0.466 7 4160104 0.13 8 4150201 0.0 7 4150201 0.274 1 4150302 0.403 3 4150303 0.207 5 4150304 0.1700 7 416030S 0.115 S 4150401 0.0 5 4150501 0.0 S 4150601 90.0 5 4150e01 4.0E-5 0.0 a 4151001 00 4 4161002 01 a 4151101 0100 I 4161102 0000 7 4161300 1

* TOP VOLUME PRESSURIZER 0 0

$-A

ID

I0

0

I,

CO

-J4

CO

"0

(D

CIA.

x
4200000 TOPPRE 8ARM:H A200001 I 0 A200101 0.13 0.236 0.0 0.0 10.0 0.236 42O1O02 :.SE-S 0.0 01 4201101 415010000 420000000 0.0 0.0 0.0 0000

iee ...... e.eo.o o.o..46..46.4.eo..464u646.4.e*8.e)*0688**4686.886

HEAT STRUCTURE INPUT DATA

8

gs*oeo * EACTOR s0*. VESSEL 044#o*seen.*s.6*o.o4o.....e•.s86 HEAT STRUCTURES o8*6***844.66

* FILLER BLOCKS INLET ANNULUS TOP VOLUME

12000000 1 6 2 1 0.606 12000100 0 I 12000101 4 0.772 12000201 4 4 12000301 0.0 4 12000401 565.2 5 12000501 200010000 0 I 1 0.33 I 12000601 0 0 0 I 0.33 I 12000701 0 0.0 0.0 0.0 I 12000801 0 .178 0.0 0.33 I

* FILLER BLOCKS INLET M4.US LOWER 5LUd 8

l2050000 1 2 I 0.I01 12050100 1 12050101 4 0.768 12050201 4 4 12050301 0.0 4 12050401 565.2 6 12050SOI 205010000 0 1 I 0.424 1 12050601 0 0 0 1 0.424 1 12050701 0 0.0 0.0 0.0 I 12050801 0 .172 0.0 0.424 I 6

t LOCKS DOILE6 C0MER NO LOWER PLEUM .

12100000 6 5 2 1 0.47 12 100100 0 1 12100101 4 0.736 12100201 4 4 12100301 0.0 4 12100401 565.2 5 12100501 210010000 0 I 1 0.956 I 121OOS0O 210030000 0 I I 0.958 3 12100504 210040000 0 I I 0.9,8 4 12100505 2350100X O I I 0.36 5 12100506 220010000 0 I I 0.37 a 12100601 0 0 0 1 0.956 4 12100602 0 0 0 I 0.36 6 12100602 0 0 0 1 0.37 6 12100701 0 0.0 0.0 0.0 6 12100801 0 0.102 0.0 0.968 4 12100802 0 0.971 0.0 • 0.26 S 12100608 0 1.003 0.0 0.a 37

: CORE SUPPORT BARREL

12010000 6 5 12010100 0 1 12010101 4 0.4101 12010201 4 4 12010201 0.0 4 12010401 565.2 • 12010501 200010000 0 12010502 205010000 0 12010503 210010000 0 12010504 210020000 0 12010505 210030000 0 12010506 210040000 0 12010601 0 0 12010602 0 0 12010603 0 a 12010604 0 0 12010605 0 0 12010606 0 0 12010701 0 0.0 12010601 0 0.179 12010602 0 0.172 12010803 0 0.102

* FLOW SKIRT - CORE FILLER AS.

12250000 10 1 12250100 0 I 12250101 4 0.38 12250201 4 4 12250301 0.0 4 12250401 665.2 6 12250501 225010000 0 12250502 230010000 10000 12250SO3 230060000 0 12250304 240010000 0 1225050S 245010000 0 12250506 246010000 0

12250601 0 0 12250602 0 0 12250603 0 0 12250604 0 0 12250605 0 0 12250606 0 0

12250701 0 0.0

12250860 0 0. 12260802 0 0.012 12250803 0 0.012 12250804 0 O.145 1225005 0 0.131 12250006 0 0.214

0.3110

r")

I-V

tI'

I 0.33

0.424 I 1 0.0SS 0.956

1 0.958 I 0.954 I 0.22I

I 0.424

0.958 1 0.958

1 I 0 0.956 .$56

0.0 6 0.33 I 0.424 2 0.645 6

1

23

4

2

3

4

5

6

12300301 1.0 • 12300302 0.0 6 12300401 I100. 6 1220040 0. 8 12300501 0 0 12300502 0 0 12300601 230010000 1000 12300602 232060000 0 12300701 I00O 0.061 12300702 low0 0.262 12300703 1000 0.245 12300704 1000 0.226 12300?05 1000 0.146 12300706 1000 0.026 12300901 0 0.01260 12300902 0 0.01260 8,

0 1 5263.3S 0 1 490.7s ? I 3263.26 I 1 490.76 0.0 0.0 I 0.0 0.0 2 0.0 0.0 3 0.0 0.0 4 0.0 0.0 S 0.0 O.0 6 0.0 0.2795 6 0.0 0.3??56•

s

6

o

6

SOSLY

2 1 0.3

! I 0.52 t 1 0.2295 6 I 1 0.3725 7 1 1 1.118 6 1 1 0.42 6

I 0.25 10 0 I 0.52 1 0 I 0.279S 6 0 1 0.2725 7 0 O I 1.116 6 1 0.42 6

0 1 0.35 10 0.0 0.0 10 0.0 0.52 I 0.0 0.279S 6 0.0 0.3775 7 0.0 1.118 a 0.0 0.42 6 0.0 0.35 10

S *FUEL 56OULIESS

12460000 1 S ! I 0.0 12460100 0 1 12460101 4 0.01 12460201 4 4 12460301 0.0 4 12460401 665.2 • 12460501 24501000 0 1 1 1. 1 12460601 246010000 0 1 I 1.0 1 12460701 0 0.0 0.0 1.8 I 12460601 0 0.131 0.0 1.8 I 12460901 0 0.214 0.0 1.8 1

*REACTOR VESSEL BOTTOM

12200000 I 1 1 0.0 12200100 0 1 12200101 4 0.092 12200201 4 4 12200201 0.0 4 12200401 665.2 8 12200501 -999 0 3949 0 1.66 1 12200601 220010000 0 1 0 1.68 12200701 0 0.0 0.0 0.0 1

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12300000 6 9 2 1 0.0 12300100 0 1 12300101 o 6 4.647E-3 1200102 I 4.742E-3 12300103 2 8.3519-3 1230001 0 2 1200202 -2 6 12300203 -3 a

22C0000O I W ST U

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• UPPER HEAD TOP PLATE

12600•00 1 5 1 1 0.0 12550100 0 1 •

12550101 4 0.474

12550201 4 4 12550301 0.0 4

12550401 566.2 5 12SSOSOI 25501000O 0 1 I 0.712 4

12550601 -999 0 3940 1 0.712 12550701 0 0 0.0 0.0 I 12S50801 0 0.0 0.0 0,712 I

* CORE SUPPORT BARREL UPPER PLEUM LOWER VOLUME

l2SO0000 1 5 2 1 0.3s1

12500100 0 1 12500101 4 0.419 12500201 4 4 12500301 0.0 4 12500401 665.2 0 12500501 2SOI0000 0 • 1 ! 0.54 12500601 0 0 0 1 •0.54 12500701 0 0.0 0.0 0.0 1 12500801 0 0.0 0.0 0.054 1

* CORE SUPPORT BARREL UPPE R PLENUI TOP VOLUME

12520000 1 $ 2 1 0•381 12520100 0 1 12520101 4 0.720

12520701 4 4 12520301 0.0 4

12520401 665.2 B 12570501 255010000 0 1 1 0.712 12520601 -99" 3949 I 0.712 12520701 0 0.0 0.0 0.0 I 12520801 0 0.0 0.0 O.712 I

INTERNALS UPPER PLENUM

1251080t 0 12610602 1a13• 0 0.0 0.0 1.0 1 0.0 0.0 1.0 2

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12151000 I 6 13161100 0 I 13161101 5 .1350 13161201 4 6 13151301 0.0 6 13151401 540. 6 13151501 316000000 0 13I51601 -937 0 13151701 0 0 13161801 0 0

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13153000 5 6 13153100 0 1 13153101 6 .2248 13153201 4 S 13163301 0.0 5 13153401 640. 6 13163501 315030000 10000 13153502 315070000 0 13153601 -997 0 13153602 -997 0 13153701 0 0 13153601 0 0 13153•02 0 0

13164000 I 6 13154100 0 I 1313,4101 5 .1620

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: INTACT LOOP PIPING

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11002000 2 6 11002100 0 1 11002101 5 .2030 11002201 4 • 11002301 0.0 5 11002401 540. 6 11002501 115020000 0 11002502 111 610000 0 11002601 -.99 0 11002602 -999 0

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: PRESSMIZERH4EAT STRUCTURES

14151000 1 1 1 I ldl81100 0 1

14151101 5 .0762 14111201 5 5 1411.301 0.0 5

14151401 518. . 14151501 415010000 0 1 I 14151601 -99H 0 3949 1 14161701 0 0 0 0 14151601 0 0.0 0.0 0.0 14112000 7 6 2 I 14152100 0 1 14152101 5 .49911 14152201 S $

0.0

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1

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8 STEAN CENERATOR P1i-SEC NEAT STNJC1$tfs

SSTEAM CENERATOA TIMING (INCL. HALF THE W SIHET) 8

1006000 6 8 2 1 0.0051054 10060100 0 I 10060101 7 0.006341894 10060201 6 7 10060301 0.0 7 10060401 540.0 a 10060601 511010000 0 I 157..8. 1 10060602 517020000 0 1 I 1310.32 2 10060603 617030000 0 1 I 1682.27 3 10060604 617030000 a I 1 1562.27 4 1006060S 0 17020000 0 ! 1 1310.32 5 10060606 5170l0000 0 I I 1579.62 a 1006050t 115040000 0 I I 1579.60 I 10060•O2 115050000 0 I I 1310.32 2 I-4

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10060503 115060000 0 1 I 1582.37 

2 10060504 115070000 0 I I 1582.27 4

10060505 116080000 0 I I 1310.32 

5

10060506 115090000 0 I 1 1579.69 6 10060701 0 . 0 0 a 10060801 0 0 0 0 

6 10060901 0 0 0 0 6

HEAT STRUCTURE THIERMAAL PIOPERTY DATA 

8

;0100100 T9L'FCTN I S U J02

20100200 TOL/FCTN I I , CAP

20100300 TBL/FCTN I I 

R

20100400 S-STEEL 20100500 C-STEEL

20100600 T8L/FCTH I 1 * INCONEL 600

* THEI•MAL CONOCTIVITY 002

20100101 366.45 7.7796 449.01 6.6267 523.15 5.7624

20100102 616.48 4.6228 699.82 4.6332 783.15 422.13

20100103 866.48 3.8803 949.$2 3.5965 1033.16 3.3576

20100104 1088.71 3.1561 1199.62 2.9838 1283.15 2.8367

20100105 1366.48 2.7138 1449.02 2.6082 1533.32 2.5217

20100106 1616.48 2.4490 1699.82 2.3919 1977.59 2.2698

20100107 2255.37 2.3071 2533.15 2.4334 2010.53 2.6•19

20100108 3088.71 2.9942

* VOLYIWTRIC NEAT CAPACITY U02

20100151 273.15 2.310466 323.15 2.572066 373.15 2.746466

20100152 473.15 2.9207E6 673.15 3.1307E6 1373.15 3.443856

20100153 1773.15 3.531066 1973.15 3.7926E6 2173.15 4.2285E6 20100154 2373.15 4.8824E6 2673.15 6.015556 2773.15 6.3210E6

20100155 2873.15 .682556 2973.15 6.7133E6 3113.15 6.800566

20100156 4699.82 6.6005E6

* TH6*RAt CO•I4UCTIVITY ZR

20100301 273.1S 9.5744 473.15 12.0044 673.15 14.0051

20100302 873.15 17.0079 1073.15 19.0087 1273.15 22.0098

20100303 1473.15 25.0109 1673.15 30.0127 1673.15 36.0149 20100304 2073.15 44.0178 2273.65 55.0225 2473.16 60.0203

• VOLVIWETRIC HEAT CAPACITY ZR

20100351 255.37 1.9041E6 1077.69 2.3122E6 1185.923 5.7124E6

20100352 1248.43 2.311666 2199.82 2.3122E6

THER6MAL CONDUCTIVITY CAP

20100201 273.15 0.14

20100202 590.0 0.24 20100203 810.0 0.29

:0100204 1090.0 0.36 ?010020S 1370.0 0.42

!0100206 3260.0 0.75

0

* THERM4AL cOHOUCTIV TY INCONEL 600

20100601 366.5 13.85 20100602 477.6 15.92

20100603 588.7 18.17 20100604 700.0 20.42 20100605 810.9 22.50 20100606 922.0 24.92 20100607 1033.2 26.83 20100608 1144.3 29.42 20100609 t477.6 36.06

* VOLUMETR1C HEAT CAPACITY GAP

20100251 273.15 5.4 20100252 3260.0 6.4

• VOLUMETRIC HEAT CAPACITY INCONEL 600

20100651 366.5 3.90865 20100652 477.6 4.08465 20100653 588.7 4.260E5 20100654 700.0 4.436E5 20100656 810.9 4.66565 20100657 $22.0 4.92965 20100658 1033.2 5.10565 20100659 1477.6 5.7276S

s HEAT STRUCTURE GENERAL TABLES.

20299900 TEMP 20299901 0.0 305.

20299800 TIAl 501 20299801 -I. 614.7 20299802 0.0 305.

20299700 TEMP 501 20299701 -1. 558. 20299702 0.0 305.

20294900 KTC-T

20294901 0.0 20. • 260 KS $5 SJURROUHNINGS HEAT LOSS

**.**.R*o oS *S***o* oS4.*o *S*888*.,*8*o*oeo*ooeSe *o S ooeo*SSs*R ee*8

• POWER

20290000 POWER 20290001 0.0 0.0 20290002 1000.0 0.0

* )**o****oe*•4o4**oo**S****e*,,******e*****8******4*e***S**S*S*oSS

* PUMP DATA

:.SINGLE PHASE HEAO CURVES

cnJ

C') H

I-I

tiz

Hi

wo t.MED CUM HO. I

1351100 I 1 1351101 0.000000C400 I.403600E#00 1351102 1.906100OE-01 1.363O6OE400 1351103 3.896300E-01 1. 318600tE00 1351104 5.9396005-01 1.232806E*00 1351105 7.902000-01 I. 133600E#00 1351106 1.OOOOOOEOO I.00000OE400

* HEAD CURVE NO. 

2

1351200 1 2 1351201 O.000000E*00 -6. 70000OE-01 1351202 2.O000000601 -5.0000OOE-Ol 1351203 4.00006OE-I .-2.S00000E-01 1351204 5.7554006-O1 0.0OOOOE*O 1351205 7.443206OE-l 2.5830OOE-OI 1351206 7.7340OOE-01 3.778000[-01 1351207 6.631300E-01 6. 3260OOE-01 1351208 1.OOOOOOE400 I.000OOE00.

* HEAD CURVE NO. 

3

1351300 1 3 1351301 -.1.000000600 2.4722006500 1351302 -8.057400-C01 2.0474006E00 13512303 -6.0690OOE-01 i.831000E00 1351304 --4.0683006-O1 I 624000E600 1351305 -2.0017106-01 1.4705005*00 1351306 O.OOOOOOE*00 1.4036006*00

* HDCURVE NO. 4

1351400 I 4 1351401 -1.000000E00 2.4722006800 1351402 -8.2297005-01 1.996500E600 1351403 -6.3332OOE-01 l. 589700* 00

1351404 -4.5534OOE-01 1.3276OOE#OO 1351405 -2.7109000-01 1. 1 94SO0E6OO 1351406 -I .7716OOE-01 1.06050OE400 1351407 -9.0730OOE-02 I.0156006E00 1351406 0.000000E*00 .3427906-01

* HEAD CURVE NO. 

6

1351500 f 5 1351501 0.0000006.00 2. 000E0-01 1351502 2.OO00OE-01 2.8000006.-0 1351503 4.000000--01 3.40000OE01 1351504 4.I180OOE-Ol 2.768000E-01 1351605 5.976300E-01 4.68400OE-01 1351506 7.934670E-01 6.992000E-Ol 1351607 l.O000000E00 1.0000006400

SHEAD CURVE NO. 

6

351600 1 S 1351601 O. 0OOOOO. 00 9.3427906-Cl 1351602 9.1099O0-02 9.122900E-E0 1351603 :.,65090.-01 *.968000E-01 1351604 2.71762O-0I1 3.7500E*01 1361605 4.5587206-01 6.4330006-01 1351606 5.744060E-01 N.35500'6-01

Ia60

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!-

If 0

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0o

,:pi

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1351607 7.4057606-01 8.4660005-Ol 1351606 7.66619E0-01 6.4690006-01 1351609 0.7147105-01 8.63800OE-01 1351610 I4.0000000*400 I. .0000)E0.00

HEAD CUWVE NO. 

7

1351700 I 

7 1351701 -1.0000006.00 -I.O00000.E+O0

1351702 8.OOOOOOE-Ol -6.300000-01 1351703 -6:.000OOOE-01 -3.00000E-01 1351704 -4.0OOOOOE-01 -5. 00000E-02 1351705 -2.000000E-01 I.5000006-01 1351706 0. 000000E*0 2. 50000GEO01

M, HEAD WAVE No0. 8a

1351800 1 

8 1351801 --. 000000-01 -1.0700000E-00

1351603 -6.000000E-O1 -9. 500000E-01 1351804 -4.0O0000)-Ol -8.600006E-01 1351605 -2.0000OO4-O1 -8.0000OOE-01 1351806 0.0O00000.00 -6.7000006-01

* SINGLE PHASE TORQ•UE DATA 

•

*TOROUE CURVE NO. * 

S

1351900 2 

1 1351901 0.0000006.00 6.0320004-01 1351902 1.930000E-01 6.3250OCE-01 1355903 3.9300OOE-01 7.3690001-Ol 1351904 5.8552006.02 6.3310006-01 1351905 7.9782OO-0- 9.2290ooE-01 1351906 1.000000100 I. OOOO0O06. *..*oo***O*O*55*9* *****W 66*S6**s*se**4**.8868888..*5SSSS8S4S

* TORO.E CURVE NO. 2 

S

1352000 2 

2 1352001 0.OOOOOE*100 -6.7000006-01

1352002 4.0.00.0_-OI -2.50OOOO-01 2352003 5.0000006-01 1.500OOE-OI 1352004 7.372550E-01 5.2658606-01 1352005 7.680490E-01 6.0659406.01 1352006 8.672300E-01 7.4366005-01 1352007 1.0000006.00 1.000000.E00 *.*9*996*455*******4**5*****e6***ss**;55*8*56*855*S4**55**545*S*•

S. TOROUE CURVE NO. 

3

1352100 2 

3 1352101 -1.O0,000OE0.0 1.984300E.00 1352102 -8.0096006-01 1.394000E.00

1352103 -6.063800E-01 1.0975o.OE00 '352104 -4.06866OE-01 8.2200006-01 " 52105 -1.9928006-01 6.6480006-01 .52206 0.00OOOE*OO 6.032000;-01

v TOROQUE CURVE NO. 4 

•

1352200 2 

4 1352201 -1.0000006.00 1.984300E.00

2352202 -6.2234006-01 1.8308006.00

1352203 -6.33710OE-02 1.6824006.00 1352204 -4.5853006-01 1.5570OOE00 1352205 -2.670230E-01 1.4346200E#00 1352206 -1.761070E-01 1.3879006*00 1352207 -6.931000-02 1.348100.400 1352208 0.0000006.00 1.2336106*00

* TORUE CURVE 040. 5 

•

1352300 2 

5 1352301 0. OOOOOE 00 -4.5000006-0I 1352302 4.000000-02 -2.50OOOO1-01 1352303 6.00OOEI-0 0.000000E.00 1352304 1. 0000OOE.00 3.569000E-01

* TORQUE CURVE NO. 

6

1352400 2 

6 1352401 O.00000E4600 1.2336106*00 1352402 9.064300E-02 1.1965006.00 1352403 I.885690E-01 1.1096006.00 1352404 2.7347006-01 1.0416006,00 1352405 4.586690E-0 I .9580001[-01 1352406 5.74480OE-01 7.807000E-01 1352407 7.3516006-O1 6.1340OOE-01 1352408 7.6952OOE-01 5.8490OOE-01 1352409 0.700570E-01 4.8770OOE-01 2352410 I. 0000OE6.00 3. $69000-O01

e TOROUE CURVE NO. 7 

0

1352S00 2 

7 1352501 -1.0000006E00 -1.0OOOOOOEOO 1352502 -3.O6OOOOE-Ol -9.000000E-01 1352503 -2.000000E-01 -5.000000E-Ol 1352504 0.00000E600 -4.5000006-01

F (OR TORUE CUVE NO. 

