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Agreement Report RELAP5/MOD3.2 Post Test Calculation of the
NUREG/IA-0170
International
Agreement Report
RELAP5/MOD3.2
Post Test Calculation of the
PKL-Experiment PKLIII-B4.3
Prepared by
L. Karner
Siemens Energierzeugung (KWU)
Freyerslebenstrasse 1
D-91058 Erlangen
Germany
Office of Nuclear Regulatory Research
U.S. Nuclear Regulatory Commission
Washington, DC 20555-0001
December 1999
Prepared as part of
The Agreement on Research Participation and Technical Exchange
under the International Code Application and Maintenance Program (CAMP)
Published by
U.S. Nuclear Regulatory Commission
I
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NUREG/IA-0170
International
Agreement Report
RELAP5/MOD3.2
Post Test Calculation of the
PKL-Experiment PKLIII-B4.3
Prepared by
L. Karner
Siemens Energierzeugung (KWU)
Freyerslebenstrasse 1
D-91058 Erlangen
Germany
Office of Nuclear Regulatory Research
U.S. Nuclear Regulatory Commission
Washington, DC 20555-0001
December 1999
Prepared as part of
The Agreement on Research Participation and Technical Exchange
under the International Code Application and Maintenance Program (CAMP)
Published by
U.S. Nuclear Regulatory Commission
Report-No.:
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Page
Table of Contents
1
2
3
3.1
3.2
3.3
3.4
Abstract
Abbreviations
Introduction
Description of the PKL Test Facility
Description of Experiment PKLIII-B4.3
Objectives of Test PKLIII-B4.3
Initial and Boundary Conditions of the Test B 4.3
Sequence of Events
Phenomenological Analysis of Test Results
4
Results of RELAP5/Mod 3.2 Analysis
4.1
Description of RELAP5/Mod 3.2
4.2
4.3
4.4
4.5
Description of Input Model
Calculational Procedures and Boundary Conditions
General System Response
Steam Generator Heat Transfer as a Function of
Nitrogen Distribution in the Primary System
Propagation of Nitrogen Concentration in the
Steam Generator U-Tubes
Conclusions
References
List of Figures
Figures
4.6
5
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3
Abstract
The PKL III test facility (Primar-Kreis-Lauf) simulates a typical 1300 MWe
Pressurized Water Reactor of Siemens/KWU. In test B4.3, the influence of non
condensables on heat transfer in the steam generators during reflux condenser
conditions was investigated.
This report presents the results of a post-test analysis of PKL 111-B4.3 using
RELAP5/Mod 3.2. A description of the input model is given, and the
correspondence of measured and calculated results is discussed.
The results of the calculation show differences in the distribution of nitrogen in the
primary system compared to the experiment. When nitrogen was injected into the
hot leg of the primary system, the heat transfer in the affected steam generator
decreased. In contrast to the experiment RELAP calculated that the volumes in
the adjacent steam generator did not get the full amount of nitrogen and that
nitrogen was transported from the steam generators to other locations during the
course of the transient. Thus the heat transfer in these steam generators later
increased in contradiction to the measured values.
In the steam generator tubes, RELAP calculated that the nitrogen accumulates in
the descending part as predicted in the experiment. For the ascending U-tubes
RELAP predicted that the nitrogen was transported to the loop seal, which was not
seen in the experiment.
Fluctuations occured during the course of the RELAP5/Mod 3.2 analysis of the
PKLIII B4.3 experiment. This phenomenon may be the main reason, that RELAP
calculates the transport of nitrogen from the steam generators into the system and
predicts finally a homogeneous distribution of nitrogen in the primary system.
The analysis performs an inkind contribution to the CAMP contract.
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4
Abbreviations
ACCU
ARV
ASC.
Byp.
CAMP
CCFL
CL
CV, CNTRLVAR
DC
DE
Depress., dp
DESC.
DH
Diff.
Exp.
HKPM, RCP
HL
Int., Integr.
L
LOCA
LPL
MFLOWJ
N
PKL, PCL
Press., P
Primary-S.
PWR
R
RDB, RPV
SATTEMP
SATT-Pr.
SATT-Sec.
SBB
SBLOCA
Secondary-S.
SG
SPW
SV
TEMP
UPL
U-tubes
accumulator
Abblaseregelventil (relief valve)
ascending (U-tubes)
bypass
Code Assessment and Maintenance Program
counter current flow limitation
cold leg, collapsed level
control variable
downcomer
Dampferzeuger (SG)
depressurization
descending (U-tubes)
Druckhalter (pressurizer)
difference
experiment
Hauptk~hlmittelpumpe (reactor coolant pump)
hot leg
integrated
loop
loss of coolant accident
lower plenum
junction mass flow
nitrogen
Primdrkreislauf, Primary Coolant Loop
pressure
primary side
pressurized water reactor
RELAP
Reaktordruckbehdlter, reactor pressure vessel
saturation temperature
saturation temperature primary side
saturation temperature secondary side
StabbOndelbehdlter (rod bundle vessel)
small break LOCA
secondary side
steam generator
Speisewasser (feedwater)
Sicherheitsventil (safety valve)
temperature
upper plenum
tubes with n-profile for SGs
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Page5
Introduction
The PKL III test facility simulates a typical 4 loop 1300 MWe pressurized water
reactor of Siemens/KWU design. Within the PKL Ill-B4 test series, three tests
have been performed to investigate the influence of non-condensables in the
primary system on steam generator heat transfer.
In Test B4.1 the primary inventory was 100 % and thus the influence of non
condensables on single-phase natural circulation was investigated. In Test B4.2
the primary inventory was reduced to 85% which generated two-phase natural
circulation. In test B4.3, by a further reduction of the inventory to 35% the
influence of non-condensables on reflux-condenser conditions was investigated.
In this report a post-test analysis of PKL 1l1-B4.3 using RELAP5/Mod 3.2 is
presented. A description of the input model is given, and the correspondence of
measured and calculated results is discussed.
The purpose of this analysis is to serve as a contribution to the verification of
RELAP5/Mod 3.2's ability to handle a non-condensable component in the
gaseous phase properly.
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Page
6
Description of the PKL Test Facility
The PKL III test facility simulates a typical 1300 MWe pressurized water reactor of
Siemens/KWU of a volume/power scale of 1:145 (Fig. 2.1). All elevations
correspond to real plant dimensions. It is a large scale facility with four primary
loops, which are arranged symmetrically around the pressure vessel. Each of the
four loops contains a main coolant pump and a fully scaled steam generator with
prototypical tubing and tube sheet. The core is simulated by a bundle of 314
electrically heated rods, with a total power of 2.5 MW, corresponding to 10% of the
scaled nominal power. The primary pressure is limited to 4.5 MPa. Regarding the
limited pressure of the PKL Ill test facility the scaling of the experiments falls into
three general categories:
The first category of experiments provides an insight into special physical
phenomena, such as CCFL or the influence of nitrogen, which are expected to
take place in PWR's at pressures below 4.5 MPa. The second category concerns
experiments "entering" a PWR-transient at a pressure level of 45 bar. The
conditions in PKL at the start of such a test are set up using code-calculations for
the PWR, an example being small break LOCAs, where the important phenomena
occur at pressures below 50 bar. The third category covers scenarios where
phenomena occurring at high pressures in PWR's can be simulated at pressures
below 50 bar in PKL, with the results being extrapolated to the original pressure
(with the help of codes or comparisons with experimental results from full-pressure
test facilities).
The test facility is equipped with all important safety and auxiliary systems, e.g.
volume control system, high and low pressure injection system, accumulators and
residual heat removal system. In correspondence to KWU-type plants, four
independent high and low pressure injection systems which are connected to both
the hot and cold legs are simulated.
The arrangement of the test facility is shown in Fig 2.1,
The steam generators of the test facility are equipped with U-tubes. Each SG has
27 heat exchanger tubes in accordance to the 1:145 scale. The tubes are
arranged to assemblies with 7 different lengths. The peak elevations of the longest
and shortest tube correspond to the plant dimensions. Two replacement bodies
are inserted in the secondary side to achieve the volume scale. A cross-sectional
view is given by Fig. 2.2.
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At least 3 U-tubes in each SG are equipped with thermocouples for the
measurement of primary side fluid temperature at different axial positions. The
axial location of these thermocouples is shown in Fig. 2.3.
Within the test facility there are more than 1300 locations for measurement
instrumentation. This provides extensive information necessary for the
understanding of all relevant thermal hydraulic phenomena.
