12.11. Input Description¶
Table 12.11.1 lists the input information that is needed in order to run the voiding model section of the SASSYS-1 and SAS4A Codes. This information is of two types: that used directly in the voiding calculation and that used by models which provide necessary input to the voiding model. This listing is a subset of the full input listing given in Section 12.16. To simplify the discussion of the information displayed in Table 12.11.1, the input variables will not be examined in the order presented in the table, but rather, they will be presented in groups of data by category, i.e., all variables pertaining to materials properties will be discussed together, all which give problem geometry information will be grouped together, etc. This discussion should be helpful to users trying to assemble input decks for running their own problems.
The variables which provide information on materials properties will be
described first. Most materials-property information, other than that
for sodium, is provided through input rather than being fixed within the
code in order to allow greater flexibility in the use of SASSYS-1. In
most cases, this information is input in the form of tables; however, in
the case of the solid fuel density and fuel thermal conductivity, either
tables or coefficients for functional relationships can be entered. The
choice between these two options is made on a channel-by-channel basis
and is flagged by the variable IRHOK
; a positive value of
IRHOK
indicates that the functional form has been selected, and a
non-positive value means that the tabular format has been chosen. The
variable COEFDS
contains the coefficients for the fuel
density relationship as a function of temperature, while RHOTAB
contains a
table of fuel density as a function of temperature
RHOTEM
. Similarly, the coefficient for the thermal
conductivity function can be read into COEFK
, while a
table of thermal conductivity values can be used in XKTAB
together with a table of temperatures in XKTEM
. In addition, the
specific heat of the fuel is read into the
table CPFTAB
as a function of temperature CPFTEM
.
Equation Variable |
Reference Equation |
Input Variable |
Suggested Value |
External Reference |
---|---|---|---|---|
- |
- |
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\(\rho_{f}\) |
- |
\(11.08 x 10^{3}\) \(2.04 x 10^{-5}\) \(8.7 x 10^{-9}\) |
- |
|
\(k_{f}\) |
- |
\(2.1\), \(2.88 x 10^{-3}\) \(2.52 x 10^{-5}\) \(5.83 x 10^{-10}\) \(5.75 x 10^{-2}\) \(5.03 x 10^{-4}\) \(2.91 x 10^{-11}\) |
- |
|
\(k_{c}\) |
- |
- |
- |
|
- |
- |
- |
- |
|
\(\rho_{f}\) |
- |
- |
- |
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- |
- |
- |
- |
|
- |
- |
300 |
- |
|
\(k_{f}\) |
- |
- |
- |
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- |
- |
- |
- |
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\(C_{f}\) |
- |
- |
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\(\left( \rho \right)_{e}\) |
- |
- |
- |
|
- |
- |
- |
- |
|
\(C_{e}\) |
- |
690 |
- |
|
\(\gamma\) |
12.7-21 |
1.3-1.6 |
- |
|
\(P_{x}\) |
- |
- |
- |
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- |
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\(T_{O}\) |
- |
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- |
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- |
- |
- |
- |
|
\(\Delta Z_{bl}\) |
12.7-28 |
.1 |
- |
|
\(\Delta Z_{bu}\) |
- |
.25 |
- |
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- |
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0 or 1 |
- |
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- |
- |
0 or 1 |
- |
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\(A_{c}\) |
12.2-1 |
- |
- |
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\(\Delta z\) |
12.2-4 |
- |
- |
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\(D_{h}\) |
12.2-7 |
- |
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\(p_{e}\) |
12.3-2 |
- |
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- |
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- |
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- |
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\(\gamma_{s}\) |
- |
- |
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\(\gamma_{c}\) |
- |
- |
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\(\gamma_{e}\) |
- |
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\(k_{s}\) |
- |
- |
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|
\(k_{s}\) |
- |
- |
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- |
- |
- |
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- |
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- |
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\(k_{f}\) |
- |
- |
- |
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\(\rho_{c}\) |
- |
- |
- |
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\(\left( \rho c \right)_{s}\) |
- |
- |
- |
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\(\left( \rho c \right)_{s}\) |