6

13S7600 2 

6 1352601 -1 . 000000.E00 -1.000000E#00

1352602 -2.5 OOO0-01 -9.000000-lE0 1352603 -8.0000006-02 -6.0000006-01 1352604 0.0000006.00 -6.7000006--1

000*** ***m$o10 *01*1**•4*44o*00****43*444

o TWO 

- PHASE MJLTIPLIER DATA

* HEAD WURVE

2353000 

0 1353001 0.0OOOE,0600 0.00000E.00 1353002 2.000006E-02 2.000006E-02 1353003 6.OOOOOOE-02 5.0000006-02 1353004 l.OO0000E-0I 1.0000006-Ol 1353005 2.0000006-01 4.600000E-01

1353006 2.40OOOOO-01 6.00OOOOE-02 1353007 3.OOOO -01 9.6OOOOOE-02 1353008 4.0000OOE-01 9.800006E-01 1353009 6.00000OE-01 8.7OOOOE-01I 1353010 8.0OO0006-01 9.0000OOE-01 1353011 9. 00000O-01 8.OOOOOOE-Ol 1353012 9.6000016-01 5.0000006-Ol 1353013 1.0000OO0e00 0.000000E.00

En

1-3

tdaH

*TORQUE CURAVE

N

1353100 

0 1353101 O.000000.E00 0.000006E.00 1353102 1.2500002-01 7.0OOOOO-02 1353103 1.650000E-01 2.250000E-01 1353104 2.4000OE-01 5.6000. E-01 1353105 8.0000006-01 5.6000006-02 1353106 9.60000O--01 4. S00000-01 1353107 I. 0000006.00 0.0000006E00

POW 2-PHASE DIFFERENCE DATA

Q, HEAM WARVE NO. 

I

2354100 I 

I 1354101 0. OOOOOE0 0 06000.OOOE00 1354102 I.000000E-01 8.3000OOE-02 1354103 2.0000004-01 1.O9OOOOE.O0 1364104 6.0OOO0E-01 1.020000E+00 1354105 7.0000OOE-01 1.010000E.00 1354106 9.OOOOOE-01 9.400000E-O1 1354107 I. 000000400 2.000000E*O0 *...S.S.16....s4s.....**5**64,...6....SSS.S...,44...S44..,.4.4..

* HEAD WARVE 810. 

2

1354200 1 

2 1354201 0.00OOOOE.00 O.OOOOOOE600 1354202 1.0000OOE-01 -4.0000006-02 1354203 2.OOOOOE-Ol 0.0OOOOO.00 1354204 3.000000E-01 1.0000OOE-01

1354205 4.0000006-01 2.1000OOE-01 1354206 8.0000006-Ol 6.7000005-02 1364207 9.OOOOO1-01 6.00OOOOE-01 1354208 I.OOOOOOE.00 1.00OOOE400

*HEAD CURVE NO. 35

2354300 1 

3 1354301 -1. OOOE0O0 -1.260000.E00 1354302 -. 000OOOE6-Ol -1.240oooE.00 1354303 -8.0OOOOO-O -1.7700006+00 1354304 -7.0OOOOO-01 -2.360000E*00 1354305 -6.00000062E- -2.7900006.00 1354306 -5.0OOOOOE-01 -2.9200006E00 1354307 -4.0000006-01 -2.6700OOE600 1354308 -2.5000006-01 -I.690o000*00 1354309 -1.0000006-01 -S.0OOOOO-02l 1354310 O.0O000.00 0.0000006.E00

s HEAD WARVE NO. 46

1354400 I 

4 1354401 -I.0000006E00 -1.160000E+00 1354402 -9.0oo0006-Ol -7.8000OO-0I1 1354403 -8.0000006-01 -5.00000OE-01 1354404 -7.000000E-O1 -3.100000E-O0 1354405 -6.000000E-Ol -1.70000O0-01 1354406 -5. 0OOO0 1 -a OO.OOOE-02 1354407 -3.5OO0006-Ol 0.0000006.00 1354406 -2.0000006-Ol 5.0000006-02

1354409 -1.0OOOOO-O B 

. 00000oo -02

to

00

(.3C) W K)

Pa

(D

:j

EL
1354410 0. 0000006.00 I.1000OOE-01

*HE~AD CURVE NO. 5

1354500 1 S 1354501 O.00OOO.OO 0.0OOOOE-00 1354502 2.OOOOOOE-01 -3.4000OOEO-O 1354503 4.0000006-O -6.5000OE-O1 1354504 6. OOOOOO-1O -9.3000006-01 1354505 8. 000006-O -I. 190000 .00 1354506 I .000000E.00 -l .4700006'400 *4*#4*S*..9 4•.* 444 ........ .............. 444 4*4 * 44, ...... 44 444494

*HEAD CURVE NO. 6

1354600 1 6 1354601 O.O0OOO0E00.00 1.1O OOE-0I 1354602 1.000OOE-01 1.3000OOE-01 1354603 2.5OOOOOE-01 1.5000006-01 1354604 4.000000E-01 1.3000OOE-01 1354605 5.000000E-O1 OOOOOOE-02 1354606 6.000000E 01 -4. OOOOOE-02 1354607 7.000OOE-01 -2.300000E-01 1354608 8.0 O E-01 -5.100000E-O1 1354609 9.OOOOOOE 01 -9.10000F6-01 1354610 4*44*4e* .0OO000006 -1.4700006e00 49 *.4 4*• ..... 44*04 444 9 4.4............449,**,*44**94*494ee

I HEAD CURVE NO. 7.

1354700 1 7 1354701 -1.0000006.00 O.OOOOOE00 1354702 0.0000006.00 0.000 06E00 4***.. 44 4 4* .4 .... 9*4*.................... 44,44449444 ....... .e4

4HEAD CURVE HO. 8

I354000 1 8

1354801 -1.000000E.00 0.OOOOOEO00 354802 0.000000E6O0 0.000000.E00

, TOROUE CURVE NO. I

1354900 2

1354901 0. O0OOO0600 6.032000E-01 1354902 1. 930OOO-01 6.325OO-01 ,354903 3.930000E-01 7.369000E-01 '54904 5.955200E-01 8.3310O-01 1:549OS 7.978200E-01 9.229000E-01 1354906 1.000000O.00

7IORUE CURVE NO. 2

1355000 2 2 .35500I O.OOOOOE.00 -6.700000E-01 1355002 4.000006-O1 -2.500000-01

1355003 5.OOOOOOE-01 1.SOOOOE-01 1355004 7.37255OE-01 5.265660E-01 •135S005 7.680490E-01 6.065940E-01 1355006 8. 672300E-01 7.4366DO6-01 "1355007 1.OOO006oO 1.0000006,00

TOROUE CURVE NO. 3 6

t.5 I00 2 3

.. 510I -1.0000OE.00 1.9643OOE00

't,5102 -8.0096OOo-01 . 3940006.00 355103 -6.0638OO-01 I.0925OO6.00

135S104 -4.0666006-O1 8.2200006-01 1355105 -1.9926006-01 6.6480OOE-01 1355106 0.000000600 6.032000E-01

* TOROUE CURVE NO. 4 6

1355200 2 4 1355201 -I.000000400 1.9643100600 1355202 -8.22340O6-01 1.8308OOE600 1355203 -6.337100E-01 1.682400.00 1355204 -4.566300E-01 I.557000E.00 1355205 -2.670230E-01 1.436200*00 1355206 -1.761070E-01 1.3679006.00 1355207 -8. 931000E-02 1.348100E00 1355206 O.OOOOOE00 1.2336106E00 9eo~4.**94e*9944*99oe4499499S449**9994e49eee*44449949440*44e***44*

* TOROJE CURVE NO. 5 S

1355300 2 • 1355301 o.OO00OOEO0 -4.60000OE-Ol 1355302 4.000000E-01 -2.500000E-01 1355303 5.000000-OlO O.OOOOOO.00 1355304 1.000000E600 3.6690OOE-O0 9* *** 494 0*9*4* 0* 0 0*4994994994*44444**4*94*4944*445

STOROUE CURVE NO. 6

13SS400 2 6 1355401 0.000000E600 1.233610E+00 1355402 9.0643006-02 1.196500E.00 1355403 1.8856906-01 1.1096OOE00 1355404 2.734700o-01 1.041600E*00 1355405 4. 86690O-01 8.958000-OI 1355406 6.744600E-01 7. 807000E-O 1355407 7.3616ooE-O1 6.1340OOE-01 1355406 7.6852006-01 6.849000E-01 1355409 8.700570E-01 4.877000EO01 1355410 I.0OOOO6OO40 3.6668000-01 *0 *#* 44*4 * * *4* * 4 44 *49944444*4**8449*99 4.54

* TOROUE CURVE NO. 7

1355500 2 7 1355501 -1.000000E#00 -1.000000E600 1355502 -3.0OOOOO-01 -9.000000E-01 1355503 -1.000000E-01 -5.0OOOOOO-01 1355504 O.O0OOOE6OO -4.5OOOOOE-01

0 TORQUE CURVE NO. 6

1355600 2 a 1355601 -1.000OOOEtOO -1.0OOOOOOO0 1355602 -2.500000OE01 -9.00000OE-01 1355603 -8.0OOOOOOO2 -8.000000E-O1 1355604 O.OO0000E600 -6.700000-o01

44444449444 4444400*4444444*44t444444#44444*44444404444*4*44445946••

* REACTOR KINETICS S

94...4*9d4~*9.*.40044444444*.*.49944499e444e4e.e494o49o*99**94*649

* POINT KINETICS 0

30000000 POINT 30000001 GCM4-AC 50.06 0. 371.875

* DELAYED NEUTRON CO14STANTS

0000101 0.042 2.01 30000102 0.1150 1.14 30000103 0.3950 3.301 30000104 0.1960 0.301 30000105 0.2190 0.305 30000106 0.0330 0.0124

*POWER HISTORY6

30000401 25.E.6 30. HR 30000402 60.0E.6 69. HR *4644444444*44,4 .... ... .,.,.. 4,... .... ... 4444,.... .

*REACTIVITY CURVE

l0000011 609

0 MODER9ATOR DENSITY REACTIVITY TABLE

30000501 0.8125 -3.4 30000502 0.875 -1.6 30000503 0.6375 -0.3 30000504 1.0 1.0 30000505 1.0625 2.2 30000506 1.125 3.1 30000507 1.1875 4.0 30000506 1.25 4.9 94:44 9*:494 44 94:4 444 ::9...4 4.4...,..,. . ..... .....4. .... :4

*DOPPLER REACTIVITY TABLE6

30000601 255. 1.5 30000602 S0o. 0.3 30000603 750. -0.7 30000604 1000. -:.6 30000605 250. -2.1 30000606 1500. -3.0 30000607 1750. -3.7 30000608 2000. -4.3 30000609 2250. -4.9 30000610 2500. -6.4 30000611 2750. -8.9 30000612 3000. -6.3

*SCRAM RO0 WORTH CURVE 609t 6

20260900 REAC-T 601 20260901 0.0 0.0 20260902 0.9 -2.9 20260903 0.2 -4.3 20260904 0.3 -4.8 20260905 0.4 -9.2 20260906 O.S -9i.9 20260907 0.6 -12.2 20260908 0.7 -12.9 20260909 0.8 -13.3 20260910 0.9 -13.6 20260911 1.0 -13.7

C

0

En

1-3

til

tlj

cl4

M

CIA

0 C
20260912 I. -12.8 20260913 1.2 -13.9 20260914 1.8 -14.0 20260915 1000. -14.0

* 6,2OERATOR DENS. FEEDBACK 6

30000701 230010000 0 0.15746 0.0 30000702 230020000 0 0.15746 0.0 30000703 230030000 0 0.15746 0.0 30000704 230040000 0 0.15746 0.0 30000705 230050000 0 0.15746 0.0 30000706 230060000 0 0.21270 0.0

* DOPPLER FEEDBAC

30000801 2300001 0 0.0170 0.0 30000602 2300002 0 0.3639 0.0 30000803 2300003 0 0.2747 0.0 30000804 2300004 0 0.2379 0.0 30000805 2300005 0 O.0976 0.0 30000806 2300006 0 0.0089 0.0

STEAM GENERATOR SECONDARY SIDE

OP OF DOWNCCMER (OUTLET OF PRIMARY SEPARATOR) 0

.44,(0000 DOl"ITOP BPRANCH • -001 I 1

0101 1.273 0.718 0.0 0.0 -90.0 -0.718 ;011A 02 4.E-5 0.7874 00 .,"J101 500010000 505000000 0.0 0.0 0.0 0100 a 8. *..C6CcCC **CCC **'***'**CC*666;**6*C6C*6686686*6*****'*86

* LON#WER SEPARATOR SECTION

.. 0000 LWR-SEP SNGLVDL 0101 1.273 0.718 0.0 0.0 -90.0 -0.719 :-41102 4.E-5 0.7874 00

F 0 INLET VOLUME 0

200 FEED-INLET BRAIJON 101 2 1 ý1*.I0 0.7525 0.518 0.0 0.0 -90.0 -0.518 l.,'.0102 4.E-5 0.10796 00 S51101 505010000 510000000 0.0 0.0 0.0 0100 -32101 510010000 515000000 0.0 0.0 0.0 0100

(PARATOR (INSIDE SHROUD. ABOVE TUBES)

i300GO0 SEPAR SEPARATR 500001 3 I 5200101 0.27671 0.718 0.0 0.0 90.0 0.719 52OO102 A.E-S 0.0 00 5201101 520010000 $25000000 0.0 2. 2. 1000 .5

5202101 520000000 505000000 0.0 S. 5. 1000 .10 5203101 619010000 620000000 0.196 0.4 0.4 1000

* BELOW MIST EXTRACTOR. ABOVE TOP OF SHROUD IN STEAM DOME a

5250000 SOTSTI ORAN4CH 5250001 1 I

5250101 .90 0.762 0.0 0.0 90.0 0.762 6250102 A.E-S 0.0 00 5251101 525010000 530000000 0.0 0.6 0.* 0100 s

* BELOW MIST EXTRACTOR. PRALLEL VOLUME

6260000 BOTSTIMMP $RANCH 5260001 2 1 6260101 .2146 0.762 0.0 0.0 -90.0 -0.762 5260102 4 .E-S 0.0 00 6261101 526010000 525000000 0.0 0.6 0.6 0103 5262101 626010000 600000000 0.0 0.0 0.0 0100 81

* MIST EXTRACTOR AND STEAM GEN OUTLET PIPE TO SCV S

6300000 STSU-PIPE PIPE 6300001 2 5300101 0.799008 I 5300102 0.04636 2 6300201 0.01365 I 6300301 0.762 1 5300302 25.074 2 6300401 0.0 2 5300601 90.0 I 6300602 0.0 2 5300001 4.E-S 0.0 2 S300901 0.4 0.4 1 5301001 00 2 5301101 0100 I 5301300 0 6301300 I

* PIPE DORWSTREAM OF SCV S

5350000 ONODINL. S8.GLVOI. 5350101 0.06557 64.44 0.0 0.0 0.0 0.0 6350102 4.E-S 0.0 00

6 AIR COOLED CON0ENSER

5400O CONOSER TMDPVOL 6400101 0.21677 17.67 0.0 0.0 0.0 0.0 6400102 4.E-5 0.02 00 5400200 2 5400207 0.0 2.0200E6 1.0 6400208 1000. 2.020016 1.0

* MAXE UP fEED STORAGE TAWE

5450000 FEEOTA.K TlDPVOL 6450101 29.61 3.048 0.0 0.0 0.0 0.0 $450102 4.6-5 0.0 00

S450200 0 0 CNTRLVAR 606 5460201 .6540C6 6.0E6 .65406E 2.785E6 .S 5450202 1.037866 6.056 1.037656 2.78566 .S

* FLOW PATH TO THE AIR COOLED CONDENSER

6550000 COACCO SNGLJUN 5650101 535010000 640000000 0.0 0.0 0.0 0100

SEHEAT STRJCTURE INPUrT DATA

$STEAM GENERATOR HEAT STRUCTIJRES

s SHROUD SECONDARY SIDE STEAM GEN1ERATOR S

15000000 3 4 2 I 0.3046 1S000100 0 I 15000101 3 0.314325 16000201 6 3 15000301 0.0 3 16000401 640.0 4 1500050t 600010000 0 1 I 0.7725 1 16000502 505010000 0 1 1 0.7726 2 "16000503 610010000 0 I I O.152 3 15000601 520010000 0 I 1 0.7725 1 16000602 619020000 0 1 1 0.7725 2 15000603 519010000 0 I I 0.152 3 16000701 0 0 0 0 3 15000801 0 0.0 0.0 0.0 3 16000901 0 0.0 0.0 0.0 3 15160000 4 4 2 0 0.6445 15160100 0 I 15150101 2 0.6572 16160201 5 3 15160301 0.0 3 16160401 540.0 4

15150501 510010000 0 1 1 0.152 1 1,150502 515010000 10000 1 I 0.7113 4 tS160601 619010000 0 1 I 0.162 I 15160602 517030000 -10000 1 1 0.:7113 4 15150701 0 0 0 0 4 15150801 0 0.0 0.0 0.0 4 51650901 0 0.0 0.0 0.0 4

<nC-,

tItij

C>L.i

I-

'-

z

-J4

CO

60S VE[SSEL VALL - SURROUND ING S

1 6050000 5 4 2 16050100 0 1 15050101 3 .73512 16050201 S 3 15050301 0.0 3 15050401 540. 4 1505051 s 505010000 0 ! 15050502 510010000 0 I 15050503 615010000 10000 I 15050601 -999 0 3949 15050602 -999 0 3949 15050603 -996 0 3949

.7112

II

I

l

l

I

.71s I .516 2 .7102 S .710 1 .616 2 .7102 5

:3j
15050701 0 0.0 0.0 0.0 5 15050801 0 0.0 0.0 0.0 6 15050901 0 0.0 0.0 0.0 5

* S.0. SECONDARY 0V,4C-60IL-RISR

* STENA GENRATOR 0OI4NCOC5R

5150000 D4C18 PIPE 5150001 3 5150101 0.23226 3 5150201 0.0 2 5150301 0.7102 3 5150401 0.0 3 5150601 -90. 3 5150701 -0.7102 3 5150801 4.E-5 0.10796 3 515090! 0.0 0.0 2

5151001 00 3 5151101 0000 2 5151300 I

: STEAM GENERATOR BOILING SECTION

5170000 8ILSCT PIPE 5170001 3 5170101 0.27871 3 5170201 0.0 2 5170301 1.85075 3 .:|70401 0.0 3 70601 , 21.0 3 ,70701 0.7102 3 .170801 4.E-5 0.0192 3 !170901 0.0 0.0 1 u170902 0.0 0.0 2 5171001 00 3 bl71101 0000 2

5171300 0

SSTEAM GENERATOR RISER

5190000 RISER PIPE

5190001 2 5190101 0.27671 2 5190201 0.0 I 5190301 1.85075 I 5190302 0.718 2 5190401 0.0 2 5190601 i1.0 I 5190602 90.0 2 5190701 0.518 1 5190702 0.718 2 5190801 4.E-5 0.5957 1 8190802 4.6-S 0.0 2 5190901 0.0 0.0 I 519100 1 00 2 5191101 0000 I 5181300 0

* SO DOHCOWR TO BOILING SECTION. VALVE fOR RECIRCULATION RATIO

5160000 0W9O0IL VALVE .160101 515010000 617000000 .232 I. 1. 0100 5160201 I 130.7 0.0 0.0 6160300 SRVVLV

5160301 216

* So BOILING SECTION TO RISER

6180000 BOILRSR SNGLJUI

5180101 517010000 619000000 0.0 0.0 0.0 0000

••*•5*5**ose**•5*5S•***•*555*ssssss**s*ssss4eee*••*..**ss*ss••*s••

*BROKEN LOOP

8 REACTOR VESSEL BROKEN LOOP HOT LEO

3000000 RV13LHL BAOpium 3000001 2 I 3000101 0.0634 0.876 0.0 0.0 0.0 0.0 3000102 4.0E-5 0.0 00 3001101 295010000 300000000 0.0634 0.1 0.1 0102 3002101 300010000 305000000 0.0 0.1 0.1 0000

*•*5555*5*5*o**555*5;5*****e*•5**5555*5•**s*5s****•ss**e•s•*ssss••

* HOT LEG PIPE TO REFLOO ASSIST BYPASS TEE •

3050000 HLPI.AS BRNAI 3050001 1 I 3050101 0.0634 0.698 0.0 0.0 0.0 0.0 3050102 4.0E-5 0.0 00 3051101 305010000 310000000 0.0 0.06 0.05 0100