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Description of Experiment PKLIII B4.3
3.1
Objectives of Test PKLIII B4.3
Page
Beginning by January 1989 the test series IIIB was initiated at the PKL test
facility. Focused on accident-management procedures the majorities of tests were
performed in order to investigate phenomena occurring during primary side and
secondary side feed and bleed procedures. Within PKL III B4 three tests have
been performed to investigate plant performance with presence of non
condensables in the primary system.
The investigation of the influence of non-condensables on plant performance was
considered to be meaningful, because accident scenarios exist where nitrogen or
hydrogen accumulates in the steam generators and reduces heat transfer to the
secondary side. Nitrogen may be expelled by the accumulators in the cause of an
postulated Large Break Loss-of-Coolant Accident. It is dissolved in the primary
system coolant, in the liquid of the refueling storage tank, and accumulator liquid,
or may be already present in the system during refueling. And hydrogen
generated by metal-water reaction at the fuel cladding may accumulate in the
steam generators during post-design accident scenarios.
In the test series primary pressure (1 MPa) and power generation rate (2 %) have
been kept constant whereas primary side inventory was different in each test. In
Test B4.1 the primary inventory was 100 % and thus the influence of non
condensables on single-phase natural circulation was investigated. In Test B4.2
the primary inventory was set to 85% which generated two-phase natural
circulation. And in Test B4.3, by a further reduction of the inventory down to 35%
the influence of non-condensables on reflux-condenser conditions was
investigated.
Descriptions of the PKL test facility and of experiment PKL III B4.3 is given in
reference /l/through /3/
3.2
Initial and Boundary Conditions of the Test B4.3
The test was initiated by a conditioning phase where the primary inventory has
been already reduced, but no nitrogen was injected.
The reflux condenser conditions resulted in an accumulation of liquid inventory in
the hot legs and in the inlet regions of the SG tubes. In the hot leg a collapsed
level of 1.2 m was observed. The collapsed levels in the tubes were 1.5 m. The
swell level in the vessel was below the inlet junctions of the loop pipings. The loop
seals were filled with water.
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With the secondary side pressure (and saturation temperature) given, the primary
side pressure is a system response. The primary side pressure is established to
generate the temperature difference, which is necessary for stationary heat
removal. In the experiment under consideration the temperature difference was
6 K.
Based on a secondary side energy balance it can be concluded, that about
460 kW are transferred to the secondary side. Consequently, the primary side heat
losses are about 60 kW. On the secondary side there is a heat loss of
approximately 10 kW per SG.
The major parameters of the stationary conditions in the primary system are
summarized in Table 3.1, the secondary side conditions are summarized in Table
3.2.
Primary Inventory
Power
Primary Pressure
Core Outlet Temperature
Main Coolant Pumps
Pressurizer
Primary/Secondary Side Temperature Difference
Primary System Initial Conditions
Tab. 3.1:
Collapsed Level in SG Downcomer
Steam Line Pressure LBA 10-40
Steam Line Temperature
Feed Water Mass Flow LAB 10-40
12 m
0.87 MPa
447 K / 174 OC
0.05 kg/s / loop
Secondary System Initial Conditions
Tab. 3.2:
3.3
35 %
2 % (520 kW)
1.0 MPa
453 K / 180 °C (saturated)
not operating
isolated
6K
Sequence of Events
Test PKLIII B4.3 investigates the system's response to a succession of nitrogen
injections periods into the primary system at various injection ports. In the course
of the test the secondary pressure was reduced occasionally in order to
compensate the influence of nitrogen on heat removal in the steam generators.
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10
The sequence of nitrogen injection periods and secondary side pressure
operations is given in Table 3.3:
Time
Event
0 - 3600 s
1. period of nitrogen injection
0.25 Nm3 , 3600 s, HL 10
(10990 - 14590 s)
4870- 6310s
(15860- 17300 s)
2. period of nitrogen injection
0.1 Nm3 , 1440 s, CL 30
6400 - 10000 s
(17390 - 20990 s)
0.25 Nm3 , 3600 s, CL 30
10880 - 11180 s
3. period of nitrogen injection
0.25 Nm3 , 300 s, HL 20
(21870 - 22170 s)
14295 - 14595 s
(25285 - 25585 s)
4. period of nitrogen injection
0.25 Nm3 , 300 s, CL 40
14735 s (25725 s)
reduction of secondary pressure to .80 MPa
16000 - 19600 s
(26990 - 30590 s)
5. period of nitrogen injection
1.5 Nm3 , 3600 s, HL 10
(21430 s)
reduction of secondary pressure to 0.55 MPa
22840 - 26440 s
(33830 - 37430 s)
6. period of nitrogen injection
1.5 Nm3 , 3600 s, CL 30
27340 s (38330 s)
reduction of secondary pressure to 0.37 MPa
(38990 s)
End of Test
Tab. 3.3:
Nitrogen Injection Periods and Secondary Side Pressure Settings
The amount of nitrogen which is injected in each of the first four periods
corresponds to the amount which is dissolved in the accumulator liquid. During
each the fifth and sixth period of injection the full depletion of a accumulator
gaseous inventory was simulated.
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3.4
Page
11
Phenomenological Analysis of Test Results
This chapter analyses the phenomena which occurred during the test and
describes
- the effect on heat transfer in the steam generator during reflux condenser
mode ifnitrogen is present in the primary system,
- the overall distribution of nitrogen in the primary system depending on the
location of an injection
- and the dependence on the primary to secondary side pressure and
temperature difference.
A detailed description of the test results will be given later in this report in
conjunction with comparison to calculational results.
The reflux condenser mode is characterized by counter-current flow of liquid and
steam in the hot leg. If nitrogen is injected into the primary system, it is
transported by convection (diffusion is not effective). At locations of lower
temperature, such as the steam generator or reactor coolant pump, steam is
condensed and nitrogen is subsequently accumulated. The quality of nitrogen is
increased until the partial pressure of steam and its saturation temperature
corresponds to the saturation pressure of the local temperature (e.g. secondary
side). These conditions represent a thermal equilibrium, and no heat transfer or
condensation occurs in such a passive area.
The transition from an active heat transfer area to a passive heat transfer area is
accelerated by the phenomenon that the inert gas is accumulated at the
condensation film on the cooling surface. The density of the inert gas in this
boundary layer is higher than in the center of the steam flow. For this reason the
partial pressure and the temperature of the steam in the nitrogen enriched layer is
lower than the average steam temperature and partial pressure in the steam flow.
After the termination of the condensation the layer of accumulated inert gas is
dispersed by diffusion.
The distribution of nitrogen in the primary system depends on the location of
injection. If a moderate amount of nitrogen is injected into a hot leg of the loop of
the test facility, it is transported to the adjacent steam generator where an
accumulation at the location of condensation takes place. A "region of inertness"
or passive area is established. It proceeds from the SG outlet chambers and
depending on the amount of nitrogen injected, can occupy the whole steam
generator. If the hot leg is completely filled, nitrogen flows to the upper plenum
and into the other hot legs. However under these conditions no permanent
accumulation of nitrogen was observed in the upper plenum. The distribution of
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nitrogen does not depend significantly on the injection rate but only on the total
amount of injected nitrogen.
If a moderate amount (0.25 Nm3 in 1h) of nitrogen is injected into the cold leg,
under reflux condenser conditions it is accumulated in the adjacent pump, as heat
losses dominate in this component and steam is accordingly condensed. If more
nitrogen is injected or if the injection rate is high, nitrogen is transported via the
bypass from the downcomer into the upper plenum and finally into the steam
generators.
The influence of nitrogen on heat transfer in the SG tubes can be compensated
by lowering the secondary pressure or increasing the primary pressure. The
resulting increase of temperature difference between primary and secondary side
has a direct impact on heat transfer. In addition the partial pressure of steam is
diminished via the accumulation of nitrogen. Therefore the concentration of
nitrogen can be higher. By an increase of primary pressure the region of inertness
is compressed and establishes thus a additional partial recovery of the heat
transfer.
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4.
Results of RELAP5IMod 3.2 Analysis
4.1
Description of RELAP5/Mod 3.2
Page
13
The Mod3.2 version of RELAP5 has been developed within the Code Applications
and Maintenance Program (CAMP).
The code development has benefitted from extensive application and comparison to
experimental data in test facilities such as LOFT, PBF, Semiscale and NRU.
RELAP5 is a highly generic code, that can be used in both nuclear and non-nuclear
systems involving mixtures of steam, water, non-condensables, and nonvolatile
solute.
A description of RELAP5/Mod3 is given in reference /4/.
4.2
Description of Input Model
The nodalization scheme is shown in fig. 4.1.