- |
- |
- |
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\(\left( \rho c \right)_{r}\) |
- |
- |
- |
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\(\left( \rho c \right)_{g}\) |
- |
- |
- |
|
\(R_{g}\) |
- |
- |
- |
|
\(A_{fr}\) |
12.2-2 |
0.1875 |
5-22 |
|
\(b_{fr}\) |
12.2-2 |
-0.2 |
5-22 |
|
- |
- |
- |
5-22 |
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- |
- |
- |
5-22 |
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- |
- |
- |
5-22 |
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- |
- |
0.2 |
- |
|
\(w\) |
- |
- |
- |
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\(K_{or}\) |
12.2-9 |
- |
5-23 |
|
\(\left( \Delta z_{i} / A \right)_{b}\) |
12.8-6 |
\(\left(D_{h} / 2 A_{c} \right)\) |
- |
|
\(\left( \Delta z_{i} / A \right)_{t}\) |
12.8-6 |
\(\left(D_{h} / 2 A_{c} \right)\) |
- |
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\(\theta1\) |
12.2-15 |
- |
- |
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\(\theta2\) |
12.2-15 |
- |
- |
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- |
- |
-15 |
- |
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- |
- |
50 |
- |
|
- |
- |
0.1 |
- |
|
\(h_{cond}\) |
- |
- |
- |
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- |
- |
0.02 |
- |
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- |
- |
- |
- |
|
- |
- |
0.667 x |
- |
|
- |
- |
- |
||
\(w_{fs}\) |
12.5-12 |
- |
||
\(f_{m}\) |
12.7-1 |
- |
- |
|
- |
- |
- |
- |
|
\(w_{fe}\) |
12.5-8 |
- |
- |
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- |
- |
3 |
- |
|
- |
- |
10 |
- |
|
\(A_{fr}\) |
12.6-9 |
0.316 |
5-22 |
|
\(b_{fr}\) |
12.6-9 |
-0.25 |
5-22 |
|
- |
- |
0.05 |
- |
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- |
- |
- |
- |
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- |
- |
- |
- |
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- |
- |
- |
- |
|
\(f_{2\phi}\) |
12.6-10 |
0 |
5-7 |
|
\(A_{fr}\) |
- |
0.316 |
5-22 |
|
\(b_{fr}\) |
- |
-0.25 |
5.7 |
|
- |
- |
\(1.0 x 10^{-5}\) |
5-22 |
|
\(A^{*}\) |
12.7.1 |
- |
- |
|
\(k_{g}\) |
12.7.1 |
1.5-2 |
- |
|
- |
- |
|||
\(M_{wg}\) |
12.7-31 |
100-130 |
- |
|
- |
- |
Since the SASSYS-1 or SAS4A calculation can accommodate up to eight
different types of fuel material, the number of fuel types used in a
given data deck must be specified. This is done through the variable
IFUEL1
. The fuel types must then each be designated as
belonging to the core or the blankets. If, in a given channel, the
blankets are of one homogeneous material and the core is of another, the
quantity IFUELV
specifies which of the IFUEL1
fuel types
is assigned to the core, while IFUELB
(Bloc 51, 16) indicates which is
assigned to the radial blankets. If, on the other hand, the core and/or
blankets each consist of radial bands of different types of fuel, the
variable IFUEL1
is used to match up each radial zone
with the appropriate fuel type in both the core and the blankets.
The cladding properties are used only in tabular form by the code.
Although only one type of cladding material is used in any one channel,
different types may be used in different channels. The total number of
types (maximum of three) for a particular run is designated in ICLAD1
,
and the type assigned to each channel is specified in
ICLADV
. The cladding thermal conductivity values are
input to EXKTB
as a function of temperature EXKTM
.
The specific heats are entered in CPCTAB
with the corresponding temperatures CPCTEM
.
The product of the cladding specific heat and the density is entered as
a variable in CROETB
as a function of temperature
CROETM
. In addition, the specific heat of the
cladding at the solidus temperature is specified in CE
.
Finally, the density of the solid cladding at an input
reference temperature is given for each channel in DENSS
.
The material properties for the structure and reflector regions are also
input in tabular form. In the case of the structure, the code allows
different sets of properties to be used for the inner and outer
structure nodes. However, the properties are constant for each node
within a particular zone and are independent of temperature. The thermal
conductivity for the inner structure node is stored in XKSTIZ
,
and that for the outer node is input to XKSTOZ
.
Similarly, the product of the density and the heat capacity for
the inner node is read into RHOCSI
, and for the outer
node, this quantity is stored in RHOCSO
. Of course,
the structure properties can vary from channel to channel.
The materials properties for the reflectors are also considered to be
constant within a given zone and independent of temperature. However,
unlike the case of the structure, the reflector variables are not
allowed to differ between the inner and outer segments. The thermal
conductivity is given in XKRF
, and the product of
density and heat capacity is input to RHOCR
. These,
too, may be different in different channels.