* STE,, GENERATOR SIILS6LTOR INLET S

3100000 SGSII BRANCH 3100001 2 I 3100101 0.0 1.424 0.0668 0.0 0.0 0.0 3100102 4.OE-5 0.0 00 3101101 370010000 310000000 0.0 0.0 0.0 0100 3102101 310010000 316000000 0.0 0.05 0.05 00DO

w S.C. PIPE AND PUMP SIIMJLATOR S

3150000 SGPSI PIPE '3150001 10 3150101 0.00836 2 3150102 0.100 7 3160103 0.0 S 3150104 0.00836 9 3160106 0.0525 10 3150201 0.0 2 3160202 0.0326 6 3150203 0.0 7 3150204 0.0081 a

cn

1-3

<n

H

z

~2j

H

'-3

H

N

315020S

3150301

3150302

3150303

3150304

3150305

3150306

3150307

1150308

1150309

3150310

3150401

3150402

5150403

J3150601

3150602

31SO603

3150604

315060S

3150701

3150702

3150703

3150704

315070S

3150706

3150707

3150708

3150709

3150710

3150801

3150802

3150803

3150804

3150805

3150901

3150902

3150903

3150904

3150905

3150906

3150907

3151001

3151101

3151300

0.0 9 0.4054 I 0.5265 2 0.362 3 1.692 4 1.699 5 1.692 6 0.362 7 2.671 8 1.842 9 0.667 10

0.0 7 0.081 I0

0.0 10 90. 4 0. 5 -90. 8 90. 9 0. 10

0.127 l

0.486 2 0.362 3 1.692 4 0.0 5 -1 .692 6 -0.362 7 -I .529 8

V.214 8 0.0 10 4.0E-S 0.0 3 4.0-5 0.0124 4 4.0Z-O 0.0 6 4.06-S 0.124 6

4.06-5 0.0 10 0.1 0.1 I

0.1 0.1 2 93.9 93.9 4 93.9 83.9 6 0.0 0.0 ? 4.1 4.1 a 0.4 0.4 9 00 10 0100 9 I

'.,

I5-a to

0

*BROKEN LOOP COLD0 LEG REACTOR VESSEL NOZZLE

3350000 RVNBL BRANCH 3350001 2 1 3350101 0.0634 0.7495 0.0 0.0 0.0 0.0

3350102 4.OE-S 0.0 00

3351101 290000000 335000000 0.0634 1.0 1.0 0102

3352101 335010000 340000000 0.0 0.1 0.1 0000

* CONNECTION TEE OF THE BYPASS ASSIST SYSTEM REACTOR VESSEL SIDE*

3400000 CT8ARV BRANI

3400001 1 I 3400101 0.06!4 0.69G 0.0 0.0 0.0 0.0

3400102 4.0-5 0.0 00 3401101 340010000 345000000 0.0 0.1 0.1 0000

*s***ss**•oooo*gs**s*ssee••q*8s5o5o•,e**50•••5**55••555555*•••Ol*5

z

0o

to

N3
: BYPASS ASSIST OUTLET ECC TEE COLD LEG

3450000 BAOET BRANCH 3450001 2 I 3450101 0.0634 0.274 0.0 0.0 0.0 0.0 3450102 4.OE-5 0.0 00 3451101 300010000 345000000 0.0 0.0 0.0 0100 3452101 345010000 350000000 0.0 0.0 0.0 0100

E CCC TEE OF BROKEN LOOP

3500000 ETIVCL SNGLVOL 3500101 0.0 2.0965 0.08311 0.0 0.0 0.0 3500102 4.OE-5 0.0 00

• REFLOOO ASSIST HOT LEO

3700000 RFASHL SNOLVO0. ^100101 0.0388 0.0 0.1713 0.0 90. 0.653 £700,02 4.06-5 0.0 00

5' 4*44.4**4******.*44*.4**488****848*888#4*8****4*8*8**88444448***

* VALVE JUNCTION FOR THE AABV

200~0 RBV VAL•E .:!1010 380000000 370000000 .01 1. A. 0100 3720201 1 6.28 0.0 0.0 3120300 SRWLV 3720301 372

REFLOCO ASSIST BYPASS SINGLE PIPf COLD LEG SIDE

3800000 RFASCL SNGLVOL 3800101 0.0388 0.0 0.20353 0.0 90. 0.653 3800102 4.06-5 0.0 0

* .... **4...***S***4**..*4..**..............*.s....s..

* EGG SYSTEM

O 8WST HPIS 

8

6250000 vTHmPI TS0PVOL 6250101 20.44 S.0 0.0 0.0 90.0 5.0 6250102 4.0F-6 0.0 00 6250200 3 6250201 0.0 1.05 305.0 6250202 1000.0 1.065 305.0

* HIGH PRESSURE INJECTION SYSTEM - A#8

6300000 HPIS T50PJUN 6300101 625000000 210000000 0. 0090"S 6300200 1 661 p 210010000 6300201 -1.0 0.0 0.0 0.0 6300202 0.0 0.0 0.0 0.0 6300203 0.0 .75687 0.0 0.0 6300204 .772566 .75687 0.0 0.0

6300205 8.3597T6 .31536 0.0 6300206 17.243666 .31636 0.0 0.0 0.0

*CAP ASSESSMEIT PARAMETERS

*CORE INLET FLUID DENSITY 20550100 DCOREINF MULT 1. 0.0 

1 20550101 VOIOFJ 225010000 20550102 RPIOFJ 226010000

20550200 OCOWEINO ulL E 

. 0.0 

1 20550201 VOIDGJ 225010000 20550202 RHOGJ 225010000

2050100 DENSCORIN SU1 1. 0.0 

1 20590101 0.0 1. CNTRLVAR 601 20590102 I. C*4TRLVAR 602

R00 CL.A00ING TEMPERATURE SAVE UP 20590300 CLOTEUPI MULT I. 0.0 

I 20590301 HT1TE6 230000109 20590400 CLOTEMP2 IIJLT 1. 0.0 I 20590401 HTTEMP 230000209 20S50500 CLOIEVAP3 MULT 1. 0.0 I 20590501 HTTEMP 230000309 20590600 CLOTEMP4 MULT I. 0.0 1 20590601 HTTEMP 230000409 20590?00 CLDTEMP5 MaLT I. 0.0 1 20590703 HTTEMP 230000609 20590800 CLOTEMP6 WULT 1. 0.0 1 2055080! H'TEEP 230000609

FLUID TEMPERATURE ATTHE CORE OUTLET 20550400 FLOVDIR TRIPUlIT 1. 0.0 

I 20550401 518

20550500 TOIRP MUiLT 1. 0.0 

1 20550501 CNTRLVAR S04 20550502 TES8PF 230060000

20550600 FLODIFN4 TRIPUNIT I. 0.0 

I 20550603 -516

20SS07DO TD1PM MULT I. 0.0 

I 20550701 CNTRLVAR 606 20550702 TEWPF 240010000

;0590900 TCOlOUT SUlI I. 0.0 

I 20590901 0. I. CNTRLVAR SOS 20590902 1. CNTRLVAR 607

0 CORE TEMPERATURE DIFFERENCE 20591000 .CTOIFF SUli I. 0.0 

1 20591001 0. 1. TEMPF 240010000 20591002 -I. TEMPF 225010000

* PRESS. DIFF. OVER THE CORE 20551200 COREINV SUM 1. 0.0 

1 20591201 0.0 I. P 225010000 20591202 -2.26 Rito 225010000

c=0

:nH

ti'

1',9 H

td

20591203 -I. 

P 20591204 3.31 RHO

: PRESS.OIFF. OVER THE DORINCOUER 20591300 OWIWINV SUM I. 20591301 0.0 I. P 20S51302 -I. P 20591303 .75 RHO

* VESSEL M•ASS IWUEPTOAY 20551400 VESSMSI SUM I. 20553401 0.0 .0465 R4HO 205S1402 .018 RHO 20551403 .071 'RHO 20551404 .136036 R1H0 20551405 .136036 We 20551406 .136036 RHO 20SSt40T t536036 RHO 20551408 .2664 RHO 20553409 .2923 RHO 20551410 .130 RHO 20551411 .04765S RHO 20551412 .04765S RHO 20551413 .047655 RiO 20551414 .047655 ,1HO 20551416 .047655 RHO 20SS1416 .064364 RHO

20551500 VESSMS2 SUM 1. 20551501 0.0 .00838S RIK) 205S1502 .008385 81l0 20551503 .008385 RHO 20551504 .332046 RHO 20551505 .079002 RHO 20553506 .1328 RHO 20551507 .0603 rd" 20551508 ,202752 RHO 20551509 .173728 8H0

20591400 VESSMASS 'SUM I. 20591401 0.0 I. CRT 20591402 I. CST

* OIOCIMER LIOUID LEVEL 20591500 O0O4LEV SUM I. 2051501 0.162 .106S VOl 2059502 .300 VOl 20591503 .274 Vol 20591504 .956 VOl 2059150S .958 VOl 20591506 .958 VOl 205507 .956 Vol 20591508 .360 VOl 20591509 .208 Vol

: UPPER PLENUM LIOUID LEVEL 20591600 UPLEV SUM I. 20591601 3.764 .3084 VO1 20555602 .693 VOl 20591603 .300 Vol 20591604 .3251 VOI

0 UPPER PLENUJ1 SUSCOOLING 20591900 UPSCOOL SUM 1. 20591901 0.0 1. 4T

245010000

245010000

0.0 

0 185010000

215010000

215010000

0.0

20O010000

290010000

205010000

210010000

210020000

210030000

210040000

215010000

220010000

225010000

230010000

230020000

230030000

230040000

230050000

230060000

0.0 

3 235010000

235020000

235030000

240010000

245010000

246010000

295010000

250010000

255010000

0.0 RLVAR 614 RLVAR 61S

0.0 

1

OF 200010000 5.

OF 290010000 OF 20SO10OO OF 210010000 OF 210020000 OF 210030000 OF 210040000 DF 215010000 OF 220010000 .4

0.0 

1 OF 240010000 .4

OF 245010000 OF 295010000 OF 250010000 4.

0.0 

1 TEMP 240030000

L0

I.-AI

i.,.

z

co

0t,

00

'.Jx1
10591902 -1. CNTRLVAR 909 I

* I.L. LIOUID LEVEL. FOR .66 M / LEPOE-PC-28 20553100 P31A sum I. 0.0 20553101 0.0 1. P 120010000

20553102 -. 183 P 155050000

20553103 -. 817 P 160010000

20553104 -6.475 RHOG 155010000

20553200 P318 SUM 9.81 0.0 1 20553201 0.0 1. RHOF 155010000 20553202 -I. HPJOG 15010000

20593100 LIO.IL DIV 1. 0.0 1 20593101 CNTRLVAR 532 !0593102 CNTRLVAR 631 4

, B.L. LIQUID LEVEL. FOR 4.86 U / LEPOE-OL-14

?0553300 .P32A Sum I. 0.0 1 20553301 0.0 I. P 315080000 .0553302 8.97 RHO 315080000

?US553303 -I. P 315050000

70553304 -47.87 65400 316060000

2O553400 P321 Sum 9.81 0.0 1 20553401 0.0 1. RHOF 315060000 .!0553402 -1. RHO• 315060000

2U593200 LIO19 DIV I. 0.0 1 20593201 CHTRLVAR 634

.0593202 CNTRLVAR 633

* PUMP PRESSURE DIFF. 20593600 DPPUMS6 SUM 1. 0.0 20593601 0.0 .5 P 150010000 "0593602 .5 P 145010000 .:0593603 -1. P 120010000

: BREAK ENERGY RELEASE

20553700 PRESSE MULT 1. 0.0 1

20553701 MFLORJ 805000000

20553702 P 800010000

20553800 PRESSENT DIV 1. 0.0 1

20553801 RHO 800010000 20553802 CHTRLVAR 537

20553900 BRUFFL SAULT 205.6--6 0.0 1

20553901 UFJ 805000000 20553902 VELFJ 805000000

20553903 VOIOFJ 805000000

20553904 RHOFJ 805000000

20SS4000 BRUGFL aiAT 205.0E64 0.0 1 20554001 UGJ 805000000

20554002 VELGJ 805000000

20554003 VOIDOGJ 805000000

20554004 RHOGJ 805000000

20594000 ORENRELEA SIN 1. 0.0 1 20594001 0.0 I. CNTRLVAR 539 2 FLUID INNER ENERGM 20594002 I. CHTRLVAR 540 0 STEA4 INNER ENERGY 20594003 I. €CIALVAR 530 0 POV EHTKIAPY PART

: BREAK INLET FLUID SU6COOLING

20594200 BRSUBCOOL Still I. 0.0 1 20594201 0.0 . SATTEMP 600010000

20594202 -i. TEI6PF 80001 0000

S O0 PRIM. TEMPERATURE DIFF. 20594500 SGTEDIFF SIU I. 0.0 1 20594501 0.0 I. TEI6PF 115030000

20594502 -I. TEPF 115100000

: SO PRIM. PRESSURE 0IFF. 20594600 SGPRPRS SUM I. 0.0 1 20594601 0.0 5. P 115010000

20594602 -I. P 120010000

: SO LIUID LEVEL

20594900 SGLIOLEV SUN I. 0.0 ! 20594901 -2.946 .7102 VOIDF 515010000 20594902 .7102 VOIDF 515020000

20594903 .7102 VOIDF 615030000 20594904 .518 VOIOF 510010000

20594905 .716 VOIOF 605010000

20594906 .716 VOIOF 500010000

20594907 .762 VOIOF 526010000

: SO PRIM. TO SEC. TIM' DIFFERENCE. INLET 20595200 SGPRSETD SUM 1. 0.0 1 20595201 0.0 5. TEYIPF 115030000

20595202 -1. TEMPF 515030000

: SO HEAT TRANSFER RATE

20595300 SGHTTRAHS SUM -1. 0.0 1 20595301 0.0 50.6736 HTRNA 006000100 20595302 42.0327 HTRNR 006000200 20595303 50.7563 HTRNR 006000300

20595304 60.s563 ITRNR 006000400 20595305 42.0327 HTRNR 006000500 20595306 50.6736 HTRIR 006000600

& PRESSURIZER LIQUID LEVEL 20595400 PRLIOLEV SUM 1. 0.0 1

20595401 0.0 .224 VOIDF 415010000 20595402 .403 VOIOF 415020000 20595403 .403 VOIDF 415030000

20595404 .207 VOIOF 415040000 2059S405 .207 VOIDF 415050000 20595406 .1705 VOIOF 415060000 20595407 .1705 VOIOF 415070000 20595408 .118 VOIDF 415080000

HPIS VOLYMETRIC FLOW RATE 20595800 HPISVOLF DIV 1000. 0.0 0

20595801 RHO 625010000 MFLOWJ 830000000

: MASS BALANCE. INTEGRATED FORM BREAK TIME

20555900 TRIPSO TRIPUNIT 1. 0.0 1

20555901 510

20556000 IdMSALI SUM 1. 0.0 I 20556001 0.0 I. MFLOWJ 630000000 20556002 -1 . MFLOWJ 605000000 20556003 1. UAFLOWJ 001000000

20556100 MSBAL2 MULT 1. 0.0 1 20556101 CHTRLVAR 559

20556102 CNTRLVAR 660

En

(n

t,.3

Hx

z-,

N20595900 IASSSAL INTEGRAL I. 0.0 0

20595901 CNTRLVAR 661 0

* PRIMARY COOLANT ENERGY BALANCE tPOV 1S CNSERVM) 20556200 HPISEGY hILT 5. 0.0 1

20556201 MFLOWJ 630000000 20556202 UF 5250100O0

20556300 PUEPENGY DIV 2. 0.0 I

20556301 RHO 135010000 20556302 PMPHEAD 135

: CORE HEATING OF FLUID 20556400 COREHTFL SLIM 1. 0.0 I 20556401 0. 12.234S7 HTRNR 230000101 20556402 12.23457 HTRNR 230000201 20556403 12.23457 HTRNR 230000301 20556404 12.23457 HTRNR 230000401 20556405 12.23457 HTRHR 230000501 20556406 16.52433 HTRNR 230000601

• PUMP SEAL WATER HEAT FLOW 20556500 PIMIPF MULT 1. 0.0 I 20556501 MFLOWJ 901000000 20556502 UF 910010000

* SS PRESSURE HEAT FLOW 20556600 SSPRHF IULT 1. 0.0 I 20556601 MFLOWJ 435000000 20556602 UF 405010000

20596000 PRIENBAL SUM I. 0.0 1 20596001 0.0 -1. CNTRLVAR 953 So 20596002 -I. CNTRLVAR 982 * EXTERNALS 20596003 5. CKTRLVAR 562 0 HPIS 20596004 -I. CNTRLVAR 940 * BREAK 20596005 1. CHTRLVAR 564 • CORE 20596006 1. CHTRLVAR 56 8 PUMP SEAL WATER 20596007 -1. CNiTRLVAR 566 SS PRESSURIZER

* PRIMARY HEAT LOSSES TO SUWRUNOINGS

20555100 STR-HTLI" SUM -1. 0.0 I 20555101 0.0 1.3716 NTRNR 100100I00 100 20555102 1.4579 HTRHR 100100200 • 105 20555103 1.0085 HTRNA 100100300 1110 20555104 .8309 WRI'4R 1001004006 115.1 20555105 .7229 HIRNR 100200100 115.2 20555106 1.4776 HTRNR 100400100 6 115.3 20555107 1.4776 HTRNR 100400200 0 115.10 20555108 .5585 HTRNR 100200200 511.11 20555109 .6147 HNRuNR OO100506 115.12 20555110 .4968 HTR4R 100100600 1105.13 2055511 1 6 IRNR 100100700• 120 20555112 .6806 HIRNR 100300100 6 12S 20555113 .3101 HTRNR 100300200 8 130 20555114 .3406 HTRNR 100300300 0 140 20555115 .SS7 HTRNR 100300400 0 145 20555116 .6806 HTRNR 100300500 6 155 20555117 .3101 HTRNR 1 00300600 160 20555116 .3496 HTRNR 100300700 * 170 / 1 14.322

205SS200 STR-NTL2 SUM -1. 0.0 I 20556201 0.0 .4431 HTRNR 100100600 6 150

I.,

'I

'--* co

30 M2

2:

Ito

p-a

:j

CD,
2055S202 .4988 HTRNP 100100900 . 175.1 20555203 .5469 HTRNR 100101000 0 175.2 20559204 .6254 HTRNR 100101100 S too rO555305 1.3035 HTRNR 100101200 8 165 20555206 .6687 HTRNR 335000100 8 335 20S55207 .6228 HTRIR 335000200 0 340 20555208 .6690 HTRNR 335000300 34S 20555209 1.0578 HTRNR 350100100 * 350 20555210 3.6545 HTR/dR 375000200s 380 2055521t .1312 H1T4R 315000100 • 315.1 20555212 .1704 HTRIR 315000200 * 315.2 20555213 1.9589 HTRNR 315300100 * 315.3 20555214 1.9589 HTRNR 31S300200 • 315.4 20555215 1.9589 HTRNR 315300300* 315.6 20553216 1.9589 ITRNR 319300400 0 315.6 20SSS217 .4174 HTR4R 315300500• 315.7 2055216 1.8029 HTRNR 315100100 8 315.8 20555219 .7639 HTRHR 315200100t 315.9 20556220 .9365 HTRNR 315400100• 315.10/ - 21.9

20S55300 STR-HTLW SUM -t. 0.0 I 20555301 0.0 .7616 HTRNR 300000100 8 300 20555302 .6228 H5I11R 300000200* 305 20555303 1.2705 H1TRNR 300000300 8 310 20555304 3.0792 HTRNR 375000100 370 20555305 -1.6600 HTRHR 220000101 • 220 20555306 1.7045 HTRNR 252000100 * 252 20555307 .7120 ITRHR 255000100 4 255 / -9.8506

20558200 STR-HTL SUM 1. 0.0 I 20598201 0.0 I. CHTRLVAR 551 20598202 I. CNTRLVAR 552 20598203 I. CHTRLVAR 553 S T.AREA -46.1242 M2

8' ********8*8***ee *ee4¢** *e*est**ee•€•*•et

* 0OUUNDAAY C0"ITION CONTROL

MAIN STEAM CONTROL VALVE 8*

5500000 MSFCV TMOPJUN 5500101 630010000 635000000 0.002573 9500200 I S01 6500201 -1. 0.0 27.80 0.0 5500202 0.0 0.0 27.80 0.0 * FLOW KATE FROM HUREG/CR-0247 6500203 3. 0.0 23.4 0.0 * PRE.SSURE RISE 5.57 - 6.90 IWA 5500204 6.0 0.0 15.1 0.0 * 51 CHANCE RATE ASSUMED 9S00209 9. 0.0 9.3 0.0 5500206 13.6 0.0 6.2 0.0 5500207 13.6 0.0 .181 0.0 * LEAKAGE 5500200 94.8 0.0 .181 0.0 5500209 94.8 0.0 2.89 0.0 * VALVE OPEN AT 89 5 5500210 104.8 0.0 2.65 0.0 * VALVE CLOSE AT 99 S 5500211 104.8 0.0 .181 0.0 • LEAKAGE 5500212 500. 0.0 .173 0.0 * FROM EXP. SCONOARY PRESSURE 5500213 1000. 0.0 .1•0 0.0 * LINEAR P-DEPENOENCE ASSUMED 5500214 1l00. 0.0 .136 0.0 a .120 K1,/S AT 4.5 MPA 5500215 2370. 0.0 .113 0.0