The core area is represented by a single axial flow channel with 8 hydraulic volumes
in the heated region. The fuel rod simulators are represented by 3 heat structures
(HST-10421, HST-10422 and HST-10423) with different power generation rates given
by General Tables 801-803. In the test facility the downcomer consists of two pipes.
Inthe RELAP input they are modeled as a single pipe.
Though being rather coarse, the modeling of the test vessel corresponds to the
requirements of Test PKLIII B4.3, as the phenomena under consideration occur in the
SGs and the loops, and as no core uncovery occurs during the course of the
experiment.
Each loop is modeled separately. The hot leg is represented by 13 hydraulic volumes.
Three types of SG tubes with different lengths are modeled (18, 20, 22 volumes). The
loop piping between SG and pump is represented by 16 volumes, piping between
pump and vessel by 5 volumes. The modeling of the piping and the steam generators
is sufficiently fine to allow an adequate representation of thermal-hydraulic
phenomena relevant in the test under consideration.
The pumps are represented by pump components; homologic data are used, which
have been determined for the LOBI test facility. The cooling of the pumps is
considered.
The noding of the steam generator secondary side has 16 axial nodes in the riser and
13 axial nodes in the downcomer.
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The nitrogen injection is simulated at the hot and cold injection port of the
emergency core cooling system. To consider the flow direction of these nozzles
towards the RPV, the injection junctions are connected to the outlet of the
volumes in the hot legs and to the inlet in the volumes of the cold legs.
The input deck includes a variety of control variables (cv). The following table
comprises control variables which are of particular interest for test PKL Ill B4.3.
Total power
cv 7900
Drained mass of primary system
cv 7500
SG collapsed levels
cvs 2103, 2203, 2303, 2403
Smoothed levels in the SGs, calculated by a
Lag component with a Lag time of 30 s
cvs 2110, 2210, 2310, 2410
Sum of the heat transfer in the short, medium
and long SG tubes of all SGs
cvs 7175, 7275, 7375, 7475
Smoothed heat transfer in the SGs, calculated
by a Lag component with a Lag time of 50 s
cvs 7176, 7276, 7376, 7476
4.3
Calculational Procedures and Boundary Conditions
The post test calculation was started to reach steady-state conditions with a
significantly reduced primary inventory. A calculation was made to meet the initial
and boundary conditions. During the calculation 1491 kg of liquid inventory was
drained from the primary system and the inventories in the SGs were adjusted by
controlling feed water flow and secondary pressure. The calculation for steady
state was stopped after 5000 s. At that time the thermal-hydraulic conditions have
been almost stationary.
As a boundary condition during the transient nitrogen was injected into hot legs 10
and 30 and cold legs 20 and 40. These injection rates are shown in Fig. 4.2 and
4.3.
As the heat transfer in the SG depends on the pressure difference and is merely
independent from the absolute pressure, during the calculations the secondary
side pressure was used in correspondence to the experiment as a calculational
boundary condition. The development of the secondary side pressure is shown in
Fig. 4.4.
Additional to these presumptions the input was fitted out with control variables to
get the nitrogen accumulation and nitrogen flow in the primary system. Together
with the heat transfer to the secondary side the results of the RELAP5/Mod3.2
analysis were assessed against the experimental results.
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15
General System Response
The overall system response to nitrogen injection is depicted in Fig. 4.5 through
Fig. 4.7.
At first the measured system behavior is discussed.
Fig 4.5 shows the pressure history of primary and secondary side. The pressure
increase following the 1. period of nitrogen injection into HL10 (0 - 3600 s) is very
moderate. The 2. period of injection into CL30 (4870 - 10000 s) has no effect on
primary system pressure. The pressure increase during the 3. injection period into
HL20 (10880-11180 s) is more pronounced than in period 1. At the end of
injection period 4 the secondary side pressure is reduced for the first time and
generates a simultaneous decrease of the primary side pressure. The subsequent
injection period 5 with large amounts of nitrogen results in an continuous increase
of primary pressure which was compensated at the end of this injection period by
a further adjustment of the secondary side pressure.
The pressure difference between the primary and secondary side results in a
difference of the corresponding saturation temperatures, which determines the
overall heat transfer. The history of calculated and measured temperatures and
temperature difference is shown in Fig. 4.6 and 4.7. The initial temperature
difference before nitrogen injection calculated by RELAP5/Mod3.2 is 4 K
compared to 6 K in the experiment. The temperature decrease on the secondary
side shown in the experiment during the first period is to be explained by a local
effect (plume of cold water at the thermocouple).
The temperature difference which is formed at the end of each injection period
is summarized in the following table:
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Experiment
RELAP
pre pressure
reduction
post pressure
reduction
pre pressure
reduction
post pressure
reduction
6K
*
4K
*
1. Period (HL 10) 6K
*
5K
*
2. Period (CL 30)
6.5 K
*
5K
*
3. Period (HL 20)
8K
*
7K
*
4. Period (CL 40)
8K
9K
7K
8K
5. Period (HL10)
19K
23K
18K
25K
6. Period (CL 30)
27 K
30 K
30 K
42 K
Initial Condition
16
• no pressure reduction performed
Tab. 4.1:
Measured and Calculated Temperature Differences between Primary
and Secondary System in Test PKL III B4.3
For the temperature differences shown in table 4, the primary temperature is taken
from the upper plenum as calculated and measured, respectively, and the
secondary temperature (for the calculation the same as for the experiment)
Fig. 4.6) corresponds to the secondary saturation pressure.
Injections of small amounts of nitrogen
into a cold legthdo not affect heat transfer
th
to secondary side. For the 5" (hot leg injection) and 6 (cold leg injection) injection
periods, heat removal was too small to generate a stationary condition. This non
equilibrium resulted into an almost constant pressure increase. At the end of each
of both periods, secondary side pressure has been reduced in the experiment.
The first temperature difference corresponds to secondary side pressure before
reduction, the second temperature difference is the respective value after
pressure reduction. As primary side pressure follows the secondary side pressure,
the reduction of pressure in the primary system results into an extension of the
volume of inertness (passive area) in the steam generators. Therefore the
temperature difference between both systems is expected to be higher with a
lower pressure level.
In the following the RELAP5 results are compared to the measured values.
During steady state (before injection of N into the system) RELAP5 shows a lower
(50%) temperature difference between primary and secondary side (Fig. 4.7, 4K
calculated by RELAP5, 6K measured), although the total heat transferred to the
secondary side is calculated to be lower in RELAP5 than in the experiment
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(440 kW vs. 460 kW). This indicates a small overestimation of heat losses on the
primary side in the RELAP5 model.
For the first period (nitrogen injection of 0,25m 3 in 1 hr into HL1 0) RELAP5
calculates a small response of the system behavior (AT increase by 1K to 5K); the
measured system response cannot be clearly interpretated, because of the shown
anomalies (Fig. 4.6) but indicates almost no increase of the primary temperatures.
The RELAP5 results (AT increase) show that the decrease of heat transfer in
SG 10, because of nitrogen injection, cannot be compensated completely by the
remaining SGs (as in the experiment).
Both the experiment and RELAP5 show almost no influence of the nitrogen
during the 2nd
injection of 0,25m 2 N in 1 hr into CL30 on the system behavior
period.
In the 3rd period (0,25m 3 N in 5min into HL 20) RELAP5 shows a similar system
response to the nitrogen injection as measured (1,5K vs 2K).
In the 4th period with 0,25m 3 nitrogen injection in 5min into CL40 both RELAP5 and
the experiment show no system response. Experiment and RELAP5 define an
increase of 1K of the primary temperature after the depressurization.
During the 5" and 6t' period of nitrogen injection, RELAP5 and the experiment
show a continuous increase of primary pressure and consequently an increase of
the temperature difference primary to secondary side, which are terminated by the
secondary side depressurization.
4.5
Steam Generator Heat Transfer as a Function of Nitrogen
Distribution in the Primary System
The distribution of nitrogen and its influence on steam generator heat transfer was
analyzed. The heat transfer in the SG depends on the distribution of nitrogen in
the U-tubes.
In the RELAP5/Mod 3.2 calculation, the nitrogen accumulations in all relevant
components can be shown using control variables. These control variables serve
as a basis to analyse the nitrogen transport. The calculated nitrogen distribution is
depicted in Fig. 4.12 through 4.37 in comparison to the experimental values. The
nitrogen mass distribution of the experiment shown in the figures is estimated
from the test report description. Additional the heat transfer of the individual SGs
can be derived from the live steam flows, hence these values are proportional to
the heat transfer, when the level in the SG secondary side is kept constant by the
feedwater injection (see Fig. 4.38). The heat transfer in the SGs of the calculation
was derived directly via the heat flux parameters of the U-tubes (see Fig. 4.39).