A couple of properties are input for the gas plenum. The product of
density and heat capacity for the plenum gas is found in RHOCG
,
and the thermal resistance of the gas is given in RG
.
These are both independent of temperature and variable form channel
to channel.
As indicated earlier in the text, several fluid heat-transfer
coefficients are required in order to model the heat transfer to the
sodium. For the bond which exists between the fuel and the cladding, the
heat-transfer coefficient is given by a correlation for which the
coefficients are read into AHBPAR
, BHBPAR
, CHBPAR
, and
HBPAR
. The limits on the bond heat-transfer coefficient
are set in HBMAX
and HBMIN
. Also, the option exists for
calculating the coefficient by the method used in the SAS3D code; this
option is invoked by setting the variable IHGAP
to zero.
The convective heat-transfer coefficient of the sodium is given by the
Dittus-Boettler correlation, for which the coefficients C1
, C2
, and C3
must be input.
If condensation of sodium vapor onto the
cladding or structure is occurring, the user-supplied condensation
heat-transfer coefficient HCOND
must be employed.
Much of the input to the voiding model is concerned with the geometry of
the problem. Most of this information can be varied from channel to
channel, but a few geometry-related features are consistent throughout
the system. First, of course, the number of channels must be specified
in NCHAN
. The location of the gas plenum must also be set
through the variable IPLUP
; IPLUP
=0 fixes the plenum above
the core, while IPLUP
=1 designates that it does below the core. The
heights of the lower coolant plenum inlet and the upper coolant plenum
outlet (ZPLENL
and ZPLENU
) must be input. Finally,
because modeling exists in SASSYS-1 to allow material expansion with
temperature, the temperature at which the input geometry information is
measured must be known; this is specified in TR
.
Much of the geometric information is initially assumed constant within
each axial zone and therefore is read in zone by zone. This requires
specification of the number of zones. The pin section always constitutes
ne axial zone, and each reflector contains from one to five zones. The
number of zones in the lower axial reflector is read into NREFB
,
while that for the upper reflector is given in NREFT
.
The data which are input on a zonal basis are the coolant flow area
per fuel pin ACCZ
, the hydraulic diameter DHZ
, and the length of each zone ZONEL
. The
structure variables designating the thickness of the inner node (DSTIZ
) and the outer node
(DSTOZ
) are read in
by zone, as is the structure perimeter SRFSTZ
.
Finally, the thicknesses of the outer and inner reflector segments
(DRFO
and DRFI
, respectively)
and the reflector perimeter SER
are all input by
zone.
Some of the remaining geometric information is read in by axial mesh
segment. The input information required about the axial mesh structure
includes the number of mesh segments in the gas plenum NPLN
,
the number of segments in the upper and lower blankets (MZUB
and
MZLB
, respectively), and the total number of segments
in each axial zone (NZNODE
). Quantities for which a
value must be entered for each axial mesh segment in the pin region
include AXHI
, the length of each axial segment; RBR
,
the inner radius of the cladding; RER
, the outer
radius of the cladding; RINFP
, the fuel inner radius; and ROUTFP
, the fuel outer radius.
Some geometric variables define the radial composition of the problem.
These include data such as the number of radial temperature segments in
the fuel (NT
), the number of concentric rings of different
types of fuel in the core and blankets (NZONF
), the
radial mesh boundaries of the fuel rings (NODSUM
),
and a flag to specify whether the radial mesh is set up on an equal
radius or equal mass basis (IEQMAS
).
A few additional pieces of information on the problem geometry must be
input. The cladding inner and outer radii in the gas plenum (RBRPL
and
RERPL
) must be specified separately from the values
in the pin region (RBR
and RER
, mentioned above), as must values for the
nominal cladding inner and outer radii (RBR0
and RER0
).
The nominal radii simply represent average values in the pin
region; usually the cladding radii in the pin are all equal at the
beginning of a run, and the nominal radii are just set to these values.
The length of the fission-gas plenum is given in PLENL
,
the area of the coolant channel plus the pin is set in AREAPC
,
and the volume fraction of the coolant in the channel is
represented in VFC
. The inertial terms below and above
the subassembly are read into DZIAB
and DZIAT
, and the
orifice coefficients at the entrance and exit of each axial zone are
stored in XKORI
. The number of pins per subassembly is
given in NPIN
, and the number of subassemblies
represented by the channel is designated in NSUBAS
.