F EED WATER VALVE

5600000 FWVLV TDPJUNI 5600101 545000000 510000000 0.05 5600200 I SO5 5600201 -1. 27.80 0.0 0.0 5600202 0.0 27.80 0.0 0.0 5600203 .7 0.0 0.0 0.0 96W0203 300. 0.0 0.0 0.0

****** 21SO200 gSo AUX. FIEUWATER 2200200

5540000 AUXFTANK l906VL 2250200

5540101 3.0 10.0 0.0 0.0 0.0 0.0 3.33E-S 1.0 It 3301201

5540200 1 2301202

6540201 0.0 315.0 0.0 2301203

23301204

6480000 AUXFJUN TDPJUNl 2301205

6480101 554000000 610000000 .1 2301206 M2 5480200 1 610 S3,1201

54*0201 -1. 0.0 0.0 0.0 2351203

5480202 73.3 0.0 0.0 0.0 2400200

6480203 73.4 .SO364 0.0 0.0 2450200

5480204 1856. .50364 0.0 0.0 2460200

5480205 1657.0 0.0 0.0 0.0 2500200

2900200

• SS VOUIME STATES 2950200

3000200 1000200 3 14.6096E6 577.73 3050200 1050200 3 14.6832E6 577.23 3100200 1100200 3 14.8606E6 677.72 3151201 1151201 3 14.860756 677.71 0.0 0.0 0.0 11510

1151202 3 14.8624S6 577.71 0. 0. 0 0.0 2 3151203 1151203 3 14.7634E6 577.68 0.0 0.0 0.0 3 3151204

1151204 3 14.7603E6 573.53 0.0 0.0 0.0 4 3151205

1151205 3 14.7365(6 569.96 0.0 0.0 0.0 6 3151206

1151206 3 14.7195E6 566.28 0.0 0.0 0.0 6 3151207 1151207 3 14.7116E6 663.09 0.0 0.0 0.0 7 3151208

1151208 3 14.704656 560.77 0.0 0.0 0.0 6 3151209

1151209 3 14.6967E6 658.68 0.0 0.0 0.0 9 3151210 1151210 3 14.6968(6 558.68 0.0 0.0 0.0 10 3350200

1151211 3 14.6191(6 558.66 0.0 0.0 0.0 11 3400200 1151212 3 14.6097E6 558.65 0.0 0.0 0.0 12 3450200 1151213 3 14.6046E6 558.6S 0.0 0.0 0.0 13 3500200 1200200 3 14.6010E6 658.65 3700200

1250200 3 14.5005E6 558.64 3800200

1300200 3 14.567056 558.63 4000200

1350200 3 14.8202(8 558.78 4000200

1400200 3 15.082156 558.78 4151201

1450200 . 3 15.0878(6 558.79 4151201

1S00200 3 15.0603E6 558.83 4151203

1550200 3 14.S884(6 956.64 4151204

1600200 3 14.5679(6 558.63 4151205 1650200 3 14,8239E6 558,78 415120. 1700200 3 15.0669(6 558.87 4151207

1751201 3 15.0542(6 558.81 0.0 0.0 0.0 1 • 4151208 1751202 3 15.0473E6 958.81 0.0 0.0 0.0 2 4200200

1800200 3 15.0436(6 558.81 5000200

1650200 3 15.0417E56 S5.81 5050200

2000200 3 15.0400(6 558.82 5100200

2050200 3 15 0190(6 558.80 5100200

2101201 3 IS01716 558.80 0.0 1 5151201

2101202 3 15.023156 655.01 0.0 0.0 0.0 2 6151202 2101203 3 15.0292E6 558.81 0.0 0.0 0.0 2 5151203

2101204 3 15.03356 55.8 0.0 0.0 0.0 4 6171201

5171202 -6171203

5191201

5191202

5200200

5250200

5260200

5301201

5301202

ri)

I-n

0-3

c:

0

ti- z

ti

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15.043756

15.0464E6

15.03235(

15.0042E6

14.9994E6

14 .991(611

14.987056

14.979326

14.9737(6

14.9879E6

14.9764(6

14.9640(6

14.9512E6

14.9316(6

14.94656

14.9329S6

14.92756(

15.0404E6

14.935856

14.935986

14.935856

14.9358(6

14.9354(6

14.9331[6

14.9299(6

14.922356

14.91606

14.9223(6

14.9299(6

14.9380(6

14.9402(6

14.9357(6

15.0404E6

16.040456

16.0404(6

1I.0404E6

14.9362f6

18.0426(6

14.9131(6

14.9O92(6

14.907156

14.9052E6

14.9028(6

14.9011(6

14.9006(6

14.9004(6

14.9002(6

14.9001(6

14.6999(6

8.57031(6

5 7233E6 6.657631(6

5. 58077(6

6.58619E6

S. 5916276

5.59162E6

6.$8571(6

6.578416

6.57236f6

6.57141(6

5.57045(6

5.57011[6

6.$7011(6

5.56987(6

5.42900(6

558.82 550.82

558.62

659.98 0.0 * 0.0 0.0 566.20 0.0 0.0 0.0 2 57i.49 0.0 0.0 0.0 3 576.31 0.0 0.0 0.0 4 579.37 0.0 0.0 0.0 6 680.13 0.0 0.0 0.0 6 655.61 0.0 0.0 0.0 1 658.81 0.0 0.0 0.0 2 558.81 0.0 0.0 0.0 3 579.53

578.71

570.71

657.75 557.75

558.81

577.75

556.69

656.62

656.93

596O.0 0.0 0.0 0.0 1 658.00 0.0 0.0 0.0 2 6598.00 0.0 0.0 0.0 3

598.00 0.0 0.0 0.0 4 558.00 0.0 0.0 0.0 6 558.00 0.0 0.0 0.0 8 558.00 0.0 0.0 0.0 7 558.00 0.0 0.0 0.0 a 558.00 0.0 O.O O. ' 558.00 0.0 0.0 0.0 10

658.70

556.58

556.40

556.00

557.16

557.73

ST2.85

577.24

0.0 0.0 0.0 0.0 I 0.0 0.0 0.0 0.0 2 0.0 0.0 0.0 0.0 3 .05661 0.0 0.0 0.0 4 1. 0.0 0.0 0.0 8 I. 0.00.00.0 6 I. 0.0 0.0 0.0 7 1. 0.0 0.0 0.0. 1

I. I.

.0144

534.87

534.93 0.0 0.0 0.0 1 534.99 0.0 0.0 0.0 2 635.05 0.0 0.0 0.0 3 .044 0.0 0.0 0.0 .O95 0.0 0.0 0.0 2 .164 0.0 0.0 0.0 3 .189 0.0 0.0 0.0 1 .194 0.0 0.0 0.0 2 .348

1.0

1.0

1.0 0.0 0.0 0.0 I 1.0 0.0 0.0 0.0 2

t

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80

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5350200 2 2.03274E6 1.0 8000200 3 15.0012E6 477.00

: 35 JUNCTION STATES

1001201 483.3 0.0 0.0

1002201 483.3 0.0 : 00.

1051201 463.3 1 0.0 .0

1101201 483.3 0.0 0.0

1151301 483.3 0.0 0.0

1151302 483.3 0.0 0.0

1151303 483.3 0.0 0.0

1151304 483.3 0.0 0.0

I151305 483.3 0.0 0.0

1201201 463.3 0.0 0.0

1202201 241.6 0.0 0.0

1203201 241.6 0.0 0.0

1251201 241.6 0.0 0.0

1252201 0.0 0.0 0.0

1350201 I 241.6 0.0

1350202 1 241.6 0.0

1451201 241.6 0.0 0.0

1452201 241.6 0.0 0.0

1501201 241.6 0.0 0.0

1502201 483.3 0.0 0.0

1551201 241.6 0.0 0.0

1650201 I 241.6 0.0

1650202 I 241.6 0.0

1701201 0.0 0.0 0.0

1751301 483.3 0.0 0.0

1001201 483.3 0.0 0.0

1851201 403.3 0.0 0.0 1852201 483.3 0.0 0.0

2051201 445.1 0.0 0.0

2101301 445.1 0.0. 0.0

2101302 445.1 0.0 0.0 2151201 445.1 0.0 0.0

2152201 i.E-S 0.0 0.0

2153201 445.1 0.0* 0.0 2251201 427.7 - 0.0 0.0

2301301 427.7 0.0- 0.0

2351301 17.4 0.0 0.0

2401201 427.7 0.0. 0.0

2402201 17.4 0.0 0.0

2451201 445.1 0.0 0.0

2461201 I.E-S 0.0 0.0

2501201 -15.9S 0.0 0.0

2502201 0.0 0.0 0.0

2901201 -15.95 O.Q. 0.0

2951201 461.1 0.0; 0.0

3001201 -6.28 0. 0.0

3002201 -6.28 0 00

3051201 -6.26 0.0 0.0

3101201 -6.28 0.0 0.0

3102201 0.0 0.0 0.0 3151301 0.0 0.0 0.0 9

3351201 6.28 0.0 0.0 3352201 6.28 0.0 0.0

3401201 6.28 0.0 0.0 3451201 -6.28 0.0 0.0

3452201 0.0 0.0 0.0

2

4

7

9

12

0.0

0.0

0.0

0.0

2

3

226 CORE BYPASS / 3.6 % 6

2

291 INLET AMN. TO 0OWNCC6ER

296 INLET ANN. TO UP / 6.6 X

4001201 0.0 0.0 0.0 372 RABV / 1.3 %

4002201 0.0 0.0 0.0

4100201 I 0.0 0.0 0.0

4151301 0.0 0.0 0.0 7

4201201 0.0 0.0 0.0 0 43S SS SYSTEM PRESSURE 5001201 0.0 0.0 0.0 5101201 102.7 0.0 0.0 5102201 130.7 0.0 0.0 I SS CONTROL FOR THE RABV LECAGE / 1.3 % 6151301 130.7 0.0 0.0 1 5156302 130.7 0.0 0.0 2 20537000 RAVVERR SUM ;. 0.0 0 5160201 1 130.7 0.0 0.0 20537001 0. I. MFLOWJ 372000000 5171301 5171302 1.260 2.010 2.829 1.608 0.0 0.0 1 2 20537002 -. 013 ILOW.J 185010000

5180201 0 3.001 4.176 0.0 20537100 RADVREO hILT 1. 0.0 0 5191301 3.489 4.073 0.0 I 20537101 CHTRLVAR 370 6201201 0.0 27.80 0.0 20537102 CNTRLVAR 612 5202201 102.9 0.0 0.0 5203201 5001 102.9 27.80 0.00.0 20. 20537200 RARVW INTEGRAL -. 03 .079 0 3 .01 .99 5261201 0.0 27.80 0.0 20537201 CNTRLVAR 371 5261201 0.0 0.0 0.0 5262201 0.0 2.0 0.0 * 5301301 0.0 27.8 0.0 1 5 SS CONTROL FOR INLET hAN. TO D0wNC(ICER FLOW

550 MAIN STEAM VALVE 20528900 IAOCERR SUM 1. 0.0 0

5550201 1 0.0 27.8 0.0 20528900 -4C3.3 1. 0.0 00

• 560 FEED WATER VAi.VE 20526501 -483.3 1. FLOWJ 165010000

* 571 SG SS LEVEL *0529000 91 50S RSUE20590 IADCREO MULT I. 0.0 0 •9 SG SS PRESSURE 20529001 CHTRLVAR 289 0 0630 HPIS INJECTION 20529002 CHTRLVAR 512 ;001201 0.0 0.0 0.0 8050201 I 0.0 0.0 0.0 20529100 IADCV INTEGRAL -. 06 .384 0 3 .01 .99 * 901 PUP COOLMIT IPJECTION 20529101 CNTRLVAR 290

0 SS CONTROL FOR TKE CORE FLOW BYPASS 3.6 3 SS CONTROL FOR VALVE 516. RECIRCULATION RATIO - 4.7

20522400 CPERR SUM 1. 0.0 120521400 ERRS16 SU3. 1. 0.0 0

20522401 0. I.PRL SU 2260000 20521401 0. I. MFLOWJ 516000000 CO 20S22402 -. 036 MFLONJ 185010000 20521402 -4.7 WFLOWJ 560000000

20521500 RECSI6 MULT I. 0.0 0 20522500 CBPREG MJLT I. 0.0 I 20521501 CNTRLVAR 214 20522501 CNTRLVAR 224 20521502 CNTRLVAR 512 20522502 CN7TALVAR 512

20S22600 C8PV INTEGRAL -.10 .214 0 3 .01 9920521600 V516 INTEGRAL -. 1 .739 0 3 .01 .99 0

20522601 CNTRLVAR 225 20521601 CNTRLVAR 215

* SS CONTROL FOR FEED WATER ENT4ALPIY

SSS CONTROL FOR INLET Nel. TO UPPER PLENU14 FLOW / 6.6 8

20560100 SPROERR SUM 1.0 0.0 0 20529400 IAUPERR SLIM 1. 0.0 0 20560101 0. -1. MFLOWJ 560000000 20529401 0. 1. MFLOWJ 296000000 20560102 .914014 VAPGEN 500010000

20529402 I. MFLOWJ 297000000 20560103 .914014 VAPGEN 505010000 20529403 -. 066 UFLOWJ 185010000 20560104 .389795 VAPGEN 510010000

20560105 .164951 VA1"EN 515010000 20529500 JAUPREG MULT I. 0.0 0 20560108 .164951 VAPGEN 515020000 20529501 CNTRLVAR 294 20560107 .164951 VAP•EH 515030000

20529502 CNTRLVAR 512 20560108 .515823 VAPGEN 517010000

20529600 IAUPV INTEGRAL -. 06 .210 0 3 .01 99 205601092 .515823 VAPGEN S17020000 20529601 C•TRLVAR 295 20560110 .51 823 VAPGEN SI7030000 20560111 .515823 519010000 20560112 .200114 VAPCEN 519020000 20560113 .200114 VAP•EN 520010000 20560114 .685800 VAP•EN 525010000 20560115 .163678 VAPGEN 526010000 20560116 .608844 VAPGEN 530010000 020$60117 1.16210 VAPGEN S30020000

0.O60200 SENTHI SUM 1.0 0.0 1 20560201 0.0 l.0 UG 517030000

in

1-3

En

H

tdJ z

tIM

00

to)

(D

:J.

(A) x
20560202 -1. UP 517030000

20560300 SSXI WULT -1. 0.0 

0 20560301 CINTRLVAR 601

20560302 CNTRLVAR 602

20560303 CHTRLVAR M12

20560400 SSX2 MhLT 1. I. 1 I I.

20560401 UFLOWJ 660000000 4300201 .166 .IE6 576.

2056OS0 SSX3 DIV I. 0.0 0 4300202 16.E6 16.M6 576.

20560501 CNTRLVAR 604 CMTRLVAR 603

*4350000 PRVALVE VALVE 20560600 FOWENTH INTEGRAL .10 .98OES 0 3 .600E6 1.0066 4350101 405010000 430000000 0.0

20560601 CNTRLVAR 605 4350201 I 0.0 0.0 * 4350300 TAPVLV

.093

0.0 .093 0100

(1)

EnH

td

1-3

-td N

e STEAM GENERATOR SS PRESSURE

5900000 . SGSSPR T4DPVOL 5900101 .1 1.0 0.0 0.0 0.0 0.0

5900102 4.E-S 0.0 00

5900200 

2

5900201 0.0 6.5766 t.

5900202 10000. 5.67E6 1.

5910000 SCSSPRJ VALVE SlO0Ol 530000000 590000000 0.0 0.0 0.0

59102Oi 1 0.0 0.0 0.0

5910300 TRPVLV

5910303 646

SO STEADY STATE LEVEL HOLDING

5700000 SGLHOLDV TUOPVO.

5700101 .1 I. 0.0 0.0 0.0 0.0

5700102 4.6-S 0.0 00

5700200 2 0 p 505010000

5700201 4.E6 4.E6 .6

5700202 7.E6 ?.E6 .6

S710000 SGLHOLDJ TPSDPJUN 5710101 505010000 570000000 .1

5710200 1 0 CNTRLVAR S1

S71020) -10. -10. 0.0 0.0

5710202 10. 1O. 0.0 0.0

2OSS1100 SGLEVERI SUM 60. 0.0

20551I01 -. 22 I. CMTRLVAR 949

20551200 YTRP-So TRIPUIEIT 

. 0.0 2055120) -501

20551300 SGLEVER2 MXLT 1. 0.0

20551301 CNTRLVAA 511

20551302 CHTRLVAR 512

* SS SYSTEM PRESSU 

E

4300000 PRVOL TMOPVOL 43()o01 .362 .224 0.0 0.0 0.0

4300)02 4.E-S 0.0 11

4300200 3 0 p 415010000

4300 64

* EN0 OF FILE 55

0100

S**ee45*454*** 00

'4 z

50 

t

-J 00

I -j

o 00

IA

.224

0

Di

mJ
* S*o LFBR2 ess

RESTART OF LOFT CALCULATION L3-6 FROM SS RUN

- LOWI RESTART too RESTART STOY-ST 101 RUN 103 2196 t05 100. 120.

0000201 200. 1.06-6 .20 00001 25 4000 4000

SOt TIME 0 GE NULL 0 1000. L

20299700 TIP 601 20299701 -1. 30S. 20299702 0.0 305. *

SO HEAT TRANSFER RATE

20595300 • SGHTTRANS SUM -1. 0.0 1 20595301 0.0 42.03127 TRNR 006000100

20595302 42.0327 HTRNR 006000200 2059S303 42.0327 HTRNR 006000300

20595304 8.7237 HTRNR 006000400

2059530S 8.7237 HTRNR 006000500

20595306 42.0327 HTRNR 006000600

20595307 42.0327 HTRNR 006000700 20595308 42.0327 HTRNR 006000800

* STEAM GENERATOR BOILING SECTION

lt70000 BILSCT PIPE 5170001 3 5170101 0.363105 3 5170201 0.0 2 5170301 0.7102 3 $170401 0.0 3 5170601 90.0 3 S170701 0.7102 3 9170801 4.E-S 0.020 3 5170901 0.0 0.0 1 5170902 0.0 0.0 2 6171001 00 3 51t1101 0000 2 5171300 0

9370000 8ILSCT PIPE 5370OO1 3 6370101 0.363105 3 5370201 0.0 2 S370301 0.7102 3 5370401 0.0 3 5370601 90.0 3 S370701 0.7102 3 5370801 4.E-S 0.020 3 5370901 0.0 0.0 1 5370902 0.0 0.0 2 5371001 00 3 5371101 0000 2 S371300 0

* STEAM GENERATOR RISER S

5190000 RISER PIPE

5190001 2 5190101 0.72631 1 5190102 0.2787i 2 S190201 0.0 1 5190301 0.:102 I 5190302 0.718 2 6190401 0.0 2 6190601 90.0 I 6190602 90.0 2 5190701 0,:18 1 5190702 0.718 2 5190601 4.E-6 0.8957 1 5190602 4.E-6 0.0 2 5190901 0.0 0.0 I 5191O01 00 2 5191101 0000 I 5191300 0

5* S 65o5* 5,0* *5 *5*58 * 5*8 500,,* *S*4S,* S*S*S****444 **4*S44**04**4

S SO D00NCCR TO BOILING SECTION. VALVE FOR RECIRCULATIOG RATIO

9160000 EWIBOIL VALVE S160101 615010000 517000000 .116 1. 1. 0100 5160201 I 65.35 0.0 0.0 5160300 SRWVLV 5160301 216

5360000 6WNSOIL VALVE 5360101 515010000 537000000 .116 1. I. 0100 5360201 I 65.35 0.0 0.0 5360300 SRVVLV 5360301 216

* SO BOILING SECTION TO RISER

9180000 BOILRSR SNGLJUN 5180101 517010000 619000000 0.0 0.0 0.0 0000

S280000 BOILRSR SNGLJUN 5280101 537010000 519000000 0.0 0.0 0.0 0000

*..........