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Consequently the calculated heat transfer of each SG can be compared with the
experiment. (Figures 4.40 through 4.43), based on the nominal heat transfer rate
in one SG of about 115 kW. When the heat transfer declines in a SG by
accumulation of nitrogen, the inertness is compensated by the increase of the
steam temperature in the primary system, which leads to a better heat transfer in
the SGs which are free from nitrogen.
Fig. 4.37 confirms a good agreement of the integral nitrogen inventory in the
system between experiment and calculation and the correctness of the boundary
conditions. Differences between calculated and measured heat transfer can be
explained via the calculated differences in nitrogen distribution.
1s' Nitrogen Iniection of 0,25m 3 into the Hot Leg of Loop 10 in lhr
The experiment shows the following: During the 1St nitrogen injection period
(Fig. 4.2) the heat transfer in SG 10 decreased (Fig 4.40) from the initial value to
20kW. The development of a passive area in the SG10 can be seen in Fig. 4.8
and 4.9. The total mass of 0,3kg N injected is accumulated in HL10 and in SG10
(Fig. 4.12 to 4.13). To preserve the total heat removal the heat transfer in the
other SGs increased (see Fig. 4.41 to 4.43) without a pressure and temperature
increase in the primary system (Figs 4.5, 4.6).
RELAP5 shows the following: The heat transfer in SG10 decreased from 110kW
to less than 10kW at 1200 sec (Fig. 4.40). This loss of total heat transfer of about
100kW (compared to approx. 40kW in the test) cannot be compensated by the
3 other SGs without a small temperature and pressure increase at the primary
side (Figs 4.5, 4.6). The evaluation of the nitrogen distribution shows that less N is
accumulated in SG1O compared to the experiment (Fig. 4.13). The increase of
pressure in the upper plenum and at the SG outlet leads to oscillatory loop seal
clearing (Fig. 4.44) and consequently to the N transport to the RCP
(Fig. 4.15, 4.16).
2nd
Nitrogen Iniection of 0,25 m3 into the Cold Leg of Loop 30 in 1hr
The experiment shows no significant change of heat transfer in all 4 SGs
(Figs 4.40 to 4.43) during the N injection. The nitrogen injected is accumulated in
the DC only (Fig. 4.36).
The RELAP5 calculation shows also no significant change in overall heat transfer.
SG10 recovers slightly around 8000 sec to about 40kW heat transfer (Fig. 4.40).
The nitrogen distribution calculated differs from the experimental results. RELAP5
calculates a nitrogen flow to the UPL and closure head (Fig. 4.36), which is an
indication of an underestimation of condensation in the pump region, resulting in
positive pressure difference CL to UPL and closure head.
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3rd Nitrogen Iniection of 0,25m 3 into the Hot Leg of Loop 20 in 5 min
The experiment shows a significant decrease of heat transfer in SG20 to 60kW
(down from 140kW) (Fig. 4.41). This decrease is compensated by a permanent
increase of heat transfer in SG30 from 160kW to about 230kW (Fig. 4.42). Beside
short peaks, SG10 and SG40 remain unaffected. The nitrogen accumulates
primarily in the SG20 and partly in the loop between SG20 outlet and loop seal.
The RELAP5 calculation shows a much stronger decrease of heat transfer down
to 0 in SG20 with a continuous recoverment thereafter (Fig. 4.41). SG30 and
SG40 show an increase from 140kW to 160kW and a continuous decrease
thereafter. SG10 shows a permanent increase of heat transfer from 40kW to
130kW (no increase in the test). Fig. 4.23 shows that not all injected nitrogen is
calculated to accumulate in the SG20, it partly flows towards the UPL. The
amount of nitrogen in SG20 decreases continuously (Fig. 4.20), thereby causing
an increase of heat transfer (Fig. 4.41).
4" Nitrogen Iniection of 0,25m3 into the Cold Leg of Loop 40 in 5 min
The experiment shows no significant change of heat transfer in any of the 4 SGs
before the depressurization (Figs 4.40 to 4.43). The secondary pressure decrease
leads to a temporary peak of heat transfer in all 4 SGs. The nitrogen is
accumulated in DC region only.
The RELAP5 calculation shows also no significant response of the system till the
depressurization. Only SG20 shows a significant reaction during the
depressurization. The nitrogen is calculated to accumulate first primarily in the DC
and partly in the UPL. Thereafter it is redistributed from the DC region into UPL
and the rest of the primary system (Fig. 4.36).
5" Nitrogen Injection of 1,5m 3 into the Hot Leg of Loop 10 in 1hr
The experiment shows no overall change in heat transfer during the injection
period (Figs 4.41 to 4.43). SG30 shows a decrease and a consecutive increase,
whereas SG40 shows in the same time period an increase and a decrease of
heat transfer. The actual decrease of heat transfer by condensation in the U-tubes
is compensated by a continuous increase of primary pressure and corresponding
saturation temperature (Fig. 4.5). The nitrogen accumulates in all 4 SGs in
parallel (Figs 4.13, 4.20, 4.27, 4.32). The pressure reduction creates similar
reactions like in period 4.
RELAP5 calculates a similar overall system response regarding the total heat
transfer and pressure increase in the primary system (Fig. 4.5 and 4.40 to 4.43).
SG10 looses completely its heat transfer capacity during the injection. SG20
reaches full capacity (up to 160kW) again and SG30 and SG40 increase also their
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heat transfer by 20kW. The nitrogen is calculated to increase in all 4 SGs similar
to the experiment.
6h Nitrogen Injection of 1,5m 3 into the Cold Leg of Loop 30 in 1 hr
The test shows a strong decrease of heat transfer in SG30 at 2400 sec down to
about 80kW. The other 3 SGs raise their heat transfer. The actual decrease in the
condensation rate in the SG U-tubes is compensated by a continuous increase of
primary pressure and corresponding saturation temperature. The nitrogen is
accumulated in all 4 SGs in parallel (Figs 4.13, 4.20, 4.27, 4.32).
The RELAP5 calculation shows a comparable result regarding the primary
pressure response (Fig. 4.5). SG20 and SG30 have a higher calculated heat
transfer compared to the test, whereas SG40 has a lower calculated value. The
nitrogen is calculated to increase in SG20, 30 and 40 but remains nearly constant
in SG10.
Conclusion
In this chapter we have discussed the nitrogen distribution in the PCL and the
influence on the heat transfer in the SGs during the 6 nitrogen injection periods.
Comparing the nitrogen distribution in the system between the experiment and the
RELAP calculation significant differences were shown in the results. In the RELAP
calculation, the nitrogen was accumulated at the measured locations but to a
different amount. The U-tubes of the SGs were calculated to receive enough inert
gas to influence the heat transfer as predicted in the experiment.
The overall heat transfer response is predicted by RELAP5 in a similar way
compared to the test. But differences are shown in the distribution of the heat
transfer among the SGs. In the experiment the heat transfer differs from 60 kW to
about 250 kW (Fig. 4.38), while in the RELAP calculation the heat transfer rate is
at a uniform level near 150 kW, but for the SGs with passive areas (Fig. 4.39).
4.6
Propagation of Nitrogen Concentration in the Steam Generator
U-Tubes
Based on the evaluation of the experiment for reflux condenser operation with a
hot injection of nitrogen, in the course of this test a front of high nitrogen
concentration is formed in the SGs, which moves through the SG from the outlet
chamber to the inlet chamber. An indication for this movement is the
measurement of fluid temperatures in the SG tubes (see Figs 4.8 to 4.11),
because steam temperature in this region decreases according to the partial
pressure. In the evaluation the presence of nitrogen in the U-tubes of the SGs has
been verified in this manner.
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As described in chapter 4.5 the heat transfer in SG 10 and SG 20 did not exactly
correspond with the prediction of the experiment. These SGs were effected by hot
leg nitrogen injection during the periods 1 and 3. In the experiment they showed a
constant heat transfer of about 10 kW resp. 60 kW after the 3rd injection period
(Figs 4.40, 4.41). In the RELAP analysis, SG 10 was activated again when
nitrogen was injected into the hot leg of loop 20 and the heat transfer in SG 20
collapsed totally. Later on, in SG 20 the heat transfer increased continuously to
about 150 kW after the termination of the 3rd nitrogen injection.
This calculated increase of the heat transfer in the RELAP5/Mod 3.2 analysis is
not shown in the experiment and should be analysed closer. As the phenomena in
each U-tube are similar, only results of the longest tube of SG 10 and 20 are
presented here.