Another category of input data is that of temperature initialization.
The inlet temperature T0TAB
must be specified as a
function of time T0TME
, with NT0TAB
being the number of entries in the inlet temperature table. The
temperature of any liquid sodium which reenters the subassembly from the
top is fixed at TUPL
. The solidus and liquidus
temperatures of the fuel are given in TFSOL
and TFLIQ
, respectively,
while those for the cladding are
defined in TESOL
and TELIQ
. The flag
which directs whether an Eulerian or a Lagrangian liquid temperature
calculation is performed prior to flow reversal is set in ILAG
,
and the amount of superheat required before boiling can begin
is fixed in DTS
. The superheat required for formation of
new bubbles after voiding has begun is given by DTSI
.
Several pieces of information concerning reactor power must be input.
The code contains an option for specifying either the power or the
external reactivity as a function of time, and the flag IPOWER
indicates which quantity is chosen. A total of NPREAT
values of the power are read into the array PREATB
,
with the corresponding times read into array PREATM
.
The flag IPOWOP
determines whether the total steady-state
reactor power is computed form the power in the peak axial segment, or
vice versa, and the power in the peak axial segment is entered in POW
.
The fraction of the total reactor power represented by
all the SASSYS-1 channels must be given, since some possible channel
configurations omit a few low power channels which must be given, since
some possible channel configurations omit a few low channels which have
a minimal impact on the calculation, and this number is input to FRPR
.
The remaining power-related data must be inserted channel by channel.
The fraction of the total power due to direct gamma heating must be
specified for the structure (GAMSS
), coolant (GAMTNC
), and cladding
(GAMTNE
). In addition, the axial and radial
shapes of the power distribution are read into PSHAPE
and PSHAPR
, respectively.
Several conditions concerning the coolant pressure must be designated
through the input. The coolant exit pressure is held constant throughout
the calculation and is read into variable PX
. The
magnitude of the coolant inlet pressure at steady state is computed by
the code, but, if the PRIMAR-4 option is not invoked, the variation of
the normalized inlet pressure with time is either read from a table or
calculated from a simple equation. The flag NPRES
determines whether the table or the equation will be used. If the
equation is chosen, the coefficients PDEC
, PDEC1
, and PDEC2
must be entered.
If the inlet pressure is to be determined from a
table, the values are entered in PRETAB
, with the
corresponding times specified in PRETME
. There is also
an option to enter the coolant flow rather than the driving pressure in
PRETAB
. This option is indicated by the flag IFLOW
. The
user specified coolant flow vs. time is only available if the PRIMAR-1
option is used, IPRION
≠ 4. With this option, the coolant
flow rate in channel IFLOW
is specified as a function of time. The
outlet plenum pressure is also specified as a function of time. The code
back-calculates the inlet plenum pressure required to give the specified
flow rate, and this inlet plenum pressure drives the coolant flow in all
other channels. Currently, this option does not work after the onset of
boiling in channel IFLOW
. Finally, the initial gas pressure in the gas
plenum at the reference temperature TR
is input through P0GAS
.
Two other areas for which input data are needed are the expressions for
calculation of friction discussed earlier and the determination of
sodium film thickness in voided regions. The coefficients \(A_{fr}\) and \(b_{fr}\)
which are used in the friction expressions are user-input rather
than fixed within the code to allow greater flexibility. These include
coefficients for the liquid slugs (AFR
and BFR
), the
sodium vapor (AFRV
and BFRV
), and the liquid sodium
film (AFRF
and BFRF
). Also, the fraction of the
two-phase friction factor to be used in voided regions is set in FVAPM
.
The calculation of film thickness requires information
about the initial film thickness left on cladding and structure as the
voiding front passes by; these numbers are stored in WF0
for the cladding and WFS00
for the structure. In
addition, the SASSYS-1 model does not try to predict when the sodium
films will evaporate completely (zero film thickness); rather, the films
are considered to be evaporated when the calculated estimates them to be
less than user-input values. In the early part of the calculation, these
minimum values are WFMIN
for the cladding and WFMINS
for the structure,
but after IFILM
axial segments have
experienced dryout, the values in WFMIND
and WFMNSD
are used instead.
A few additional pieces fo information are needed inorder to run the
calculation. The steady-state coolant mass flow rate is input to W0
and the fraction of the total reactor flow which is
actually represented by core channels is read into FRFLOW
(again, to accommodate channel maps which do not include all the
subassemblies in the reactor; see the discussion of FRPR
given above).