10060504 115060000 0 1 1 271.9S 4 10060SO5 115070000 0 I 1 271.95 6 10060506 116070000 0 I I 1310.32 6 10060507 115000000 0 I I 1310.32 7 10060508 116090000 0 I I 1310.32 6 10060701 0 0 0 0 8 10060801 0 0 0 0 a 10060901 0 0 0 0 8

S171201 2 5.59162E6 .044 0.0 0.0 0.0 1 5171202 2 6.68571E6 .095 0.0 0.0 0.0 2 6171203 2 5.57814C6 .164 0.0 0.0 0.0 3 5191201 2 5.57236E6 .189 0.0 0.0 0.0 1 9371201 2 9.59162E6 .000 0.0 0.0 0.0 5371202 2 86.571E6 .044 0.0 0.0 0.0 2 5371203 2 6.57814E6 .095 0.0 0.0 0.0 3

9191202 2 6.57141E6 .194 0.0 0.0 0.0 2

S171301 0.403 0.822 0.0 1 5171302 0.605 1.257 0.0 2 S160201 0 2.3741 4.1176 0.0 5191301 3.050 4.162 0.0 1 5371301 0.403 0.822 0.0 1 5371302 0.605 1.257 0.0 2 5200201 0 2.3741 4.1876 0.0

* SS CONTROL FOR VALVE 516. RECIRCULATION RATIO - 4.7

20521400 ERR516 SUM I. 0.0 0 00 20521401 0. 1. UFLOWJ 616000000 20521402 1. MFLOWJ 526000000 *4 20521403 -4.7 MFLOWJ 660000000

20521600 V516 INTEGRAL -. 01 .117 0 3 .01 .92 20521601 clTRIVAR 215

* FEED WATER VALVE

5600000 FwJLV TIEIAJIM 6600101 545000000 510000000 o.os 6600200 I 513 5600201 -I. 27.80 0.0 0.0 5600202 0.0 27.50 0.0 0.0 5600203 .7 0.0 0.0 0.0

5600208 3000. 0.0 0.0 0.0

v SS CONTROL FOR FEED WATER ENTHALPHY

20560100 SPRDERR SUM 1.0 0.0 0 20560101 0. -I. MFLOWJ 560000000 20560102 .914014 VAPGEN 500010000 20560103 .914014 VAPGEN 505010000 20560104 .389795 VAPOEN 510010000 20560105 .164951 VAPGEN 515010000 20560106 .164951 VAPGEN 516020000 20560107 .164951 VAPGEN 516030000 20560106 .257877 VAPGEN 517010000 20560109 .257877 VAPGEN 517020000 20560110 .297877 VAPCEN 617030000 20560111 .51523 VAPGEN 619010000 20560112 .200114 VAP-EN 519020OO0

0

cn

I-3

G-2

a

w

z

to

1-4

to

-4

to

to.

0x

* STEAM GENERATOR TUBES

I0060000 6 6 2 I 10060100 0 I 10060101 5 0.006340984

10060201 6 6 10060301 0.0 5 10060401 550.0 6 10060601 617010000 0 1 1 1310.32 10060602 517020000 0 I 1310.:2 10060603 517030000 0 . . 1310.23 10060604 519010000 0 27195 10060605 519010000 0 1 1 271.96 10060606 637030000 0 1 1310.32 10060607 537020000 0 1 1 1310.32 10060608 537010000 0 1 1210.32 10060501 115040000 0 1 1 1310.32 10060502 115050000 0 1 1 1310.32 10060503 115060000 0 I 1310.32

0.0051054

2

2

3

4

6

67

2

3
20560113 .200114 VAPGEN 520010000 

C 20560114 .685800 VAPIEN 525010000 20560115 .163670 VAPGEN 526010000 

En 20560116 .608844 VAPGEH 530010000 20560117 .257877 VAPGEN 537010000 20560118 .257877 VAPG-N 537020000 

H 20560119 .257877 VAPGEN 537030000

205600 FOWMNTh INTEGRAL .0 .,8066 0 3 .$6OE6 .lO6 20560601 CNTRLVAR 605 

: TOTAL t'd 90 DOWNCOR MASS FLOW 20594500 SGOCFLW SMU 1.0 0.0 0 20594801 0. 1. WkLOJ 616000000 20594802 UFL0WJ M. 536000000 END OF FILE 

H

H

co

cl I'

.e3

I -
e*g LFCR3 ccc * RESTART OF LoFT CALCULATION 1.3-6 FROM SS RIN

L ON00 RESTART 10 RE1START TRANSNT l01 RUN

103 

a

1O5 100. 120.

)000201 260. 1.O-6 .20 00001 28 4000 4000

*PRIMARY COOLANT PUMP I TRIP-Si1 

4

1350000 PCPI PUMP 1350101 0.0366 0.0 0.099 0.0 90.0 0.319 1350102 0

135010. 130010000 0.0 0.0 0.0 0100 1350109 140000000. 0.0 0.05 0100 1350301 0 0 0 -1 -I 511 0

1350302 369.0 0.911 0.3155 96.0 500.6 1.431 1350303 613.6 0.0 207.4 0.004 19.698 0.0 1350308 .212465 0.0 -25. 29.5 6.28 1350310 0.0 0.0 0.0

SINGLE I PHASE HEAD CURVES

* HEAD CURVE NO. I 

g 1351100 I

1351101 0.O00000E+00 1.403600E*00 1351102 1.906100E-01 1.363600E*00 1351103 3.89630OE-01 1.318600[400

1351104 5.93960OE-01 1.2328001.00 1351105 7.9020001-01 1.133600E#00 1351106 I.100000O0 I.O0000OOE00

* HEAD CURVE NO. 2 

g

1351200 1 

2 13S1201 O.O0OOO0E+OO -6.7000OOE-01 1351202 2.OOOOOO-Ol -5.0000001-Ol 1351203 4.000000E-O -2.600000E-01 1351204 5.7554001-01 0.000000.+00

13S1205 7.443200E-01 2.5830001-Ol 1351206 7.734600[-01 3.778000E-01 1351207 8.6313001-01 6.3260001-01

13S1208 1.000000E100 1.000000E.00

* HEAD CURVE NO. 3 

e

1351300 1 

3 !3S1301 -1.000000E+00 2.472200E+00

351302 -8.057400F-01 2.047400E#00 1351303 -6.0690006-01 1.831000E*O0

1351304 -4.068300O-01 1.624000WE00 1351305 -2.001710E-0I 1.4705001,00 1351306 0.*00000*1O*0* 1.•403600E#00 HEAc CR NOcecec. * g g*cc e *O ge* e see**O ec** ee**e e seeceecce * HEAD CURVE NO. A C

1351400 1 

4 1351401 -I. .0000001.0 2.472200[E00 13S1402 -:.229700[-01 1.9968001,00 13S1403 -6.333200E-01 1. 897004+00

1351404 -4.:553400E-01 1.3279001e00 1351405 -2.710900E-01 1.1949001,00 1351406 - .771600E-01 1.060500E#00 1351407 -9.0730001-02 1.0156001e00

1351408 0. OOOOOOE00 9.342790E-01

* HEAO CURVE NO. 5 

C

C

1351500 I 

6 1351501 0.O00000E0O0 2.500000E-01 1351502 2.000000E-01 2.800000E-01

1351503 4.00000O0-01 3.4000001-01 1351504 4.1180001-01 2.76800OE-01 1351505 5.9763001-01 4.5840001-01 1351506 7.9346701-01 6.992000-01

1351507 1 OOOOOEeOO 1.000000E*00

0 HEAD CURVE NO. 6 

C

g

1351600 I 

6 1351601 0.000000E*00 9.342790E-01 1351602 9.109900E-02 9.229000[-01

13S1603 1.865090E-01 8.968000E-01 1351604 2.7176201-01 8.7500OOE-01 1351605 4.5587201-01 8.4330001-01 1351606 6.744060E-01 8.3550001-01 1351607 7.405760E-01 8.4660001-01 1351608 7.6661901-01 8.4690001-01 1351609 8.7147101-01 6.8380001-01 1351610 1.0000001'00 I.0000001e00

c HEAD CURME NO. 7 

0

C

13S1700 I 7 1351701 -I.000000e=00 -I .000000E100 1351702 -8.000000E-O -6.3000001-01 1371703 -6.000000E-01 -3.000000E-01 1351704 -4.OOOOOOE-01 -5.0000OOE-02 1351705 -2.0000E0-01 I..50000OE-01 1351706 0.O00000E0,O 2.600000[-0l

c HEAD CURVE NO. 8 a

I351300 I 

I 13S1601 - .000000E*00 -1.0000001*00 1351802 -8.00000OE-01 -9.7000OO1-01 1351803 -6.OOOOOOE-01 -9.500000E-01

1311804 -4.000001E-01 -8.8000001-01 1351(0S -2.0000001-01 -8.0000001-01

1351606 0.-00000O00 -6.7000001"01

0 SINGLE PHASE TORQUE DATA ccc.. cc c cc ece eec geeccce..... * .... '" eg""8'"g'8'84'8"4"'"'1

• TOROUE CURVE NO. 1 

4

1391900 2 1 1351901 0.000000=E00 6.0320001-01

1351902 1.930000E-01 6.3250O-01

1351903 3.9300001-01 7.3690001-01

0

E~n H

tij Hxw

1351904 5.9S52006-01 I.331000=-01 13S1905 7.978200E-01 0.2290001-01 1351906 I.OOOOOOEe00 1.0000@00400

o TORQUE CURVE NO. 

2

1352000 2 

2 1352001 0.000000E*00 -6.700000[-01 1392002 4.0000OOE-01 -2.6000OO-01 1352003 6.0000001-01 I. 5000001-01 1352004 7.3725501-01 8.2565860-01 1352009 7.680490E-01 6.065940E-01 1352006 4.672300E-01 7.436600[-01 1352007 .00000010E00 1.0000001.00

cTORQUE CURVE NO. 

3

1352100 2 

3 1352101 -1.000}001E00 1.9843001400 1352102 -8.0096001-01 I..3940001E00 13S2103 -6.0638001-01 1.0975001.00

1352104 -4.068600o-01 8.2200001-01 1352105 -1.9928001-01 6.6480001-01 1352106 0.0000001.00 6.0320001-01

g TOROUE CURVE NO. 

4

C

1352200 2 

4 1392201 -1.000000E#00 1.9843001.00 1352202 -8.223400E-01 1.0308001+00 1352203 -6.3371001-01 1.682400E.00 1392204 -4.8553001-01 1.6570001.00 1352205 -2.670230E-01 1.4362001400 1352206 -1.761070E-01 1.3879001.00 1352207 -8.9310001-02 1.3481001.00 1352208 0.000000OO00 1.2336101E00

cTRQUE CURVE NO. C

1352300 2 

6 1352301 0.0000001*00 -4. 500000-01

1392302 4.0OOOOOE-01 -2.500000-o01 1362303 6.0000GOE-01 0.0000001.00 1352304 1.0000001.00 3.6690001-01

s TOROUE CURVE NO. 

6

1352400 2 

6 1352401 0.0000001,00 1.233610E400

1352402 9.0643006-02 1.1965001400 1352403 1 8856901-01 1.109600E.00

13S2404 2. 7347001=-01 1.0416001E00 1392409 4.58669012-01 8.9580001-01

1352406 6.7448001-01 7.8070001-01 1352407 7.3816001-01 6.1340006-01 13S2408 ?.689200E-01 5.8490001-01 1352409 8.700570E-01 4.877D0O-01 "1352410 1.000000E,00 3.5690001-01

g TORQUE CURVE NO. 

7

T132500 2 

" 1352501 -I o*0000001'00 -I .0000001.0o

1352502 -3.000000E-01 -9.0000001-01 1352903 -I .0000OOO-01 -6.00000O-O l

00

C)3

z3

00

I-o

Sd:j
1352504 O. O0OOOE+0O .4.500000[-Ol

* FOR TORQUE CURVE NO. a

1352600 2 8 1352601 -I. 0000006400 -I. 000006*00 1352602 -2.5000OOE-0I .9.000000E-Ol 1352603 -8.OOOOOOE-02 .6.0OO00OE-01 1352604 0.00OOOOE.00 -6 70000OE-01

* TW * TWO - P*A*S** PISASE MULTIPLI* I8JLTOPLI6R D*A*58*8*5585504 DATA 555* 8 55 **S***5654***

* HEAD CURVE

1353000 0

1353001 0.000000E+00 0.00004OE,00 1363002 1.0000005-01 7 .00000E-02 1353003 2.0000006-01 I .8000006-01 1353004 3.000006E-01 3.4000006E-0 1353005 3.5000006-01 6.000000E-01 1353006 3.7000O06-01 7. 00000E-01 1353007 4 0000006-01 7.200000E-01 1353008 .OOOOOOE-O1 7.500000S -01 1353009 6.000000-01 7,7000006-01 1353010 7.00000F-01 7.7000006-01 1353011 8.OOOOOE-0l 7.400000E-01 1353012 9.000000E-01 6.100000D-01 1353013 S. 500000-01 4.0 (W000 -01 1355014 1. 0000006O0 0.O00000E*O0 S**. 445*. 45 555550 05 54554445*555****** 5*5*445555****5*4S*5*S****

Y TOROU1 CURVE

1353100 0 1353101 0.000000E400 O:0000000E00 1353102 1.0000006-01 0. 00000E,00 1353103 2.000OOOE-01 I.OOOOOOE-0I 1353104 3.000000E-01 3.O000006-01 1353105 3.500000E-01 5.000000E-01 1353106 4.000000E-01 7.000006-01 1353107 5.000006E-01 7.600000E-01 1353108 6.O000006-01 ?.500000E-01 1353109 7.0000006-01 7.500000E-01 353110 8.0000006-01 7.500000E-01 1353111 9.000000E-01 6.0000006-Ol 1353112 1.000000E*00 0.O000000E*0

P pU.MP 2-PIASE DIFFERENC6E DATA

HEAD A CURVE 00. 1

1354100 1 1354101 0.000000E#00 1.403600E400 1354102 1.9061006-01 1.363600E*00 1354103 3.896300E-01 1.3186006400 1354104 5.9396006-01 1.2328006400 1354105 7.9020006-01 1.133600E+00 1354106 1.000000E.00 1.00000E.00

SHEAD CURVE NO. 2

1354200 1 2

1354201 O.0000006E00 -6.700006-01 1354202 2.000000,-01 -5.00000E-01 1354203 4.0G0000E-01 -2.5000OE-01 1354204 5.755400E-01 0. O00OE#0 1354205 7.4432006-01 2.5830006-01 1354208 6 . 7348000-01 3.778000E-01 1354207 8.631300E-01 6.326000E-01 1354206 1.0000OE6.00 1.000000E.00

HEAD E CURVE NO. 3

1354300 I 3 1354301 -1.000000E#00 -I *160000E#00

1354302 -9.000000E-01 -1.240000E*00 1354303 -0.0000006-01 -1.7700006E00 1354304 -7.0000006-01 -2.3600006.00 1354305 -6.000000E-01 -2.790000E.00 1354306 -5.000000E-O -2.910000E+00 1354307 -4.0000006-01 -2.6700006E00 1354300 -2.5000005-01 -1.6900006E00 1354309 -. 0000OOE,-01 -S.000006E-01 1354310 0.00000.E00 0.09000OOE.00 ***55*54*585*S*58*5*5*8555555d**5***5*S*s***4e5***4****S55*5*R5***

* HEAD CURVE NO. 4

1354400 1 4 1354401 -1.000000E+00 -I.1600006*00 1354402 -9.000000E-01 -7.80000OE-01 1354403 -8.0000001-01 -5.000000e-0O 1354404 -7.000000-E01 -3.100000E-01 1354405 -6.000000E-O1 -1.7000006-01 1354406 -S.00000E6-Ol -S.000000E-02 1354407 -3.5000006-01 0.O00000.E00 1354408 -2.0000006-01 6.0000001-02 1354409 -I.00000,6-01 8.000000E-02 1354410 0.000OOE.00 1.1000001-01 55545 4455* 5* * 54 05S5S***,0.**•***.***55* *****4 **58554505 .,4,*****

* HEAD CURVE NO. 5 8

1354500 I 6 1354605 0.0000001£00 0.000OOE.00 1354502 2. 000000-01 -3.400000E-01 1354503 4.000000E-01 -6.600000E-01 1354504 6.000006E-01 -9.3000006-01 1354505 8.0000OOE-01 -1.1900006.00 1354506 . . OO0OOOE00 -I .470000,E00

* HEAD CURVE NO. 6

1354600 1 6 1354601 0.0000006.O00 1.1000006-01 1354602 I.0000006-0I 1.30000OOE-01 1354603 2.600OOE-01 1.SOOOOOE-O 1354604 4.0000006£-0 1.3000006-01 13S4605 S.OOOOOOE-Ol 7.0000OOE-02 13S4606 6.0000006-01 -4.000000E-02 1354607 7.00000E-O01 -2.30000OE-01 1354608 8.0000OOE-01 -5.100000E-01 1354609 9.0000006-01 -9.1000001E-O 1354610 1.000000E.00 -1.470000E.00

*HEAD CURVE NO. 7

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*HEAD CURVE NO. 8

13S4800 I 8 1354801 -1.0000009400 0.0000006#00 1354802 0.O000000E.00 0. 00000000

" TOR*UE CURVE NO. I ."

1354900 2 1 1364901 O.0000006.00 6.0320006-01 1354902 1.930000E-01 6.325000E-01 1354903 3.93000O6-01 7.369000£-01 1354904 8.9552006-01 8.33100OE-01 1354903 7.978200E-01 9.2290OOE-01 1354906 1.0000006,00 . 0000OOE000

a TORQUE CURVE NO. 2

1355000 2 2 1355001 0.0000001,00 -6.700000-01 1355002 4.0000006-Ol -2.5000009-01 1355003 S.OOOOOOE-01 1.500000E-01 1355004 7.3726506-05 6.2668606£-05 1355005 7.6804906-01 6.065940£-01 1355006 8.672300E-01 7.43660OE-01 1355007 I.O00000,E0O0 I.O0006OOE0

*TOROUE CURVE NO. 3

1355100 2 3 1365101 -1.0000006400 1.9843006.00 1355102 -8.0096006-01 1.9394000E.00 1355103 -6.0638006-01 1.097500E#00 1355104 -4.06860016-01 8.2200006-01 1355105 -5.9928006-01 6.646 0 0-01 1355106 0.90000E000 6.032000E-01

*TORQUE CURVE NO. 4

5355200 2 4 1355201 -1.0000006,00 1.5643006o,0 1355202 -8.2234006-01 I.83080OE#00 1355203 -6.337100(-01 1.682400EO00 1355204 -4.5853006-01 1. 557000E*00 1355205 -2.6702306-01 i.4362006*00 1355706 -1.7610706-01 1.3879006.00 1355707 -8.9310006-02 5.3481006.00 1355208 0.OO0OOO,00 1.2336106*00

TOR•UE CURVE NO. 6

1355300 2 6 1355301 0.000000E600 -4.S00001•-01 1355302 4.000000E-01 -2.500000"01

1355303 6.0000O00-Ol 0.OO0000.E00 1355304 5055*5S0*655 1.0000E000 3.56900OE-01 'lO' 5540;••' ....... p554 ........ ....... ,..''5058*...'''

*1 TROUE CURVE NO. 6*

5365400 2 6 1355401 0.000000EO0 1.23361PE.00 1366402 9.0643006-02 1•196500E.00 136S403 5.68666E-01 5 .10W66OE600

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1355408 7.6e5200E-01 5.849000E-01 1355409 8. 700570E-01 4.877000E-01 1355410 1.OOOOOOE.00 3.56BO006E-01

* TOROUE CURVE NO. 7

236550 7 1355501 -o.000000E.0 -|.000000600 tol

1355502 -3.000000E-01 -9.000006E-O 1355503 -I.O00000E-01 -5.000000E-01

1355504 O.000000.00 -4.6000006-01

* TOROUE CURVE NO. S "1-

1355600 .2 

a 1355601 -1.000000E6.0 -1.0000006.00

1355602 -2.500000E-01 -9.000000E-01 1355603 -8.0000006-02 -8.000000E-01 1355604 0.000000E.00 -6.700000E-Ol

1350200 3 14.A19556 560.35 1350201 I 241.6 0.0 0.0 1350202 I 241.5 0.0 0.0 END M OF FILE

Io 

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STUDSVIK ENERGITEKNIK AB NP-87/128

1987-11-03

Appendix B.1 (31)

0 CORE INLET FLUID DENSITY (CNTRLYAA SO) CASE A 0 CORE INLET FLUIO DENSI T (CNIRLVAR R011 CASE I A CORE INLEt FLUID DENSITT ICNTRLYAR O l CASE C

Plot B. 1

w

0

o0 ___ "___ 

-2S0 0 230 500 750 1000 1230 1500 ITSO 2000 2230 250 i0

TIME (S)

0

0

+IC

REACTOR POWER IRKTPOV 0) CASE A REACTOR POWER NRKrPOW 0) CASE B REACtOR POWER KRKrPOW 01 CASE C PRIM. EXTERNALS HEAT ,L.0W ICNTRLYAR 9821 CASE A PRIM. EXTERNALS MEAT FLO W .CtRLVAR 982) CASE e PRIM. EXTERNAALS MEAT FLOW (CRIRLYAR 982) CASE C

Plot B. 2

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0 _______ _______ _______ _______ _______ "T

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0~~

0 -

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TIME. (S)

isoo •o 20060' 2250 2500
STUDSVIK ENERGITEKNIK AB NP-8-7/128 Appendix B.2

1987-11-03

CORE CLAD rEMPERATURE VOL. I cr'-2014-O1| ... I EXP. CORE CLAD TEMPERATURE VOL. I (CrIRLYAR 9031 CASE A

CORE CLAD CEtiPERATURE VOL. I 'CI.RLVAR 103) CASE S CORE CLAD TEM'P'ERATURE VOL. I ICYNRLYAR 903) CASE C

0

0

£t

Plot B. 3

w

(L:

0

-20 a 20 Soo 750 1000 1250 1500 17_0 2000 2250 25b

0

TIME (s)

0

0

A•

CORE CLAD fEMP[RATURE VOL. 2 (E-IF?-01 ... 1 EXP. CORE CLAD TEMIPERATURE VOL. 2 (CftRLVAR 904) CASE A CORE CLAD tEMPERAIURE VOL. 2 (CYTRLVAR 904) CASE B CORE CLAD TEMIPERATURE VOL. 2 (CRIRLVAR 904) CASE C Plot B. 4

w

CL

0,.