When condensation takes place in the U-tubes, heat is transferred to the
secondary side. Another criterion for heat transfer is the temperature difference
between the steam in the U-tubes and the secondary side of a SG. In figures 4.8
through 4.11 steam temperatures and secondary side temperatures are depicted
for the ascending and descending U-tubes. The temperature differences confirm
the heat transfer shown by the steam condensation in the figures 4.49 and 4.50.
Furthermore the temperature differences between the saturation temperatures
and the steam temperatures in figures 4.8 through 4.11 indicate the presence of
nitrogen in the U-tubes as predicted in the experiment.
Figures 4.49 and 4.50 of the RELAP calculation show the generation of
condensate in the respective SG for the ascending and descending U-tubes. As
predicted in the test, the condensate generation in the descending part decreased
earlier than in the ascending tubes, caused by concentration of nitrogen during
condensation of steam and by the flow of nitrogen from the ascending part to the
descending part together with steam.
At 1000 s, generation of condensate in the descending U-tubes of the SG 10
(Fig. 4.49) has been stopped totally by reaching a saturated state of the mixture.
At 4000 s in SG 10 the nitrogen inventory in the descending part decreased while
it was constant in the ascending tubes (RELAP calculation, Fig 4.17). The reason
for this behavior shows the integral nitrogen flow at the inlet and outlet of pipe 320
(RELAP calculation, Fig. 4.18). Nitrogen that flowed to the loop seal (RELAP
calculation, Fig. 4.14) has been withdrawn from the ascending U-tubes. The same
behavior of the RELAP calculation showed SG 20 at 11500 s (Figs 4.24, 4.25).
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Therefore the heat transfer behavior calculated by RELAP5 of SG10 and SG20
after nitrogen injection into their corresponding hot legs can be explained by the
nitrogen transport out of the SG U-tubes into SG outlet and the adjacent loop.
In the experiment the nitrogen obviously remains in the U-tubes of the affected
SG (see Figs 4.13, 4.14 and 4.20, 4.21).
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23
Conclusions
The PKL Ill test facility simulates a typical 1300 MWe pressurized water reactor of
Siemens/KWU design. In Test B4.3, the influence of non-condensables on reflux
condenser conditions was investigated.
This report presents a post-test analysis of PKL III B4.3 using RELAP5/Mod 3.2.
A description of the input model is given, and the correspondence of measured
and calculated results is discussed.
The main findings of the comparison of RELAP5/Mod 3.2 results with the PKLIII
B4.3 experiment are as follows:
The general system response (pressure, temperature) of nitrogen injection in the
primary system is calculated by RELAP5/Mod3.2 quite well. In a detailed
evaluation RELAP5 calculates a non conservative behavior of heat transfer for
small nitrogen injections effecting a particular SG. This statement can be
concluded from the course of the heat transfers in the SGs 10 and 20 ( see
chapter 4.5 and 4.6).Thus a too large calculated heat removal from the primary
system underestimates the effect of nitrogen on the emergency core cooling in
loss of coolant accidents. When the steam flow of the reflux condenser operation
is terminated in a SG caused by inertness, less nitrogen of the injection is
transported to the SG U-tubes. For this reason first a smaller nitrogen inventory in
the U-tubes of a SG has been calculated to accumulate as predicted in the
experiment and later on the nitrogen has been calculated to leave the SG
(chapter 4.6).
Looking at the figures of the transient, it is shown that RELAP calculates small
fluctuations which transport nitrogen in the system without physical background.
In a long term behavior, because of this numerical instability RELAP will predict
a homogenous distribution of the nitrogen in the primary system.
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References
/1/
K. Umminger et al
Station Blackout Experiment in PKLIII Test Facility and RELAP5/MOD2
Analyses
ICONE-3, Kyoto Japan, April 1995
/2/
P. Weber et al.
PWR-Related Integral Safety Experiments in the PKLIII Test Facility
SBLOCA under Beyond-Design-Basis Accident Conditions
NURETH-7 Saratoge Springs, USA. Sept 95
/3/
B. Schoen, P. Weber
Large Scale Experiment on Two-Phase Flow and Heat Transfer with
Nitrogen in a Steam Generator under SBLOCA Conditions
Int. Symposium on Two-Phase Flow Modelling and Experimentation
Rome, Italy, Oct. 1995
/4/
Idaho National Engineering Laboratory
RELAP5/MOD3 Code Manual
NUREG/CR-5535 INEL-95/0174 Vol. I - VII
"The
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List of Figures
Fig. Text
2.1
2.2
2.3
4.1
4.2
4.3
4.4
4.5
4.6
4.7
4.8
4.9
4.10
4.11
4.12
4.13
4.14
4.15
4.16
4.17
4.18
4.19
4.20
4.21
4.22
4.23
4.24
4.25
4.26
4.27
4.28
View of PKLIII Test Facility
Cross-Sectional View of a PLK Ill Steam Generator
Axial Locations of Thermocouples in SG tubes
Nodalization of the PKL III Test Facility with Respect to the B 4.3 Experiment
Nitrogen Injection Rate into Hot Legs 10 (X) and 20 (- -)
Nitrogen Injection Rate into Hot Legs 30 (X) and 40 (- -)
Secondary System Pressure RELAP (X), Experiment (+)
Primary Pressure RELAP (X), Experiment (Z), Secondary Pressure RELAP (+),
Experiment (Y)
Primary Temperature RELAP (X), Experiment (Z), Secondary Temperature
RELAP(+), Experiment(Y)
Temperature Difference Primary-Side - Secondary-Side RELAP(X), Experiment(+)
Fluid Temperature SG 10, Ascending U-tubes RELAP(X), Experiment(+),
Level 0.3m, Saturation Temperature Secondary Side(Z),
Saturation Temperature Primary Side(Y)
Fluid Temperature SG 10, Descending U-tubes RELAP(X), Experiment(+),
Level 0.3m, Saturation Temperature Secondary Side(Z),
Saturation Temperature Primary Side(Y)
Fluid Temperature SG 20, Ascending U-tubes RELAP(X), Experiment(+),
Level 0.3m, Saturation Temperature Secondary Side(Z),
Saturation Temperature Primary Side(Y)
Fluid Temperature SG 20, Descending U-tubes RELAP(X), Experiment(+),
Level 0.3m, Saturation Temperature Secondary Side(Z),
Saturation Temperature Primary Side(Y)
Nitrogen Mass Loop 10 Hot Leg + SG Inlet
Nitrogen Mass Loop 10 Steam Generator U-tubes
Nitrogen Mass Steam Generator 10 Outlet to Half Loop Seal
Nitrogen Mass Loop 10 Half Loop Seal to RPV Inlet
Integrated Nitrogen Injection Loop 10 Hot Leg(Z), SG-Side(X), RPV-Side(+)
Nitrogen Mass SG 10, Pipe 320 Ascending(X), Descending(+) U-tubes
Integrated Nitrogen Mass Flow SG 10, Pipe 320 Inlet(X), Outlet(+)
Nitrogen Mass Loop 20 Hot Leg + SG Inlet
Nitrogen Mass Loop 20 Steam Generator U-tubes
Nitrogen Mass Steam Generator 20 Outlet to Half Loop Seal
Nitrogen Mass Loop 20 Half Loop Seal to RPV Inlet
Integrated Nitrogen Injection Loop 20 Hot Leg(Z), SG-Side(X), RPV-Side(+)
Nitrogen Mass SG 20, Pipe 420 Ascending(X), Descending(+) U-tubes
Integrated Nitrogen Mass Flow SG 20, Pipe 420 Inlet(X), Outlet(+)
Nitrogen Mass Loop 30 Hot Leg + SG Inlet
Nitrogen Mass Loop 30 Steam Generator U-tubes
Nitrogen Mass Steam Generator 30 Outlet to Half Loop Seal
Siemens AG • Power Generation Group
L:\Kamerkpkl3b43_wr_r5m3.2_my.doc
H30-K5314 Bericht KWU, engl. 4.94 D
The reproduction, transmission or use of this document or its contents is not
permitted without express written authority. Offenders willbe liable for
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(KWU)
of autillity model or design, are reserved.