The heat of fusion for the fuel is given in UFMELT
,
and that for the cladding is read into UEMELT
. Also,
the product of the Stefan-Boltzmann constant and the emissivity is
assigned to the variable DEL
.
The options for gas release due to pin failure are determined by IGASRL
and IGRLTM
. If IGASRL=0, this option is
not used. The method in which pin failure is determined is specified by
IGRLTM
. If IGRLTM
=0, then DEFORM-5 triggers pin failure in pin group M
when the cladding life fraction exceeds FRUPT
(M). If
IGRLTM
=1, then gas release in pin group M occurs in node IFAIL
at time
TMFAIL
(M). In addition, the gas
release model requires input values for DZBCGL
and DZBCGU
for cutting off bubbles after they flow out the top of
the subassembly. GAMGAS
and GASMW
provide properties of the gas. FRACP
(M) specifies the
fraction of the pins in each group. AGSRLS
and GASKOR
determine the gas flow rate through the cladding rip,
and PGRMIN
specifies when gas release will be shut off. The initial
plenum gas pressure is determined by P0GAS
if it is not
calculated by DEFORM.
Time-step control involves specification of a number of input variables.
The maximum number of main time steps is given in MAXSTP
,
and the maximum problem time is TIMAX
. The initial main
time-step size is DT0
, and the maximum size after the
initiation of voiding is DTMMXB
. The maximum
heat-transfer time-step length after boiling has begun is DTMXB
.
The minimum coolant time-step size before voiding is DTCMIN
;
after the onset of boiling, it is TPDMIN
.
The different time-step sizes are limited by several input criteria. The
main time step must be small enough so that the power does not make a
fractional change greater than that specified in DPWMAX
during the step. The heat-transfer time step must be limited so that,
over its span, the fuel temperature does not change by more than DTFUEL
,
the cladding temperature by more than DTCLAD
,
and, prior to voiding, the coolant flow rate by DWMAX
.
The coolant time-step size must be small enough so that the liquid
temperature does not change by more than DTLMAX
, the vapor temperature
by more than DTVMAX
, and the position of any liquid-vapor interface by
more than DZIMAX
.
Printout of results is guided by several input variables. Normally, a
standard printout pertaining just to the voiding model is output at the
end of designated coolant time steps, and a general standard printout is
given at the end of designated main time steps. Boiling printout occurs
every IBLPRN
coolant time steps. General printout is
done every IPO
main time steps up until main time step
IBLPRT
; after step IBLPRT
, general printout is given
every IPOBOI
time steps. The temperatures in the general
printout may be listed in units of degrees Kelvin or degrees centigrade
at the discretion of the user through the variable ITKEL
;
however, the user is advised that the labels in the printout will state
that temperatures are listed in degrees Kelvin regardless of which
option is chosen.
If desired, more detailed output can be obtained through several of the
input variables. This is intended primarily for the use of the code
developers and outside users who wish to modify the code, but it may on
occasion be helpful if problems are encountered in simply running the
code. The simplest of this additional output is flagged by the variable
IHEX
. This number will activate a hexadecimal printout of
the sum of the coolant temperatures in a channel. The hexadecimal print
is an exact representation of the sum (without truncation) and is
therefore useful when comparing two different runs of similar data decks
to indicate at what point the two calculations began to diverge. A more
extensive output is invoked by the variable IDBUGV
. Many different printout options are
incorporated into IDBUGV
. The print selected will begin at step IERSTP
.
Prints specialized to the voiding model are also
available. The variable IDBGBL
will trigger the same
extensive voiding-related output as the IDBUGV
=4 option, but it will
begin the output on coolant time step IDBLST
rather than
on main time step IERSTP
. This allows the user to begin a lengthy
printout much closer to the time at which the difficulty develops than
is possible with IDBUGV
. The array IDBFLG
initiates
more specialized voiding points. The coolant time step on which each of
these prints starts is stored in array IDBSTP
.
A few additional input variables remain to be discussed. The remaining
quantities include THETA1
and THETA2
, the coefficients
which determine the degree of implicitness of the liquid slug
calculation; SLMIN
, the minimum length of a liquid slug
in between two vapor bubbles (minimum slug length is required to
stabilize the calculation); and XMINL
, the bubble length
above which the pressure gradient voiding model is used and below which
the pressure gradient voiding model is used.