-250 0 250 S00 750 1000 1250 1500 1750 2000 2250 25S

TIME (S)

00
STUDSVIK ENERGITEKNIK AB NP-87/128 Appendix B.3

1987-11-03

CORE CLAD TEMPERAIURE VOL. 3 IYE-IF7-026 .. I CXP. CDORE CLAD TEIPERATURE VOL. 3 ICNTRLRAR SOS) CASE A CORE CLAD TEMPERATURE VOL. 3 (CN IRLVAR 905) CASE 8

CORE CLAD TEMPERATURC VOL. 3 (CMIRLYAR SS) CASE C

a

a

A

Plot B. 5

LIJ

CL

-250 0 250 500 750 1000 1250 1500 1150 2000 2250 250i0

TIME (S)

0

a

A.

CORE CLAD TEMPERATURE VOL. 4 (TE*2LO-D3t .. C EXP. CORE CLAD (EMPERA URC VOL. 4 ICNTRLVAR 906) CASE A CORE CLAD TErMPERATURE VOL. 4 (CNTRLVAR 9062 CASE B CORE CLAD TEMPERATURE VOL. 4 (CNTRLVAR 9062 CASE C Plot B. 6

W%

LI

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a_

1:

725o 0 250 500 750 1000 1250 1500 1750 2000 2250 250

TIME (S)

0
STUDSVIK ENERGITEKNIK AB NP-87/128

1987-11-03

Appendix B.4

0a CORE CLAD TEMPERATURE VOL. 3 (Tt-20I4-04S ... 1 EXP. CORE CLAD TEMPERATURE VOL. 5 (CNTRLYAR 9073 CASE A CORE CLAD TEMPERATURE VOL. 5 (CNIRLVAR $07) CASE B CORE CLAD TEMPERATURE VOL. 5 (CMTRLVAR 07) CASE C Plot B. 7

9

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T IME (S) I0

0

a

A

CORE CLAD TEMPERATURE VOL. G ITE-SH?-062 .. I EXP.

CORE CLAD TEMPERATURE VOL. 6 (CNTRLVAR 908) CASE A CORE CLAD TEMPERATURE VOL. 6 (CWARLVAR 908o CASE 8 CORE CLAD TEMPERATURE VOL. 6 (CNTRLYAR 908) CASE C Plot B. 8

w

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0 250 500 750 1000 1250

TIME (S)

1500 1750 2000 2250 2500
STUDSVIK ENERGITEKNIK AB NP-87/128

1987-11-03

Appendix B.5

0

a

4£

CORE OUTLETtEMPEfRATUAL C IL.IUP-00 I..' LE? COALt OU ILET I fWERAI AATEA I (CNTLYAR90910 CASR% CORAE OUJTLET TEMPERATURE ICOOTALYAR 909) CASE a CORE OUTLET LTEMPEATURE (CMTALVAR 909) CASE C Plot B. 9

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TIME (S)

1500 In50 2000 2250 2500
STUDSVIK ENERGITEKNIK AB NP-87/128

1987-11-03

Appendix B.6

0 CORE INLET MASS FLOW (CMFLOWJ 225) CASE A a COREf INLET MASS FLO W t"FLOWJ 225) CASE I A CORE 14L ! MASS FLOW (lIFLOWJ 225) CASE C

Plot B.11

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O CORE MASS INVENTORY IC NTRLVAR 932) CASE 8 & CORE MASS INVENTORY (CNfRLVAR 932) CASE C

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3000 1250

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STUDSVIK ENERGITEKNIK AB NP-87/128

1987-•1,-03

Appendix B.7

0 C0OWNC0P¶( MASS INVENTORY (CNIftLVAR 9131 CASE A O OUNCOM(R MAS IVENSCA? ICATALVAR 913, CASI A DO OMICtER MASS 2INVENITORY IC TLIAR 93) CASEC Plot B. 13

CL.

TIME (S)

0 VESSEL TOTAL MASS INVENTORY (CWTRLVAR 914) CASE A 0 VESSEL TOTAL MASS INVENTORY (CNTRLVAR 9I4I CASE 8 A VESSEL TOTAL MASS INVENTORY (CVTRLVAR 9.4) CASE C

Plot B. 14

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TIME (S)

15 00 1730 2060 22'50 25i
STUDSIVJA ENERGITEKNIK AB NP-87/128

1987-11-03

Appendix B.6

O DOWCOMER LIQUID LEVEL ILE-S;-DQ 1XPV. O DOWCOMER LIQUID LEVEL (Ck RL AR 9151 CASE A ODM'NCOMER LIQUID LEVEL (CRYRLVAR 915) CASE B 4 DOWNCOMER LIQUID LEVEL ICMIRLVAR 9131 CASE C Plot B. 15

-I

LU

TIME (S)

a UPPER PLEWUMI LIQUID LEVEL (LE-3UP-001I6 LX?. 0 UPPER PLENIUM LIQUID LEVEL (CNTRLVAR 9I61 CASE A A UPPER PLENUM LIQUID LEVEL (CNTRLVAR 916) CASE 5

* UPPER PLENUM LIQUID LEVEL (CNfRLVAR 916) CASE C Plot B. 16

-.J

data from

bubble plot

N -.

-250 0 250 500 750 1000 1250 1500 1750 2000 2250 251

TIME (S)

00
.STUDSVIK ENERGITEKNIK AB NP-87/128

1987-11-03

Appendix B.9

DOVWNCOMER INLET TEMPERATURE ITE-IST-CO3 .. CXP. 0 DOVNCOMER INLET TEMPERATURE (TEMPF 205) CASE A a DOWNCOMER INLET TEMPERATURE (TEMPF' 205) CASE 0

DOWWC0MER INLET TEMPERATURE ITEMPF 205) CASE C Plot B.17

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:-230 a 2S0 500 750 1000 12'50 1500 1750 20'00 2250 25b

TIME (S)

O0

O UPPER PLENUM TEMPERATURE (TE-IUP-0Ol ...1 EXP. 0 UPPER PLENUM TE MPERATURE (TEMPF 240) CASE A A UPPER PLENUM TEMPERATURE (TEMPF 240) CASE 8

+ UPPER PLE NUUM TEMPERATURE (TEMPF 240) CASE C Plot B. 18

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TIME (S)
STUDSVIK ENERGITEKNIK AB NP-87/128

1987-1-1-03

Appendix B.10

a

a UPPER PLENUM SUMCMOLING (SC-SUP-1021 EXP. UPPER PLEN UM SUBCOOLING ICNERLVAR 91:) CASE A UPPER PLENUM SUBCOOILING CCItRLVAR 91i) CASE B UPPER PLENUM SUSCOOLING (CWTRLYAR $19) CASE C Plot B.19

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0L

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TIME (S)
STUDSVIK ENERGITEKNIK AB NP-87/128

1987-11-03

Appendix B.11

a

a

£.

UPPER PLENUM PRESSURE (FE-IUP-OOIAI| EXF. UPPER PLECUMI PRESSURE (P 245) CASE A

UPPER PLENUM PRESSURE (P 245) CASE 8 UPPER PLENU4M PRESSURE (P 2431 CASE C Plot B.21

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In

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00

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a LOVER PLENUM PRESSURE (PE-IS?-OCIA ... ' EXP. LOWER PLENUM PRESSURE (P 223) CASE A LOWER PLENUM PRESSURE (P 2251 CASE 8 LOWER PLENUM PRESSURE (P 223) CASE C Plot B.22

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1500 1750 2000 2250 2500
STUDSVIK ENERGITEKNIK AB NP-87/i28

1987-.1.1.-03

Appendix B.12

0

0

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I.L. LOtS FLUID DENSITT (DE-FC-20SI EXP. I.1. MLO LEG FLUID DENSITY (RHO 1053 CASE A |.L. HOT LEC FLUID DENSIT 1 RHO 103S CASE 0 1.L. HOT LEG FLUID DENSItT IRHO 1053 CASE C Plot B.23

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1500 1750 2000 22501 2500
STUDSVIK ENERGITEKNIK AB NP-87/128

1987-11-03

Appendix B.13

0 ,Hot LEC MASS FLOW RATE (3FLOWJ 1101 CASE A 0 "Of LEG MASS FLOW RATE (hFLOWJ 3 03 CASE 8 A N01, LtG MASS FLOW R AE CIMFLOWJ 1103 CASE C

Plot B.25

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00
STUDSVIK ENERGITEKNIK AB NP-87/128

1987-11-03

Appendix B.14

0

0 MCI. 'OT LEC PRESSURE (PE-PC-O02l EXP. I.L. WOO LEG PRESSURE (PtlOS) CASE A

1.4. HOT LEC PRESSURE (P 105) CASE I 1.1. 1OT LEC PRESSURE (P l0) CASE C Plot B.27

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0..

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0

0 _______

C

-50 ) 250 S0o 750 1000 1250 1300 1750 2000 2250 250

TIME (S)

0 I.L. COLD LEG FLUID DENSITY (DE-PCG-IS) EXP. 0 I.L. COLD LEG FLUID DENSITY (RHO IN5) CkSE A £ I.L. COLD LEG FLUID DENSITY (RHO 18S1 CASE B 4 I.L. COLD LEG FLUID DENSITY (RHO 183) CASE C Plot B.28

so 6 250 500 730 1OO0 1250 1300 1150 2000 2250 250

.0

w.

z

0

TIME (S)
STUDSVIK ENERGITEKNIK AB NP-87/128

1987-1.1-03

Appendix B.15

a

0 COLD LEG P:UP FLUID DENSITY D-PC-3OSI ES?. COLD LEG *UMP FLUID DENSltY CR1O 115.132 CASE A COLD LEG PUMP FLUID DENSITY l Rl40 1t5,13 CASE 0 COLD LEG PUMP FLUID DENSIiTl I1O 115.13) CASE C Plot B.29

_ .1 _

-230 0 250 Soo t'50 1000 1250 150 sbo 1 ?0 2000 2250 250(

T IME (S)

0 .L. COLD LEG FLUID VENSIITY (OME-OL*IO) X

SB.L. COL LEGFUD NI• RO45 CASE S.L. COLD LEG FLUID ES T 0_ 3 CASE 9

4. B.L. COLD LEG FLUID DEWSIIT (RHO 345) CASE C Plot B.30

-250 0 230 So0 750 1000 1250 1500 1750 2000 2250 25000

TIME (S)
STUDSVIK ENERGITEKNIK AB NP-87/128 Appendix B.16

1987-11-03

I.L. LOOP SEAL. LIOUID LEVEL ILEPO;-PC-0213 EXP. l.L. LOOP SEAL LIOU1D LEVEL ICNIRLVAR I3) CASE A

I.L. LOOP SEAL LIOUID LEVEL (C TRLVAR 931) CASE 5 I.L. LOOP SEAL LIOUID LEVEL tCMIRLVAR 931) CASE C

a

0

Plot B.31

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-250 0 250 500 a 70 1000 1250 1500 I ?so 2000 2250 25(

TIME (S)

00

0 B.L. LOOP SEAL LIOUID LEVEL (CWTRLVAR :32) CASE A

0 .L. LOOP SEAL LIQUID LEVEL (C ,TRLVAR 932) CASE 8 -.L. LOOP SEAL LIOUID LEVEL lCNTRL AR 932) CASE C

Plot B.32

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L.i

TIME (S)
STUDSVIK ENERGITEKNIK AB NP-87/128

1987-A-1.i-03

Appendix B.17

0

S

*

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w

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0 I.L. COLD LEG t ESSUR E IP 20 CAS rA

I.L. COLO LEG PRESSURE (1 1203 CASE A

* I.L. COLD LEG PRESSURE (P 1203 CASE C Plot B.34

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TIME (S)
STUDSVIK ENERGITEKNIK AB NP-87/128

1987-11-03

Appendix B.18

0 8.k. COLD LEG PRESSURE IPE*8k*0Ol) [XP. 0 3,. COLD LEG PRESSURE IP 343) CASA A 8,L. COLD LEG PRESSURC (P 345) CASE I + .k. COLD LEG PRESSURE tP.345) CASE C Plot B.35

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00

TIME (S)

0 PRESS.O IF. ACROSS PUMPS (POE*PC-1OO) CX?. 0 PRESSOIFF. ACROSS PUMPS (CNfRLVAR 936) CASE A A PRESS.OIFF. ACROSS PUMPS (CMfRLVAR 936) CASE B

+ PRESS.DWF. ACROSS PUMPS (CNtRLYAR 836) CASE C Plot B.36

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STUDSVIK ENERGITEKNIK AB NP-87/128

1987-11-03

Appendix B.19

a

a

£

4

SPMEE Or PUMP I IRPE-PC-O011 EXP. S3E 0 Of PUMP I IPUMPV[L 3,33) CASE A SPEC0 Or PUMP I (PUMPY L 1353 CASE 8

SPEED Or PUMP I (PUIMPVEL 135) CASE C Plot B.37

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WqEAR FLUID DENSITY (O-PC-SO2A) EXP. S'EAK FLUIO DENSITY IRHO 300) CASE A BREAK FLU|O 0DENSIT (RHO a00) CASE B BMEAK FLUID DE NSITI (RHO 800) CASE C Plot B.38

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STUDSVIK ENERGITEKNIK AB NP-87/128

1987-1.1-03

Appendix B.20

0 SNEkKK "AS$ FLCOW RAITE tWR-PC-SI1231) g O IEAI PISS LOW RE tTFLCWJ 0S CASi A A OR AKM fASS VLOd RATE (TVLVJ S03) CASE 6 01 O.IEKM ASS fI.OW WAE (TfLOVJ 8031 CASE C Plot B.39

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Plot B.40

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1750 2000 2250 2500
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1987-11-03

Appendix B.21

0

C

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BREAK INLET TEMPERATURE ITE-PC-SOIC) E)P. BIAK INLET TEIMERATUNE (TIVF 8001 CASE A

OREAK INLET TEMPERATUR E IIEMPF 800) CASE B BREAK INL E TEMIPERATURE ICEMPF 800) CASE C Plot B.41

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0 BREAK INLET SUO C: (CNTRLVAR 9:2,) CASE A A BREAK INLET SVCJ. (C I RLVA R 9421 CASE B 4. BREAK INLET SUBC- ICNIRLYAR $42) CASE C Plot B.42

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1987-11-03

Appendix B.22

0

0 BREAK INLET PRESSURE (PE-PC-SOt) EXP. |REAK :ILET PRESSURE (P :001) CASE A BREAK INLET PRESSURE (P 8002 CASE I BREAK INLET PRESSURE tP 800) CASE C Plot B.43

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1987-11-03

Appendix B.23

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4

SC Patl. TErM. DoFr. (rT-SC-OOI - IE-SC-iO2) EXP. SC PRI. TElI. DIFF. ICNTRLVAR 943) CASE A SC PR). T[ilt. 03FF. ICISALYAR 145) CASE B

SC PRI. TMP:1. 01FF. ICITRLVAR 943) CASE C Plot B.45

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a Sc PR). SIDE PRESSURE DIFF. (POE-PC-OO2) EXP. O Sc PFR. SIDE PfESSURE D0FF. (CmIRLVAR 94$) CASE A A SC PRI. SIDE PRESSURE DIFF. (CNIRLVAR 946) CASE B + sC PRI. SIDE PRESSURE DIFF. (CMIRLVAR 146) CASE C Plot B.46

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1.987-1.1'-03

Appendix B.24

0 SC FLUID DENS|IT (RMO 5IS.03) CASE A I Sc FLUID D(WSIIT (RHO 03S.OlI CAS S a SC FLUID aENSITI (RHO 51S.031 CASE C Plot B.47

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0 SC MASS FLOW RATE (PFLOVJ SIG) CASE A

A SC MASS FLOW RATE (MFLOVJ 5161 CASE A

h SC ((ASS FLOW RAILf (ILOWJ 5A6) CASE C Plot 93.48

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1987-11-03

Appendix B.25

O SC LIOUID LEVEL ILD-PO04oOD8I EXP. a SC LIQUID LEVEL (CM RLVAR 2491 CASE A a SC LIQUID LEVEL ICNIRLVAR :49) CASE a + SC LIOUID LEVEL ICN RLVAR 54 ) CASE C Plot B.49

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O SC LIOUID IEIPERATUVE R TE-SE-OS) EXP. SSC LIQUID 1TEMPtRATURE (tIE PF 515.03) CASE A a SC LIQUID IEIPERATUR (TETIPF 515.03) CASE a + SC LIOUID TEIMPERATUOE ITEnPF 5)1.03) CASE C Plot B. 50

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STUDSVIK ENERGITEKNIK AB NP-87/128

1987-A.1.-03

Appendix B.26

a

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0

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TIME (S)
STUDSV11% JZNERGITEKNIK AB NP-87/128

1987-11-03

Appendix B.27

1 SC HEAT IRANSFER RATE (C-TRLVAR SS93 CASE A o SC HEAT IRAHSIER RATE (CNTRL AR I3) CASE B A SC HEAT IRAN$rER RAIE (C.TRLVAF 9S 3 CASE C Plot B.53

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PRESSUkIZER LIOUIO LEVEL tLI-PI39-006) EXP. PRESSURIZER LIOUID LEVEL (C3TRLVAR 954) CASE A PRESSURIZER LIOUID LEVEL ICCtRLVAR 9543 CASE B PRESSURIZER LIOU1O LEVEL (CNTRLVAR 954) CASE C Plot B.54

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1987-11-03

Appendix B.28

O PRESSURIZER LIQUID TEMP. tE-P139-020) EXP. O PRESSURIZER LICUID TEMP. ITEI9P 415.02) CASE A £ PRESSURIZER LIQUID TEMP. ITEMP 415.02) CASE S 4 PRESSURIZER LIQUID TEmP. (TNETPV 413.02) CASE C Plot B.55

TIME (S)

0

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PRESSUkIZER STEAM TEMP. ITE-PI39-01S) EXP. PRESSURIZER STEAM 1EMP. ITEMPO 4;5.07) CASE A PRESSURIZER STEAM TEMP:. TTEMPO 435.0?) CASE 8 PRESSURIZER STEAM TEMP. ITEMPO 415.07) CASE C Plot B.56

TIME (S)
STUDSVIK ENERGITEKNIK AB NP-87/128

1987-11-03

Appendix B.29

8 PRESSUR•IZER PRESSURE (PC-PC-004) EXP. O PRESSUNIZER PRESSURE (P 413.08) CASE A a PRESSURIZER PRESSURE (P 413.08) CASE 5 + PRESSURI|ZER PRESSURE (P 415.08) CASE C Plot B. 57

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TIME (S)

8 WPIS VOtTPETR1C FLOW RATE (FT-PI28-104) IXP. O wPIS VOLTMIETRIC FLOW RATE (CNTRLVAR 958) CASE A A 0915 VOLYIIETRIC FLOW RATE (CNTRLVAR 958) CASE 8 * HWIS VOLTIETRIC FLOW RATE (CMIRLVAR 958) CASE C Plot B.58

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ft I_____ I_____ _____ _____ _____ _____ _____ _____ _____ _____ _____

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TIME (S)

1300 1730 20 0 2250 2300
STUDSVIK ENERGITEKNIK AB NP-87/128

1987-.11--03

Appendix B.30

O ST"EIM IMASS BALANCE (CRNRLYAR 9S2) CASE A a SYSTM MASS SATI.AC (CNTRLVAl I55) CASE B A SSTESf MASS BM.ANCE (CrIRLVAR 559) CASE C

Plot B.59

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TIME (S)

8 COOLANT ENERYC BALANCE (CMINLYAR 9601 CASE A

0 COOLANT ENERT BALANCE (CNIRLYAR 960) CASE B a COOLANT ENERGY BALANCE (CNTRLVAR 560) CASE C

Plot B.60

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1987-11-03

Appendix B.31

a COMPUTATION CPU TIME (CPUTIME 0) CASE A . COMPUTAT ION CPU T IME CCPUT IPI 0) CAS E 3 A E04FU TATI ON CPU I IME (CPUT IME 0) CASE C Plot B. 61

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TIME (S)

1750 2000 2250 2500

O COMPUTAIION MASS ERROR (EMASS 0) CASE A O COMPUTAt ION MASS ERROR CEMASS 0) CASE 9 SC0MPUTATI0O MASS ERROR ([EMASS 0) CASE C

Plot B. 62

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STUDSVIK ENERGITEKNIK AB NP-87/128 Appendix C.1 (6)

1987-11-03

Case A

CALCULATION-TO-EXPERIMENT DATA UNCERTAINTY ANALYSIS FOR NRC/ICAP. .................. = ........................