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4.29
4.30
4.31
4.32
4.33
4.34
4.35
4.36
4.37
4.38
4.39
4.40
4.41
4.42
4.43
4.44
4.45
4.46
4.47
4.48
4.49
4.50
Page
26
Nitrogen Mass Loop 30 Half Loop Seal to RPV Inlet
Integrated Nitrogen Injection Loop 30 Cold Leg(Z), RPV-Side(X), SG-Side(+)
Nitrogen Mass Loop 40 Hot Leg + SG Inlet
Nitrogen Mass Loop 40 Steam Generator U-tubes
Nitrogen Mass Steam Generator 40 Outlet to Half Loop Seal
Nitrogen Mass Loop 4 Half Loop Seal to RPV Inlet
Integrated Nitrogen Injection Loop 40 Cold Leg(Z), RPV-Side(X), SG-Side(+)
Nitrogen Mass Closure Head and UPL (X), DC(+), LPL Core and Core-Bypass(Z)
Nitrogen Mass Primary System RELAP(X), Injected Nitrogen Mass(+)
Heat Transfer Experiment SGs 10(X), 20(+), 30(Z), 40(Y)
Heat Transfer RELAP (smoothed) SG 10(X), 20(+), 30(Z), 40(Y)
Heat Transfer SG 10 Experiment(X), RELAP(+)
Heat Transfer SG 20 Experiment(X), RELAP(+)
Heat Transfer SG 30 Experiment(X), RELAP(+)
Heat Transfer SG 40 Experiment(X), RELAP(+)
Collapsed Level Loop Seal 10 SG-Side RELAP(X), Experiment(+)
Collapsed Level Loop Seal 20 SG-Side RELAP(X), Experiment(+)
Collapsed Level Loop Seal 30 SG-Side RELAP(X), Experiment(+)
Collapsed Level Loop Seal 40 SG-Side RELAP(X), Experiment(+)
Collapsed Level RPV RELAP Core(X), DC(+); Experiment Core(Z), DC(Y)
Condensate Generation SG 10, Pipe 320 Ascending(X), Descending(+) U-tubes
Condensate Generation SG 20, Pipe 420 Ascending(X), Descending(+) U-tubes
Siemens AG - Power Generation Group (KWU)
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27
Figures
Siemens AG - Power Generation Group (KWU)
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H30-K5314 Bericht KWU, engl. 4.94 D
reproduction, trassttIssion or use of this document or its contents is not
The
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Abb. 2.1: View of PKLIII Test Facility
Siemens AG • Power Generation Group (KWU)
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Page
00
E
A
thermocouple SG tube
Fig. 2.2:
Cross-Sectional View of a PKL III Steam Generator
Siemens AG - Power Generation Group (KWU)
L:\Kamer\pk13b43_wr.r5m3.2-my.doc
H30-K5314 Bericht KWU, engl. 4.94 D
replacement bodies
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Page
30
Hohe [mmI
Ebenez
10310
9975
9635
9300
8965
8625
8 290
MIA
6 700
VtA
5000
HIA
VJA
2880
2 000
1 300
G/A
F/A
E/A
"700
D/A
300
150
0
CIA
B/A
A/A
tf
Etntfitf
Austritt
Fig. 2.3: Axial Locations of Thermocouples in SG tubes
Siemens AG -Power Generation Group (KWU)
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permitted without express written authority. Offenders willbe liable for
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of a utillity model or design, are reserved.
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Fig. 4.1 :Nodalization of the PKL Ill Test Facility with Respect to the B 4.3 Experiment
Siemens AG • Power Generation Group (KWU)
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H30-K5314 Bericht KWU, engl. 4.94 D
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permitted without express written authority. Offenders willbe liable for
damages. All rights, including rights created by patent grant or registration
of a utillity model or design, are reserved.
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wie auf Titelseite bzw. erster Seite angegeben
0
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This document Is subject to the restrictions
set forth on the first or title page
25. 5.98
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d
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Comparison of Experiment and Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.2: Nitrogen Injection Rate into Hot Legs 10(X) and 20(--)
4. c. lea 40
16
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25. 5.98
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Comparison of Experiment and Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.3: Nitrogen Injection Rate into Cold Legs 30(X) and 40(- -)
2
22
24
dp
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26
28
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*103
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set forth on the first or title page
25.5.98
6:43: 4
DOKU.980513.1842.14668
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Data b4_3 -- RELAP5/Mod3.2
Fig. 4.4: Secondary System Pressure RELAP(X), Experiment(+)
16
18
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1 '214 ' 1 '216'
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1 '218
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6. c. leg 30
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25.5.98
6:43: 5
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Data b4_3 -- RELAP5/Mod3.2
Fig. 4.5: Primary Pressure R(X), Exp.(Z), Secondary Press. R(+), Exp.(Y)
16
18
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set forth on the first or title page
25.5.98
6:43: 6
DOKU.980513.1842.14668
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16
4. c. leg 40
Comparison of Experiment and Analysis PKIL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.6: Primary Temperature R(X), Exp.(Z), Second. Temp. R(+), Exp.(Y)
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25. 5.98
6:43: 6
SDOKU.980513.1842.14668
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....
....
..
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2. c. leg 30
-
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16
18
-- p
4. c. leg 40
Comparison of Experiment and Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4,7: Temperature Diff. Primary-S. - Secondary-S. R(X), Exp.(+)
2ý
22
24
28
26
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dp
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z:D
This document Is subject to the restrictions
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25.5.98
8:40:29
"Q-rCD
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16
18
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' ' Th
2?
'
I
22
24
dp
1. h. leg 10
2. c. leg 30
3. h. leg 20
4. c. leg 40
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.8: SG 10 Asc. U-Tubes R(X), Exp.(+), Satt-sec(Z), Satt-pr(Y)
5. h. leg 10
*103
26
dp
6. c. lec 30
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Uo
z
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25.5.98
8:40:30
DOKU.980513.1842.14668
(C)
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185
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180
175
170
165
160
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12
Time
s)
14ts
3. h. leg 20
4. c. leg 40
0
16
18
"*103
2T?
dp
1. h. leg 10
2. c. leg 30
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.9: SG 10 Desc. U-Tubes R(X), Exp.(+), Satt-sec(Z), Satt-pr(Y)
5. h. lea 10
5. h, lea 10
dp
6 r Inn .10
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25. 5.98
8:40:25
DOKU.980513.1842.14668
a:
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18
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1. h. lea 10
z
2. c. lea 30
3. h. lea 20
4. c. lea 40
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.10: SG 20 Asc. U-Tubes R(X), Exp.(+), Satt-sec(Z), Satt-pr(Y)
2T
22
24
dp
5. h. lea 10
26
1 28
dp
6. c. leg 30
"*103
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C')
0
This document is subject to the restrictions
set forth on the first or title page
25. 5.98
8:40:26
DOKU.980513.1842.14668
0
5.Q
Temperature (C)
200
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..............
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165 . ............................................
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...........
155 . ...........................
150-.
0
.
o0
I
2
4
6
8
10
12
Depress. dp
N Injection
14
Time ýs)
16
18
0
1. h. leg 10
2. c. leg 30
3. h. leg 20
4. c. leg 40
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.11: SG 20 Desc. U-Tubes R(X), Exp.(+), Satt-sec(Z), Satt-pr(Y)
2
dp
5. h. leg 10
22
26 128
24
_o
6. c. leg 30
dp
"*103
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U)
0
z
This document is subject to the restrictions
set forth on the first or title page
25.5.98
7:18:11
(D
DOKU.980513.1842.14668
0
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Mass (kg)
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I
141
1. h. leg 10
2. c. leg 30
3. h. leg 20
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.12: Nitrogen Mass Loop 10 Hot Leg + SG Inlet
dap
4. c. leg 40
16
18
Do
5Sh.ieg 10
24
dp
26
28
dp
6. c. leg 30
*103
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z
This document is subject to the restrictions
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25.5.98
7:18:28
D
DOKU.980513.1842.14668
Mass (kg)
1.0 ..............
JJ
X
CD
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0
0..
CD
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0 .8 . .................
C
CL
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m
0
0.6.
0.4.
0.2
Co
5D
4h.
0.0-
r
0
i
2
16
18
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N Injection
*103
2b
dp
1. h. leg 10
2. c. leg 30
3. h. leg 20
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.13: Nitrogen Mass Loop 10 SG U-Tubes
4. c. leg 40
5. h. leg 10
dp
6. c. leg 30
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25.5.98
7:18:28
CD
DOKU.980513.1842.14668
CL
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0
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.........................
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11',I
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N Injection
,11
Time (p)
--
4. c. leg 40
5. h. leg 10
dap
1. h. leg 10
2. c. leg 30
3. h. leg 20
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.14: N Mass SG 10 Outlet to half Loop Seal
,'18
21
*103
dlp
dp
6. c. leq 30
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25. 5.98
7:18:28
DOKU.98051 3.1842.14668
Z
Q~0
t
CD0 Z
C0
m
0
4-U
CD
01
6
8
10
12
Depress. dp
N Injection
2. c. leg 30
3. h. leg 20
Comparison of Experiment und Analysis PKL Ill B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.15: N Mass Loop 10 half Loop Seal to RPV Inlet
141
Time_,S)
I_
4. c. leg 40
*103
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U)
0
z
This document is subject to the restrictions
set forth on the first or title page
25.5.98
7:47:58
(D
DOKU.98051 3.1842.14668
_0
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Mass (kg)
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CD
0)
0,
. .. .-, -
1. h. tea 10
dp
2. c. leo 30
3.
h. lea 20
4.
Ien4fl
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.16: Int. N Injection L. 10 Hot Leg(Z), SG-Side(X), RPV-Side(+)
I, Ion IA
dp
*103
This document is subject to the restrictions
set forth on the first or title page
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i)
0
25.5.98
7:48:44
(D
_0
DOKU.98051 3.1842.14668
(0
Mass (kg)
0.09-1
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..........
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CD
0.08
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....
............................
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C
z
(0
0.07
....................
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0.05
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0.04
0.03
0.02
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4T-
0.00
6
8
10
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N Iniection
12
__
14
*103
)
_ Times)
dp
2dp
1. h. leg 10
2. c. leg 30
3. h. leg 20
4. c. leg 40
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.17: N Mass SG 10, Pipe 320 Ascending(X), Descending(+) U-Tubes
5. h. leg 10
dp
6. c. lel 30
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25.5.98
7:48:56
DOKU.980513.1842.14668
CL
CD
0
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.................................................................................
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z
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C
V.
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RILkAP Calculation
-C
0)2
CoB
!
C°
2
4
6
8
12
10
1'6
'
1'8
'
'2
Tim24ceg)
Depress. dp
N Injection
-
T1e s
22
I .2
14- I 2 16 1 '2
dp
1. h. leQ
v 10
2. c. leg 30
3. h. leg 20
4. c. leg 40
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.18: Integr. N Mass Flow SG 10, Pipe 320 Inlet(X), Outlet(+)
5. h. leg 10
dp
6. c. lea 30
*103
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25.5.98
7:18:29
n DOKU.980513.1842.14668
,C
CL
Mass
0.5(kg)
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0.45........................
.....
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0.05
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S i
i
4
6
,
RiELAP
8
i,
10
Depress. dp
N Injection
•
2. c. leg 30
12
3. h. leg 20
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.19: Nitrogen Mass Loop 20 Hot Leg + SG Inlet
,
141
Time ()
d
4. c. leg 40
16
18
2ý
Idp
dp
5. h. leg 10
(
.............
•.......................•..... ...................
.;................
...........
Experimnent: no N'Acoumulation
1. h. leg 10
••
•4
22
24
26
J 28
dp
6. c. leg 30
"103
e
This document is subject to the restrictions
set forth on the first or title page
Dieses Blatt unterliegt den Weitergabebeschr-nkungen
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z
25.5.98
7:18:29
"Z3CD
DOKU.98051 3.1842.14668
5..
0
Co
Mass (kg)
..................
...........
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..........
CD
z
0
CL
C
0.8
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z
... .. ........................... { . .................... ... ........ ................... .
4o
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0.6
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0.4
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0
0.
2
4
6
8
10
S'
I '
12
'I
141
Timeis)
''
16
'
-
18
1. h. leg 10
2. c. leg 30
3. h. leg 20
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.20: Nitrogen Mass Loop 20 SG U-Tubes
4. c. leg 40
'
I
"*103
D
dp)
Depress. dp
N Injection
'
dp
dp
5. h. leg 10
6. c. leg 30
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25.5.98
7:18:29
-r
z
3ý
DOKU.980513.1842.14668
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2
4
6
8
10
12
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N Injection
.
. ...........................
........................... ............................
.......................................................
14/
Tie
1. h. leg 10
2. c. leg 30
3. h. leg 20
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.21: N Mass SG 20 Outlet to half Loop Sea[
16
18
p•
4. c. leg 40
2ý
22
24
dp
5. h. leg 10
26
28
dlp
6. c. leg 30
*103
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This document is subject to the restrictions
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25.5.98
7:18:30
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2. c. leg 30
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Comparison of Experiment und Analysis PKL IIl B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.22: N Mass Loop 20 half Loop Seal to RPV Inlet
4. c. leg 40
212
214
dp
d
N Injection
21
5. h. leg 10
216
28
dp
6. c. leg 30
*103
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2. c. leg 30
3. h. leg 20
141
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4. c. leg 40
Comparison of Experiment und Analysis PKIL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.23: Int. N2 Injection L. 20 Hot Leg(Z), SG-Side(X), RPV-Side(+)
I '
16
I
18
,
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22
24
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i
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6. c. leg 30
28
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25.5.98
7:49:19
a)
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-
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3. h. leg 20
16I
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4. c. leg 40
Comparison of Experiment und Analysis PKL IIl B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.24: N Mass SG 20, Pipe 420 Ascending(X), Descending(+) U-Tubes
*103
It
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6. c. leg 30
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25. 5.98
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Comparison of Experiment und Analysis PKL III B 4.3
'
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24
1 28
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dp
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26
6. c. leg 30
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This document is subject to the restrictions
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25.5.98
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18
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Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.26: Nitrogen Mass Loop 30 Hot Leg + SG Inlet
4. c. leg 40
CA
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2ý
22
24
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26
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6. c. leg 30
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£/
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This document is subject to the restrictions
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25.5.98
7:18:30
DOKU.980513.1842.14668
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2. c. leg 30
3. h. leg 20
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.27: N Mass Loop 30 SG U-Tubes
4. c. leg 40
16
18
0
5. h. leg 10
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6. c. leq 30
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25.5.98
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DOKU.980513.1842.14668
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Comparison
-- of
Experiment und Analysis PKL III B 4.3
Comparison
Data b43N Mass
4.28:
Data
Fig. b4_3 -- RELAP5/Mod3.2
Fig. 4.28: N Mass SG 30 Outlet to half Loop Seal
Depress. dp
N
,
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25.5.98
7:18:31
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16141AK'~hM
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2. c. leg 30
3. h. leg 20
Comparison of Experiment und Analysis PKIL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.29: N Mass Loop 30 half Loop Seal to RPV Inlet
4. c. leg 40
,118
21
W
dp
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L
24
26 I
dp
6. c. leg 30
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25.5.98
7:47:59
"I"
DOKU.98051 3.1842.14668
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2. c. leg 30
3. h. leg 20
4. c. leg 40
Comparison of Experiment und Analysis PKL III B 4.3
Data M4_3 -- RELAP5/Mod3.2
Fig. 4.30: Int. N Injection L. 30 Cold Leg(Z), RPV-Side(X), SG-Side(±)
5. h. leg 10
6. c. leg 30
1 28
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25.5.98
7:18:31
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2
4
6
8
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16
12
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Depress. dp
N Injection
..
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2. c. leg 30
3. h. leg 20
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.31: Nitrogen Mass Loop 40 Hot Leg + SG Inlet
4. c. leg 40
XI
I
1
2?
1
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22
'
1
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I
24
'
1
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26
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1 28
dp
dp
5. h. lea 10
,
6. c. leq 30
"*103
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set forth on the first or title page
25.5.98
7:18:32
"I
DOKU.98051 3.1842.14668
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0.0
6
N Injection
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Time js)
Depress. dp
4 dp
1. h. leg 10
2. c. leg 30
3. h. leg 20
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.32: Nitrogen Mass Loop 40 SG U-Tubes
dp
S hr Ig~n 10
4 c Ian 40
5 h le 10
dp
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25.5.98
7:18:32
"-rJ
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DOKU.980513.1842.14668
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Mass (kg)
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N Injection
1. h. leg 10
2. c. leg 30
3. h. leg 20
Comparison of Experiment und Analysis PKL Ill B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.33: N Mass SG 40 Outlet to half Loop Seal
2'8
141
Tim es)
4. c. leg 40
dp
dp
5. h. leg 10
6. c. leg 30
-103
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25.5.98
7:18:32
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Depress. dp
N Injection
22
14|
dp
1dp
1.h.iegl10
2.c.Ileg 30
3. h.leg 20
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.34: N Mass Loop 40 half Loop Seal to RPV Inlet
4. c. leg 40
24
5. h. leg 10
26
28
dp
6. c. lea 30
-103
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25.5.98
7:47:59
a
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DOKU.98051 3.1842.14668
Mass (kg)
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4. c. lea 40
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.35: Int. N Injection L. 40 Cold Leg(Z), RPV-Side(X), SG-Side(+)
'
I
*103
2?
dp
1dp
1.h. lec 10
I
5. h. lea 10
dp
6. c. lea 30
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25.5.98
7:18:57
DO
CD
DOKU.980513.1842.14668
Mass (kg)
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2. c. leq 30
3. h. leq 20
4. c. lea 40
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.36: N Mass Closure Head and UPL(X), DC(+), LPL Core and Byp.(Z)
5. h. lea 10
6. c. lea 30
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7:19:1
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Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.37: N Mass Primary System RELAP(X), Injected N Mass(+)
22
24
5. h. leg 10
*103
26'
dp
dp
Depress. dp
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2?