FIRST LINE DIFFERENCE BETWEEN CALCULATED AND (AVERAGED) EXPERIMENTAL DATA AT END OF THE INTERVAL

SECOND LINE MEAN DIFFERENCE OVER THE INTERVAL

THIRD LINE MEAN SIGMA OVER THE INTERVAL (ROOT MEAN SOUARE OF THE DIFFERENCE)

- CODES - ---- TIME INTERVAL - - - -

CALC. EXP. 0.0 - 20.00 - 80.00 - 200.0 - 800.0 -. 1000. - 1500. - 2000.

C 3A - C 3X -1.32 -2.01 -1.82 -3.20 -5.42 -5.90 -11.4

-2.39 -1.47 -1.90 -2.19 -4.20 -5.44 -7.87

2.69 1.52 1.90 2.24 4.24 5.44 8.04

C 4A - C 4X -. 770 -1.27 -1.37 -2.66 -4.96 -5.24 -10.7

4.44 -1.14 -1.30 -1.83 -3.73 -4.89 -7.18

6.56 1.18 1.30 1.68 3.79 4.89 7.32

C SA - C 5X -. 240 -1.20 -1.55 -2.84 -5.34 -5.39 -10.9

2.76 -. 607 -1.42 -2.02 -3.99 -5.31 -7.34

4.24 .701 1.42 2.06 4.05 8.31 7.52

C SA - C 6X -. 570 -1.09 -1.14 -2.60 -5.24 -5.67 -11.1

3.76 -. 817 -1.18 -1.83 -3.87 -5.22 -7.53

8.87 .851 1.19 1.&8 3.94 5.22 7.69

C 7A - C 7X -1.98 -1.22 -1.50 -2.91 -5.42 -5.89 -11.4

-2.13 -1.42 -1.38 -2.00 -4.00 -5.44 -7.82

2.18 1.43 1.38 2.05 4.07 6.44 7.98

C &A - C OX -1.90 -1.46 -1.51 -3.06 -5.45 -6.29 -11.9

-2.30 -1.53 -1.49 -2.20 -4.18 -5.74 -8.25

2.36 1.53 1.49 2.25 4.24 5.74 8.41

C 9A - C 9X -3.60 -3.51 -4.32 -5.82 -8.01 -8.73 -14.1

-3.09 -3.70 -3.84 -4.55 -6.51 -7.98 -10.4

3.15 3.71 3.84 4.58 6.55 7.96 10.5

C M - C AX -. 431 .993 .556 .890E-01 -. 632E-01 -. 535 -. 437

.647 .176 .698 .116 -. 238E-01 -. 356 -. 456

1.35 .470 .733 .198 .310 .398 .489

V SA - V 8X -2.80 -4.93 -4.64 -5.62 -8.28 -8.62 -13.4

-3.08 -3.99 -5.04 -4.90 -6.81 -8.20 -10.1

3.08 4.07 5.04 4.91 6.65 8.20 10.2

V GA - V 6) -3.06 -3.03 -3.84 -5.13 -7.44 -8.02 -13.5

-1.54 -3.14 -3.38 -4.03 -5.96 -7.38 -9.79

2.13 3.15 3.38 4.05 6.00 7.38 9.92

V 7A - V 7X 6.59 3.61 3.25 3.45 2.79 2.76 3.99

7.12 5.43 3.60 3.22 3.14 2.77 3.32

7.13 5.90 3.61 3.22 3.14 2.77 3.34

V SA -'V UX -3.14 -4.86 -4.47 -5.46 -7.11 -7.23 -12.6

-3.00 -3.90 -4.72 -4.77 -6.25 -7.00 -9.17

3.01 3.94 4.73 4.79 5.26 7.00 9.29

V 9A - V OX .601 .960E-01 .135E-01 -. 107 -. 285 -. 231 -. 419 .740 .292 .626E-01 -. 3696-01 -. 196 -. 247 -. 287

.763 .425 .6586-01 .5186-01 .194 .247 .293

V M - V AX .479 -. 267E-01 -. 107 -. 252 -. 437 -. 301 -. 517

.618 .178 -. 866E-01 -. 176 -. 341 -. 367 -. 378

.633 .354 .610E-01 .182 .345 .370 .364

HLIA - HLIX -31.5 29.0 48.6 -72.4 43.7 42.0 -2.43

-16.0 2.13 56.1 -15.3 -48.9 58.2 23.8

19.2 22.6 56.6 49.3 80.2 58.6 28.1

HL2A - HLX2 -29.2 -12.0 -31.2 94.1 155. 16.1 8.95

-27.5 -21.3 -21.6 6.24 20.0 68.2 -4.46

27.7 22.0 22.2 31.1 Ill. 78.2 6.91

HL4A - HL4X -.810 a70 0. -. -1.93 -5.16 -5.64 -11.6

.651 -. 996E-01 -. 262 -1.39 -3.49 -5.09 -7.65

1.51 .212 .343 1.48 3.56 5.09 7.84

HLSA - HLSX .680 .806E-01 .2196-01 -. 114 -. 287 -. 201 -. 359

.695 .291 .698E-01 -. 6566-01 -. 203 -. 235 -. 244

.706 .421 .635E-01 .7056-01 .208 .236 .249

CLIA - CL1X -2.62 -60.3 6.02 15.5 131. 42.7 1.18

-13.7 -38.7 -16.8 17.5 70.6 76.7 11.3

16.3 45.7 26.4 20.2 79.1 79.5 16.8

CL2A - CL2X 744. 662. 586. 353. 190. 52.6 12.5

749. 700. 631. 460. 269. 114. 26.5

749. 700. 631. 466. 273. 121. 29.0

CL3A - CL3K -5.17 -2.03 4.34 167. -7.43 -15.1 -6.18

-. 318 -5.87 -1.11 94.9 114. -13.7 -11.8

2.11 7.38 7.02 176. 136. 16.4 12.4

CL4A - CL4X .252 -. 916 -1.72 -3.15 -. 385 -. 6376-01 -. 686E-01

.441 -. 666 -1.10 -3.47 -1.33 -. 217 -. 675E-01

.475 .625 1.13 3.73 1.54 .241 .685E-01

CL6A - CL6X -. 360 -2.37 -1.90 -2.49 -5.23 -5.61 -11.2

-. '409 -1.30 -2.25 -2.00 -3.74 -5.22 -7.64

.503 1.54 2.25 2.02 3.82 6.22 7.81

CL7A - CLWX .668 .105 .467E-01 -. 164 -. 367 -. 298 -. 490

.697 .279 .734E-01 -. 6726-01 -. 265 -. 321 -. 359

.710 .402 .7496-01 .964E-01 .271 .322 .364
STUDSVIK ENERGITEKNIK AB NP-87/128 Appendix C.2

1987-11-03

- COoDS - ---- TIM INTERVAL ----

CAM. E. 0.0 - 20.00 - 0.00 - 200.0 - 500.0 - 10oo. - 1600. - 2000.

CLSA - CL6X .468 -. 873E-01 -. 187 -. 316 -. 634 -. 476 -. 669

.617 .135 -. 122 -. 245 -. 395 -. 489 -. 533

•.631 .348 .125 .248 .399 .489 .536

CL9A - CLOX -8.48 -76.0 -133. -32.1 -13.3 -13.4 -18.6

-1.60 -43.6 -88.5 -71.5 -17.6 -14.0 -16.7

3.03 51.6 90.4 84.4 16.8 14.0 16.8

CLt. - CLAX 17.8 1.60 10.2 -14.9 7.60 -13.9 -16.3

14.7 -. 792 7.26 -4.67 -11.8 -12.5 -13.6

14.8 5.93 10.3 33.8 12.3 13.1 13.7

BR1A - BRIX 10.2 -32.0 79.3 180. 127. 26.3 -2.32 44.8 -23.3 14.1 101. 123. 71.6 13.9

68.3 30.7 32.2 107. 126. 75.6 18.0

SR2A - BR2X 8.81 1.17 .404 .1IIE-01 -. 236E-01 -. 471E-01 -. 334

7.26 3.54 .630 .298 .204E-01 .279 -. 696E-01 8.22 3.93 .766 .384 .179 .315 .306

RAA - SR4X -. 370 -1.82 -1.62 -2.02 -4.42 -5.26 -11.3 -10.6 -1.16 -1.85 -1.55 -3.12 -4.77 -7.43

15.3 1.34 1.86 1.57 3.21 4.77 7.63

BRSA - BR6X 4.43 2.14 .956 .942 .804 1.24 1.71

15.6 3.12 1.82 .551 .672 1.05 1.37

19.7 3.68 1.86 .661 .680 1.05 1.38

BR6A - BR6X .551 .344E-01 -. 684E-01 -. 127 -. 293 -. 262 -. 474 .781 .232 -. 374E-02 -. 100 -. 213 -. 271 -. 333 .809 .384 .267E-01 .103 .219 .271 .339

SPIA - SPIX -9.06 -. 510 -. 930 -3.46 -6.33 -6.72 -13.0

-9.22 -3.64 -. 681 -1.83 -4.50 -6.56 -9.20

9.42 4.34 .682 1.98 4.60 6.57 9.35

SP2A - SP2X -7.42 1.82 1.99 1.97 1.84 1.60 3.67

-6.67 -1.79 2.34 2.67 2.39 2.26 2.60

7.10 3.22 2.38 2.60 2.42 2.27 2.65

SP3A - SP3X -4.49 -70.6 -77.5 -18.5 -15.7 -16.2 -20.0

-1.64 -41.1 -66.4 -42.9 -14.2 -17.1 -18.2

1.79 48.9 57.5 48.8 14.3 17.1 18.2

833A - nu -. 620 -. 648 -. 678 -. 576 -. 813 -.S1i -. 626 -. 628 -.899 -. 562 -. 577 -. 566 -. 489 -. 672

.577 .600 .564 .577 .666 .489 .574

SS4A - SX 15.0 -. 940 -6.73 -6.19 -1.52 2.00 -9.52

11.4 5.88 -3.64 -7.65 -4.17 1.53 -1.72

11.8 7.91 4.09 7.67 4.48 1.96 3.63

IS33 - SS5X .101 .130 .433E-01 -. 165 -. 476 -1.33 -2.06 -. 210E-01 .125 .103 -. 662E-01 -. 268 -. 882 -1.75 .647E-01 .128 .112 .902E-01 .300 .918 1.77

S IA - S IX -24.1 .429 5.81 3.03 -5.19 -9.63 -3.34

-20.6 -9.41 3.06 6.75 -. 296 -8.09 -7.57

21.2 12.2 3.70 5.83 2.65 8.22 7.77

P IA - P IX .816E-01 .676E-01 .840E-01 .836E-01 .844E-01 .839E-01 .839E-01

.446E-01 .619E-01 .BO1E-01 .839E-01 .838E-01 .840E-01 .842E-01

.55OE-01 .626E-01 .803E-01 .839E-01 .838E-01 .940E-01 .842E-01

P 2A - P 2X -20.1 -2.15 -9.29 -34.9 -56.6 -71.6 -93.9

-12.0 -14.0 -4.86 -23.1 -46.6 -63.4 -82.0

12.9 16.8 5.28 24.2 46.8 63.5 82.2

P 3A - P 3X -19.8 2.07 5.16 -6.62 -21.6 -33.6 -45.5

-13.3 -12.2 4.12 -. 194 -14.4 -27.6 -39.4

14.0 15.9 4.29 3.53 15.0 27.8 39.5

P4A- P4X .337 -. 162E-01 -. 985E-01 -. 266 -. 442 -. 387 -. 576

.300 .179 -. 417E-01 -. 178 -. 347 -. 405 -. 442

.308 .344 .474E-01 .185 .361 .405 .446

EC1A - ECIX -. 670E-03 -. 657E-01 -. 259E-01 .198E-01 .284E-01 .718E-02 .606E-01 -. 136 .201E-03 -. 386E-01 -. 454E-02 .282E-01 .215E-01 .322E-01

.161 .636E-01 .393E-01 .134E-01 .299E-01 .2456-01 .3486-01
STUDSVIK ENERGITEKNIK AB NP-87/128 Appendix C.3

1987-11-03

Case B

CALCULATI O-TO-EXPERIMENT DATA UNCERTAINTY ANALYSIS FOR NRC/CA. -. .............................

FIRST LIKE DIFFERENCE BETWEEN CALCULATED AND (AVERAGED) EXPERIMENTAL DATA AT END OF THE INTERVAL

SECOND LINE MEAN DIFFERENCE OVER THE INTERVAL THIRD LINE MEAN 51GMA OVER THE INTERVAL (ROOT MAN SOUARE OF THE DIFFERENCE)

- CODES --.- - TIME INTERVAL ----

CALC. EXP. 0.0 - 20.00 - 80.00 - 200.0 - 600.0 - 1000. - 1600. - 2000.

C 30 - C 3X .600E-01 -1.98 -1.86 -3.43 -5.95 -4.71 -7.84 -. 206 -. 957 -1.81 -2.29 -4.92 -5.16 -5.33

1.22 1.22 1.51 2.34 4.97 5.17 5.40

C 48 - C 4X .600 -1.25 -1.42 -2.81 -5.60 -4.06 -7.13

6.57 -. 639 -1.22 -1.94 -4.46 -4.62 -4.62 8.25 .924 1.22 1.99 4.63 4.64 4.70

C 68 - C 6X 1.12 -1.18 -1.61 -2.99 -5.67 -4.20 -7.34 4.86 -.10s -1.34 -2.12 -4.72 -5.03 -4.81

5.92 .746 1.34 2.17 4.79 5.05 4.89

C 68 - C 6X .790 -1.09 -1.20 -2.77 -5.78 -4.49 -7.61 5.82 -. 320 -1.11 -1.94 -4.61 -4.96 -4.99

7.41 .708 1.11 1.99 4.69 4.96 5.06

C 78 - C 7X -. 600 -1.22 -1.66 -3.06 -5.96 -4.71 -7.85 -. 300E-01 -. 923 -1.30 -2.11 -4.73 -5.16 -5.29

.639 .964 1.31 2.16 4.81 6.17 5.37

C 8B - C OX -. s00 -1.45 -1.56 -3.21 -5.90 -5.10 -8.36

-. 199 -1.01 -1.41 -2.31 -4.91 -5.46 -5.70 .684 1.07 1.41 . 2.35 4.99 5.48 5.77

C 98 - C SX -2.24 -3.50 -4.37 -5.99 -8.54 -7.54 -10.5 -. 975 -3.21 -3.76 -4.65 -7.24 -7.70 -7.84

1.32 3.25 3.77 4.66 7.29 7.71 7.89

C AS - C AX -. 343 .977 .558 .849E-01 -. 641E-01 -.535 -. 424

.646 ,190 .693 .101 -. 483E-01 -. 357 -. 4"6 1.27 .462 .730 .189 .289 .400 .480

V S8 - V 5X -1.61 -4.91 -4.72 -6.00 -8.82 -7.43 -9.73 -1.22 -3.56 -4.96 -5.01 -7.54 -7.94 -7.65

1.25 3.76 4.96 5.03 7.59 7.95 7.59

V68- V 6X -1.64 -3.02 -3.89 -5.30 -7.98 -6.83 -9.81

.539 -2.63 -3.30 -4.13 -6.69 -7.10 -7.21

1.74 2.70 3.30 4.16 6.74 7.12 7.27

V 78 - V 7X 5.16 3.60 3.24 3.46 2.78 2.76 3.98

5.25 5.11 3.59 3.22 3.14 2.77 3.32

5.27 5.46 3.60 3.22 3.14 2.77 3.34

V 88 -.V 8X -1.80 -4.03 -4.52 -5.62 -7.64 -6.04 -8.94

-.817 -3.40 -4.64 -4.86 -6.96 -6.73 -6.61 .959 3.53 4.64 4.88 6.98 6.75 6.66

V 98 - V 9X .592 .954E-0I .750E-02 -. 123 -. 330 -. 164 -. 246 .781 .310 .898E-O1 -. 4746-01 -. 251 -. 230 -. 146 .798 .433 .745E-01 .617E-01 .269 .236 .149

V AB - V AX .469 -. 270E-01 -. 113 -. 268 -. 481 -. 224 -. 345

.658 .196 -. 494E-01 -. 186 -. 406 -. 349 -. 237 .678 .359 .574E-01 .192 .410 .360 .240

HLI0 - HLIX -34.4 28.0 47.4 -76.3 50.2 42.6 13.0

-22.0 -. 245 64.9 -15.5 -50.1 63.0 25.9

22.9 22.3 55.5 48.6 86.0 63.6 29.1

HL28 - HL2X -32.1 -14.9 -32.1 92.8 159. 19.7 10.2

-30.3 -24.3 -23.2 5.79 15.7 73.0 -3.06

30.5 24.9 23.8 31.2 116. 83.3 8.61

HL4B - NL4X .990 .20OE-0I -. 620 -2.10 -5.70 -4.45 -7.90

2.68 .433 -. 181 -1.50 -4.23 -4.81 -5.08

3.08 .574 .327 1.59 4.32 4.83 6.17

HLSB - HLSX .570 .794E-01 .137E-01 -. 130 -. 332 -. 123 -. 186

.736 .306 .621E-01 -. 9666E-01 -. 268 -. 218 -. 103 .751 .428 .871E-01 .B10E-01 .274 .226 .106

CLIO - CLIX -4.96 -61.0 6.69 7.68 137. 44.4 S.77 -17.1 -39.5 -17.5 16.0 88.7 79.8 14.7

19.4 45.6 27.7 21.0 80.4 83.8 18.6

CL28 - CL2X 742. 661. 8a6. 344. 195. 54.8 14.3

745. 699. 630. 461. 270. 117. 28.5 745. 700. 630. 467. 273. 124. 30.6

CL38 - CL3X -9.09 -2.57 3.23 175. -8.19 -14.7 -5.21 -3.96 -7.95 -1.65 68.7 101. -13.6 -11.1

4.56 8.85 7.08 121. 123. 15.3 11.0

CL48 - CLAX .286 -. 640 -1.57 -3.26 -. 370 -. 89E-'01 -. 5856-01 .479 -. 469 -. 805 -3.46 -1.44 -. 178 -. 6186-01

.512 .524 .873 3.73 1.63 .215 .529E-01

CL68 - CL6X .820 -2.36 -1.99 -2.67 -5.77 -4.42 -7.63 1.43 -. 855 -2.17 -2.12 -4.48 -4.95 -5.10 1.4$ 1.46 2.18 2.14 4.57 4.97 6.18

CL78 - CL7X .557 .107 .385E-01 -. 180 -. 402 -. 221 -. 317 .736 .300 .8196-01 -. 792E-01 -. 332 -. 305 -. 21' .755 .412 .8486-01 .107 .339 .310
STUDSVIK ENERGITEKNIK AB NP-87/128

1987-11-03

Appendix C.4

- COOES - -- TIME INTERVAL ----

CAIC. EXP. 0.0 - 20.00 - 50.00 - 200.0 - 600.0 - 1000.

CL88 - CLSX .451 .650

.669

CL9B - CL9X -13.6

-7.58

7.86

CLAB - CLAX 17.8

14.7

14.8

BRID - BRIX 7.85

42.3

57.0

1R2B - 8R2X 8.59

7.08

8.02

BR48 - BR4X .810 -9.29

14.8

BR58 - Sf5X 3.19

14.6

19.3

SACI - BR6X .543

.821

.855

SPIS - SPIX -7.52

-7.33

7.58

8P28 - S2X -6.99

-6.88

7.13

SP38 - SP3X -3.15

-. 689

.954

8333 - 9S3X -. 341

-.177

.249

am48 - SS4X 8.56

4.93

6.64

S658 - 8S5X .147

.8156-01

.8376-01

Is -'S IX -16.1

-12.3

13.1

P 1e - P IX .837E-01

.5686-01

.6366-01

P 28 - P 2X -20.1

-11.8 12.7

P 38 - P 3X -19.7

-13.0

13.7

P 48 - P 4X .341

.349

.363

5018 - ECIX -. 670E-03

-. 135

.161

-. 937E-01 .146

.347

-81.2

-50.0

55.7

1.60

-. 792

8.93

-33.7

-24.5

31.0

2.04

3.51

3. 186

-1.83

-. 737

1.25

1.91

2.82

3.25

.850E-02

.245

.390

-. 480 -3.01

3.66

1.83

-1.66

3.05

-76.9

-51.5

57.6

-. 117 -. 152

.162

.540

3.50

4.37

.128

.131

.131

-1.02

-6.51

8.02

.672E-01

.6196-01

.627E-01

-2.14

-13.8

16.6

1.74

-12.1

15.8

-. 144E-01

.200

.349

-. 195 -. 120

.124

-130.

-90.4

91.9

10.2

7.26

10.3

80.3

13.0

32.3

.398

.572

.688

-1.61

-1.78

1.78

.975

1.78

1.82

-. 660E-01

.415E-03

.3306-01

-. 980 -. 489

.602

2.02

2.35

2.39

-80.3

-71.3

71.5

-. 106 -. 111

.115

-2;00

-1.35

1.46

.306E-01

.108

.121

1.03

.862

1.09

.8396-01

.BOE-01

.801E-01

-9.35

-4.77

5.22

4.76

3.96

4.13

-. 105 -. 3296-01

.439E-01

-. 333 -. 257

.260

-31.6

-71.6

83.8

-14.9

-4.67

33.8

164.

102.

109.

.232

.353

.506

-2.19

-1.68

1.70

.535

.548

.558

-. 143 -. 113

.117

-3.63

-1.94

2.09

1.96

2.58

2.61

-18.2

-41.9

48.0

-. 141 -. 125

.125

-1.86

-2.84

2.67

-. 182 -. 7946-01

.102

-1.46

.921

1.25

.836E-01

.838E-01

.8386-01

-35.1

-23.2

24.3

-6.88

-. 489

3.52

-. 281 -. 189

.196

.209E-01

-. 392E-02

.134E-01

-. 579 -. 460

.465

-12.9

-14.9

16.2

7.60

-11.8

12.3

131.

121.

122.

-. 5756-01

-. 1876-01

.149

-4.94

-3.85

3.95

.803

.679

.686

-. 335 -. 277

.283

-6.87

-5.24

5.34

1.84

2.40

2.42

-16.5

-13.0

13.2

-. 207 -. 169

.170

1.63

.574

1.55

-. 517 -. 351

.362

-8.88

-5.78

6.27

.844E-01

.8386-01

.838E-01

-56.2

-47.2

47.6

-21.5

-15.1

15.6

-. 486 -. 412

.417

.3106-01

.320E-01

.336E-01

- 1500.

-. 399

-. 471

.474

-12.9

-13.5

13.5

-13.9

-12.5

13.1

26.7

76.1

79.1

-. 187

.206

.254

-4.02

-4.46

4.48

1.24

1.05

1.05

-. 182 -. 252

.257

-5.52

-6.29

6.30

1.60

2.26

2.27

-15.9

-16.9

16.9

-. 297 -. 234

.235

3.26

2.77

2.84

-1.24

-. 857

.883

-9.70

-9.06

9.08

.839E-01

.8406-01

.8406-01

-70.3

-63.1

63.2

-32.2

-26.7

26.8

-. 310 -. 388

.391

.259E-02

.205E-01

.237E-01

- 2000.

-. 497 -. 392

.393

-18.3

-16.2

16.3

-16.3

-13.6

13.7

.810

16.6

19.6

-. 260 -. 207E-01

.285

-7.63

-4.86

4.96

1.72

1.37

1.38

-. 300 -. 192

.196

-9.36

-6.63

6.70

3.67

2.60

2.65

-19.4

-17.5

17.6

-. 370 -. 321

.323

-6.27

1.33

3.04

-1.90

-1.58

1.60

-2.94

-8.05

8.27

.839E-01

.842E-01

.842E-01

-90.2

-79.4

79.6

-". 0 -37.6

37.8

-. 402 -. 301

.303

.504E-01

.2396-01

.267E-01

-. 5586-01 -. 2566-01 -. 107E-02 -. 392E-01 .532E-01 .3996-01
STUDSVIK ENERGITEKNIK AB NP-87/128 Appendix C.5

1987-11-03

Case C

CA•LCULATION-TO-EXPERIMENT DATA UNCERTAINTY ANALYSIS FOR NRC/ZCAP.

FIRST LINE DIFFERENCE BETWEEN CALCULATED AND (AVERAGED) EXPERIMENTAL DATA AT END OF THE INTERVAL SECOND LINE MEAN DIFFERENCE OVER THE INTERVAL

THIRD LINE MEAN SI(3M OVER THE INTERVAL (ROOT MEAN SOUARE OF THE DIFFERENCE)

- CODES - ---- TIME INTERVAL ----

CALM. EXP. 0.0 - 20.00 - S0.00 - 200.0 - 500.0 - 1000. - 1800. - 2000.

C 3C - C 3X .IOOE-01 -2.01 -1.99 -3.94 -6.52 -5.17 -5.11 - 260 -. 947 -1.92 -2.59 -65.44 -5.73 -5.80

1.21 1.21 1.92 2.67 5.48 6.74 5.66

C 4C - C 4X .550 -1.27 -1.49 -3.32 -6.06 -4.52 -7.43 6.51 -. 530 -1.31 -2.24 -4.98 -5.19 -8.08 8.22 .911 1.31 2.32 5.04 5.21 6.15

C 50 - C 5X 1.07 -1.19 -1.66 -3.60 -6.44 -4.67 -7.60

4.80 -. 908E-01 -1.41 -2.42 -5.24 -5.61 -5.27 6.69 .733 1.42 2.49 5.30 6.63 5.34

C 6C - C 6X .750 -1.08 -1.23 -3.28 -6.35 -4.96 -7.77 5.77 -. 299 -1.16 -2.23 -5.13 -5.52 -5.46

7.39 .683 1.17 2.31 5.20 5.54 5.52

C 7C - C 7X -. 650 -1.18 -1.58 -3.57 -5.52 -5.17 -8.11 -. 812E-01 -. 896 -1.36 -2.40 -5.25 -5.74 -5.75

.666 .929 1.36 2.47 6.32 5.75 5.62

C aC - C 8X -. 550 -1.46 -1.47 -3.69 -6.54 -5.56 -8.66 -. 247 -. 986 -1.42 -2.55 -5.42 -6.02 -6.16

.599 1.04 1.43 2.63 6.49 6.03 6.22

C 90 - C 9X -2.29 -3.47 -4.31 -6.45 -9.09 -7.98 -10.8 -1.03 -3.17 -3.77 -4.80 -7.75 -8.24 -8.30 1.38 3.21 3.76 4.93 7.80 8.25 8.36

C AC - C AX -. 3S2 1.00 .744 .767E-01 -. 6SDE-0l -. 537 -. 425

.549 .207 .786 .187 -. 5654-01 -. 357 -. 449

1.27 .486 .814 .278 .295 .399 .462

V sC - V ax -1.64 -4.96 -5.06 -6.50 -9.37 -7.07 -10.0 -1.19 -3.56 -5.16 -5.41 -6.06 -6.44 -8.02 1.22 3.75 5.16 5.42 8.11 8.46 8.05

V SC - V eX -1.69 -3.00 -3.91 -5.76 -8.63 -7.27 -10.1 .495 -2.60 -3.31 -4.36 -7.20 -7.65 -7.68

1.76 2.67 3.31 4.40 7.26 7.66 7.73

V ?C - V 7X 5.17 3.74 3.36 3.45 2.7$ 2.75 3.98 5.28 5.13 3.70 3.24 3.14 2.77 3.32

5.31 6.47 3.70 3.24 3.14 2.77 3.34

V BC - V &X -1.85 -4.86 -4.63 -6.08 -8.19 -6.48 -9.23 -. 669 -3.39 -4.74 -5.16 -7.46 -7.27 -7.07

1.01 3.52 4.74 5.19 7.48 7.29 7.11

V 9C - V 9X .5687 .113 .232E-01 -. 167 -. 376 -. 183 -. 261

.779 .316 .777E-01 -. 689E-01 -. 297 -. 270 -. 173 .798 .434 .612E-01 .902E-01 .303 .276 .175

V AC - V AX .464 -. 570E-02 -. 805E-01 -. 310 -. 526 -. 253 -. 360

.656 .204 -. 323E-01 -. 200 -. 451 -. 390 -. 264

.676 .366 .4019-01 .213 .456 .400 .266

HLIC - NLIX -34.3 28.2 49.1 -73.5 47.7 38.2 10.5 -21.9 .208 56.4 -16.6 -53.6 56.1 23.7

22.8 22.7 66.0 62.9 67.6 68.6 27.3

HL2C - HL2X -32.1 -14.9 -32.3 -239. 167. 17.0 9.98

-30.3 -24.3 -23.3 -19.9 -. 940 66.5 -3.62

30.6 24.9 24.0 65.0 121. 76.2 6.36

NL4C - HL4X .940 .600E-01 -. 600 -2.57 -6.28 -4.90 -6.20

2.64 .464 -. 173 -1.76 -4.74 -5.36 -5.56 3.05 .575 .320 1.89 4.82 5.38 5.62

ML1. - HL5X .565 .103 .187E-01 -. 176 -. 370 -. 153 -. 201 .733 .313 .7051-01 -. 926E-01 -. 314 -. 269 -. 130 .750 .429 .752E-01 .111 .319 .267 .132

CLIC - CLIX -4.92 -65.0 -8.92 11.0 133. 43.5 4.39

-17.2 -41.1 -26.3 6.58 96.2 76.2 16.2 19.4 47.7 32.3 16.0 77.2 79.4 19.4

CL2C - CL2X 742. 657. 566. 364. 197. 65.7 14.1 745. 698. 621. 457.. 276. 123. 26.1

745. 699. 621. 461. 276. 130. 30.4

CL3C - CI.3X -9.04 -2.75 -. 470 202. -6.53 -14.6 -5.27

-3.95 -7.96 -2.07 67.6 104. -13.7 -11.2 4.56 6.88 6.67 145. 126. 15.4 11.9

CLAC - CLAX .2865 -. 787 -. 605 -3.08 -. 391 -. 835E-01 -. 594E-01 .479 -. 509 -. 649 -3.16 -1.22 -. 228 -. 623E-01 .513 .561 .685 3.61 1.47 .254 .6368-01

CL6C - CL6X .790 -2.41 -2.39 -3.17 -6.32 -4.63 -7.96

1.45 -. 680 -2.39 -2.54 -4.99 -5.42 -5.68

1.50 1.46 2.39 2.56 5.07 8.44 5.64

CLC - CL7X .552 .975E-01 -. 170E-01 -. 232 -. 449 -. 252 -. 332 .734 .299 .526E-01 -. 131 -. 380 -. 34S -. 246

.766 .411 .6278-01 .147 .386 .353 .247
STUDSVIK ENERGITEKNIK AB NP-87/128 Appendix C.6

1987-11-03

---- TIME INTERVAL - - - -

- 200.0 - 600.0 - 1000. - 1600. - 2000.

- COOES -

CALC. EXP. 0.0 - 20.00 - 80.00

CL8C - CLSX .446

.648

.670

CL9C - CL9X -13.6

-7.63

7.90

CLAC - CLAX 17.8

14.7

14.8

MRIC - BRIX 7.89

42.2

57.0

BR2C - BR2X 8.59

7.08

8.01

9R4C - BR4X .780 -9.27

14.8

BRSC - 5R5X 3.18

14.5

19.3

SR6C - BR6X .538 .819

.855

SPIC - SPIX -7.56

-7.37

7.62

8P2C - SP2X -6.99

-5682

7.07

8P3C - SP3X -3.18

-. 721

.990

S33 - 863X -. S41 -. 181

.250

6S4C - 334X 8.50

4.91

5.62

S35C - S3SX .145

.635E-01

.680E-01

8 10 - S iX -16.1

-12.3

13.1

P 10 - P IX .826E-01

.559E-01

.6266-01

P 2C - P 2X -20.1

-11.8

12.8

P 3C - P 3X -19.8

-13.0

13.8

P 40 - P 4X .336

.245

.349

6CIC - ECIX -. 670E-03

-. 135

.161

-. 716E-01

.155

.345

-52.5

-40.5

44.2

1.60

-. 792

8.93

-38.3

-25.6

32.5

2.31

3.54

3.89

-1.88

-. 734

1.25

2.09

2.89

3.29

.228E-01

.253

•390

-. 450 -2.98

3.65

1.83

-1.66

3.06

-28.7

-39.9

44.9

-. 117 -. 153

.162

.360

3.19

4.48

.132

.134

.134

-. 606 -6.17

7.82

.671E-01

.618E-01

.626E-01

-2.03

-13.8

16.6

1.90

-12.0

15.7

-. 280E-02

.206

.348

-. 685E-01 -. 148E-02

.533E-01

-. 163 -. 9816-01

.101

-27.4

-38.9

40.7

10.2

7.26

10.3

66.8

4.87

27.8

.427

.653

.774

-1.95

-1.98

1.98

1.70

2.16

2.17

-. 263E-01

.193E-01

.312E-01

-1.01

-. 525

.630

2.14

2.41

2.46

-22.4

-26.9 28,1

-. 105

-. 111

.115

-- 1.91

-1.35

1.43

.223E-01

.101

.115

.912

.821

1.01

.839E-01

.•00E-01

.8015-01

-9.24

-4.73

5.18

4.92

3.99

4.15

-. 931E-01 -. 287E-01

.397E-01

-. 2765-01 -. 400E-01

.407E-01

-. 376 -. 266

.275

-23.1

-27.5

28.9

-14.9

-4.67

33.8

167.

88.4

95.8

.243

.500

.522

-2.65

-2.02

2.06

.546

.766

.863

-. 186 -. 126 .136

-4.12

-2.24

2.41

1.99

2.66

2.67

-12.9

-17.3

17.8

-. 138 -. 122

.123

-. 590 -1.96

2.00

-. 227 -. 109

.132

-3.23

-. 264

1.24

.836E-01

.838E-01

.838E-01

-35.6

-23.4

24.6

-7.42

-. 836

3.76

-. 327 -. 212

.223

.234E-0?

-. 318E-02

.146E-01

-. 624 -. 505

.609

-10.1

-11.5

13.1

7.60

-11.8

12.3

128.

117.

119.

-. 606E-01

-. 481E-01

.159

-5.49

-4.36

4.45

.904

.685

.693

-. 381 -. 322

.327

-7.43

-5.76

5.85

1.85

2.41

2.43

-13.7

-11.0

11.2

-. 208 -. 169

.170

1.08

.$94

1.07

-. 563 -. 396

.406

-8.88

-6.42

S.68

.844E-01

.838E-01

.8386E-C

-68.7

-47.7

48.1

-21.7

-15.4

15.8

-. 531

-. 458

.462

.3366-01

.346E-01

.361E-01

-. 428 -. 512 -. 512 -. 419 .616 .420

-11.1 -18.2 -9.95 -15.9 9.97 16.0

-13.9 -16.3 -12.5 -13.6 13.1 13.7

27.2 1.27

73.2 17.1

76.7 20.3

-. 245E-01 -. 252

.286 .529E-02

.325 .208

-4.52 -7.92

-5.03 -5.33

5.04 5.41

1.24 1.72

1.05 1.37

1.05 1.38

-. 215 -. 314 -. 294 -. 219

•298 .222

-5.98 -9.65

-6.84 -7.10

6.85 7.16

1.61 3.67

2.28 2.60

2.29 2.65

-14.6 -19.4

-14.5 -17.3

14.15 17.4

-. 268 -. 369 -. 236 -. 319

.236 .321

2.83 -6.65

2.21 .319

2.29 2.82

-1.27 -1.92 -. 8a" -1.61

.923 1.63

-9.72 -2.86

-9.05 -8.00

9.07 8.22

.839E-01 .939E-01

.640E-01 .842E-01

.840E-01 .942E-01

-70.8 -90.5

-63.7 -79.9

63.8 80.1

-32.0 -43.7

-26.7 -37.6

26.9 37.7

-. 339 -. 417 -. 428 -. 328

.432 .329

.430E-02 .5136-01

.2281-01 .255E-01

.2586E-01 .280E-01
STUDSVIK ENERGITEKNIK AB NP-87/128 Appendix D.1 (1)

1987-11-03

STUDSVIK

THIS TAPE CONTAINS DATA FROM THE ICAP PREDICTION CALCULATION

WITH THE RELAP5/MOD2/36.04 FOR THE LOFT EXPERIMENT NO. L3-6.

CONTENTS, FILE 1 .

2.

3.

4.

5.

6.

7.

a.

THIS DESCRIPTIVE TEXT

INPUT CASE A, STEADY STATE

B, -"- ,UPDATES

C, -"- ,UPDATES TO A + B

DATA, EXPERIMENT - CASE A

- CASE B - CASE C

I. COMPUTER

NAME

WORD SIZE

II. TAPE FORMAT

NUMBER OF TRACKS

PACKING DENSITY

RECORD SIZE

BLOCKING FACTOR

CODED

CONTROL WORDS

CYBER 170-810

60

9

1600 BPI

80

64

EBCDIC

NO

III. DATA FORMAT, FOR EACH OF THE FILES 5 THROUGH 8

TITLE RECORD(S). (FORMAT I5,A75)

FIELD 1. THE NUMBER OF DATA CHANNELS ON THE FILE

FIELD 2, PROBLEM IDENTIFICATION

UP TO FIVE ADDITIONAL IDENTIFICATION RECORDS

MAY BE ADDED BY 'C' IN COLUMN 1 OF FIELD 1

DATA SET RECORD 1, (FORMAT 215,A60)

FIELD 1, NUMBER OF DATA POINTS

FIELD 2. THE ENGINEERING UNIT CODE (EUC) FOR THE

VARIABLE

FIELD 3. IDENTIFYING TEXT OF THE DATA

REMAINING DATA SET RECORDS FORMAT 5(E16.9)

EACH DATA CHANNEL SUBMITTED IS GIVEN THROUGH TWO DATA

SETS, THE FIRST OF WHICH IS THE TIME DATA SET.

THE TWO SETS HAVE THE SAME NUMBER OF DATA POINTS.

THE TIME DATA SET IS IDENTIFIED BY EUC-77 (FIELD 2)

AND THE IDENTIFYING TEXT 'TIME' (FIELD 3).

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

I2-891 (Asigemd by NRC. Add Vol.. Suoo.. Rev.. NRCM 1102. and Addendum Numbemr. If any.) 3201.202. BIBLIOGRAPHIC DATA SHEET NIJREG/1A-0033

[See instructions on the reverse)

2. TITLE AND SuBTITLE STUDSVI K/NP-87/128

Assessment of RELAP5/MOD2, Cycle 36.04 3. DATE REPORTPUBLISHED

Against LOFT Small Break Experiment L3-6 ,,ONTH' i EA

July 1990

4. FIN OR GRANT NUMBER

N/A

5. AUTHORIS) 6. TYPE OF REPORT

John Eriksson Technical

7. PERIOD COVERED inctv eoi•ws.

8. PERFORMING ORGANIZATION - NAME AND ADDRESS (If NRC. provide Oivision. Office or Region,'U.S. Nucleit, Rgularo,' Commisson. and mailing ad•oress.,it conttrtor, yowao,.

nao" and mailing address.)

Swedish Nuclear Power -Inspectorate.....

Box 27106

10252 Stockholm

Sweden

9. SPONSORING ORGANIZATION - NAME AND ADDR ESS III NRC. type "nwSe as ooow"; if contractor. provide NRC Oivision. Office of Region. U4 Nuclea Regulatory Commisuon. and mailing addres.)

Office of Nuclear Regulatory Research

U.S. Nuclear Regulatory Commission

Washington, DC 20555

10. SUPPLEMENTARY NOTES

11. ABSTRACT 200 words ori e

The LOFT small break experiment L3-6 has been analyzed as part of.Sweden's

contribution to the International Thermal-Hydraulic Code Assessment and

Applications Program (ICAP).

Three calculations, of which two were sensitivity studies, were carried out.

following quantities were:varied:

the content of secondary side fluid and the feed water

valve closure

the two-phase characteristics of the main pumps

All three predictions agreed reasonably well with most of the measured data.

sensitivity calculations resulted only in marginal improvements.

The

The

The predicted and measured data are compared on plots and their differences are

quantified over intervals in real time.

12. KEY WORDS/DESCR!PTORS fList words orohrases that wll &mistresearcher in locating the or..i . 3.AVAIASILI8TY STATEMENT

Unlimited

RELAP5/MOD2/ Cycle 36.04 Against LOFT Small Break 14. sEcURT CLASSIFICATION

Experiment L3-6 IThis PaOW

Unclassified

(This Roorr•l

Uncl assi fi ed

15. NUMBER OF PAGES

16. PRICE

NRC FORM 335 !2-8)


NUREG/IA-0033 ASSESSMENT OF RELAPS/MOD2, CYCLE 36.04 AGAINST LOFT

SMALL BREAK EXPERIMENT L3-6

JULY 1990