6. c. leg 30
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z
This document is subject to the restrictions
set forth on the first or title page
25.5.98
6:55: 4
DOKU.980513.1842.14668
CL
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6
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2. c. leg 30
3. h. leg 20
4. c. leg 40
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/M0d3.2
Fig. 4.38: Heat Transfer Experiment SGs 10(X), 20(+), 30(Z), 40(Y)
dp
5. h. leg 10
dp
6. c. leg 30
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0)
0
z
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set forth on the first or title page
25. 5.98
6:43: 7
CL
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Power (kW)
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Comparison of Experiment and Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.39: Heat Transfer RELAP (smoothed) SG 1O(X), 20(+), 30(Z), 40(Y)
2ý
-214
dp
dp
5. h. leg 10
216.128
6. c. leg 30
Co
*103
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zD
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This document is subject to the restrictions
set forth on the first or title page
25.5.98
6:55: 5
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DOKU.980513.1842.14668
0
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2. c. leg 30
3. h. leg 20
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/M0d3.2
Fig. 4.40: Heat Transfer SG 10 Experiment(X), RELAP(+)
14ý
Tim (s
4. c. leg 40
16
18
)_
5. h. leq 10
28
2
_
dp
6. c. leq 30
"103
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Cl:
0
z
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set forth on the first or title page
25.5.98
6:55: 5
CD
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4.3
PKL III B
Experiment
undofAnalysis
Comparison
RELAP5/M0d3.2
-B 4.3
und Analysis PKIL III RELAP(+)
Comparison of Experiment
b4_3
Data
Transfer
Experiment(X),
Heat
20
Data b4_3 -- RELAP5/MOd3.2
Fig.4.41"
SG
Fig. 4.41: Heat Transfer SG 20 Experiment(X), RELAP(+)
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,
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141
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16
18
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2
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0)
0
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This document is subject to the restrictions
set forth on the first or title page
25.5.98
6:55-:5
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DOKU.980513.1 842.14668
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180
160
140
120
100-
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2
4
6
10
12
16
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141
2. c. leq30
3. h.lea 20
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/MOd3.2
Fig. 4.42: Heat Transfer SG 30 Experiment(X), RELAP(+)
4. c. lecg40
22
24
5. h. lea 10
26
dp
dp
1p
1. h.leal10
2ý
6. c. lea 30
This document is subject to the restrictions
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0
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25.5.98
6:55: 5
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•
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v
3. h. leg 20
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Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/M0d3.2
Fig. 4.43: Heat Transfer SG 40 Experiment(X), RELAP(+)
4. c. leg 40
'
2I,'
22
24
dp
5. h. leg 10
"*103
26
dp
6. c. leg 30
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:D
This document is subject to the restrictions
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25.5.98
7:19:1
'I
DOKU.98051 3.1842.14668
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_
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.44: CL Loop-Seal 10 SG-Side RELAP(X), Experiment(+)
I
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16
18
27
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22
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24
26
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5. h. lea 10
F
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28
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6. c.
lea 30
i
*103
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set forth on the first or title page
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wle auf Titelseite bzw. erster Seite angegeben
25.5.98
7:19: 1
CD
M
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2. c. leg 30
3. h. leg 20
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.45: CL Loop-Seal 20 SG-Side RELAP(X), Experiment(+)
4. c. leg 40
16
18
28
2
dp
dp
dp
- p
5. h. leg 10
6. c. leg 30
"103
Dieses Blatt unterliegt den Weitergabebeschr~nkungen
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t
This document is subject to the restrictions
set forth on the first or title page
25.5.98
7:19:1
:IJ
CD
DOKU.98051 3.1842.14668
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Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.46: CL Loop-Seal 30 SG-Side RELAP(X), Experiment(+)
4. c. leg 40
26
2
dp
5. h. leg 10
i 28
dp
6. c. leq 30
.10
3
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25.5.98
7:19:2
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DOKU.980513.1842.14668
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8
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16
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3. h. leg 20
Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.47: CL Loop-Seal 40 SG-Side RELAP(X), Experiment(+)
22
24
dp
_
1. h. leg 10
2ý
4. c. leg 40
5. h. leg 10
26
28
dp
6. c. leg 30
*103
This document is subject to the restrictions
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Comparison of Experiment und Analysis PKL III B 4.3
Data b4_3 -- RELAP5/Mod3.2
Fig. 4.48: RPV RELAP Core(X), DC(+); Experiment Core(Z), DC(Y)
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This document is subject to the restrictions
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U.S. NUCLEAR REGULATORY COMMISSION
NRC FORM 335
(2489)
NRCM 110GD
3201,3202
1. REPORT NUMBER
(Assigned by NRC, Add Vol., Supp., Rev.,
and Addendum Numbers, Ifany.)
BIBLIOGRAPHIC DATA SHEET
(See inshocb= on the revee)
NUREG/iA-0170
2. TITLE AND SUBTITLE
RELAP5/MOD3.2
Post Test Calculation of the PKL-Experiment
PKLIII-B4.3
3.
DATE REPORT PUBLISHED
3.__DATEREPORT__PUBLISHED
j
MONTH
November
YEAR
1999
4. FIN OR GRANT NUMBER
5. AUTHOR(S)
L. Karner
6. TYPE OF REPORT
Technical
7. PERIOD COVERED (InclusiveDaebs)
8. PERFORMING ORGANIZATION - NAME AND ADDRESS (ff NRC, provide Division, Office orRegion, U.S. NuclearRegulatory Commission,and malting addrss;if contractor,
provide name and mailing address.)
Siemens Energierzeugung (KWU)
Freyerslebenstrasse 1
D-91058 Erlangen
Germany
9. SPONSORING ORGANIZATION - NAME AND ADDRESS IfNRC, type "Seneas above'; ifconhw.acor, provideNRC Division, O•ft& or Region, U.S. NuckeerRegu/afor, Commission,
and mailingaddress)
Division of System Analysis and Regulatory Effectiveness
Office of Nuclear Regulatory Research
U.S. Nuclear Regulatory Commission
Washington, DC 20555-0001
10. SUPPLEMENTARY NOTES
11. ABSTRACT (20o words or-ess)
The PKL III test facility (Primar-Kreis-Lauf) simulates a typical 1300 MWe Pressurized Water Reactor of Siemens/KWU. In test
B4.3, the influence of non-condensables on heat transfer inthe steam generators during reflux condenser conditions was
investigated. This report presents the results of a post-test analysis of PKL 11I-B4.3 using RELAPS/MOD 3.2. A description of the
input model is given, and the correspondence of measured and calculated results is discussed.. The results of the calculation
show differences inthe distribution of nitrogen inthe primary system compared to the experiment When nitrogen was injected into
the hot leg of the primary system, the heat transfer in the affected steam generator decreased. In contrast to the experiment
RELAP calculated that the volumes in the adjacent steam generator did not get the full amount of nitrogen and that nitrogen was
transported from the steam generators to other locations during the course of the transient Thus, the heat transfer in these steam
generators later increased in contradiction to the measured values. In the steam generator tubes, RELAP calculated that the
nitrogen accumulated in the descending part as predicted in the experiment For the ascending U-tubes RELAP predicted that the
nitrogen was transported to the loop seal, which was not seen in the experiment Fluctuations occurred during the course of the
RELAPS/MOD 3.2 analysis of the PKLIII 134.3 experiment This phenomenon may be the main reason, that RELAP calculates the
transport of nitrogen from the steam generators into the system and predicts finally a homogeneous distribution of nitrogen in the
primary system. The analysis performs an in kind contribution to the CAMP contract
12. KEY WORDS/DESCRIPTORS (Ust words orphrasesthat will assistresearchers in locating Yeraport
13. AVAILABILITY STATEMENT
unlimited
PKL III Test Facility
PWR
non-condensables
steam-generator
RELAP5/MOD3.2
14. SECURITY CLASSIFICATION
(This Rge)
unclassified
(This Repor)
unclassified
15. NUMBER OF PAGES
16. PRICE
NRC FORM 335 (2-89)
Federal Recycling Program
NUREG/IA-O0170
fI,AIS/M(-j)3.2 V'OS'TTfEI
Rl
UNITED STATES
NUCLEAR REGULATORY COMMISSION
WASHINGTON, DC 20555-0001
OFFICIAL BUSINESS
PENALTY FOR PRIVATE USE, $300
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