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dsin.txt
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dsin.txt
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#1
char Aclass(3,24)
Adymosim
1.4
Modelica experiment file
//TEST EDIT
# Experiment parameters
double experiment(7,1)
0 # StartTime Time at which integration starts
# (and linearization and trimming time)
1 # StopTime Time at which integration stops
0 # Increment Communication step size, if > 0
500 # nInterval Number of communication intervals, if > 0
1.0000000000000000E-004 # Tolerance Relative precision of signals for
# simulation, linearization and trimming
0 # MaxFixedStep Maximum step size of fixed step size
# integrators, if > 0.0
8 # Algorithm Integration algorithm as integer (1...28)
#
# | model| | | dense | state |
# Algorithm | typ | stiff | order | output| event |
# ------------+------+-------+--------+-------+-------+
# 1 | deabm | ode | no | 1-12 | yes | no |
# 2 | lsode1 | ode | no | 1-12 | yes | no |
# 3 | lsode2 | ode | yes | 1-5 | yes | no |
# 4 | lsodar | ode | both |1-12,1-5| yes | yes |
# 5 | dopri5 | ode | no | 5 | no | no |
# 6 | dopri8 | ode | no | 8 | no | no |
# 7 | grk4t | ode | yes | 4 | no | no |
# 8 | dassl | dae | yes | 1-5 | yes | yes |
# 9 | odassl | hdae | yes | 1-5 | yes | yes |
# 10 | mexx | hdae | no | 2-24 | no | no |
# 11 | euler | ode | no | 1 | no | yes |
# 12 | rkfix2 | ode | no | 2 | no | yes |
# 13 | rkfix3 | ode | no | 3 | no | yes |
# 14 | rkfix4 | ode | no | 4 | no | yes |
#>=14| others | ode |yes/no | 2-5 | yes | yes |
# ---+--------+------+-------+--------+-------+-------+
# euler and rkfix have fixed stepsize.
# Method tuning parameters
double method(27,1)
1 # grid type of communication time grid, defined by
# = 1: equidistant points ("Increment/nInterval")
# = 2: vector of grid points ("tgrid")
# = 3: variable step integrator (automatically)
# = 4: model (call of "increment" in Dymola, e.g.
# incr=Time > 2 then 0 else 0.1
# dummy=increment(incr))
# grid = 1,3 is stopped by "StopTime"
# grid = 2 is stopped by "tgrid(last)"
# grid = 4 runs forever (stopped by model)
1 # nt Use every NT time instant, if grid = 3
3 # dense 1/2/3 restart/step/interpolate GRID points
1 # evgrid 0/1 do not/save event points in comm. time grid
1 # evu 0/1 U-discontinuity does not/trigger events
0 # evuord U-discontinuity order to consider (0,1,...)
0 # error 0/1/2 One message/warning/error messages
0 # jac 0/1 Compute jacobian numerically/by BLOCKJ
0 # xd0c 0/1 Compute/set XD0
0 # f3 0/1 Ignore/use F3 of HDAE (= index 1)
0 # f4 0/1 Ignore/use F4 of HDAE (= index 2)
0 # f5 0/1 Ignore/use F5 of HDAE (= invar.)
0 # debug flags for debug information (1<<0 uses pdebug)
100 # pdebug priority of debug information (1...100)
0 # fmax Maximum number of evaluations of BLOCKF, if > 0
0 # ordmax Maximum allowed integration order, if > 0
0 # hmax Maximum absolute stepsize, if > 0
0 # hmin Minimum absolute stepsize, if > 0 (use with care!)
0 # h0 Stepsize to be attempted on first step, if > 0
2.0000000000000000E-014 # teps Bound to check, if 2 equal time instants
1.0000000000000000E-010 # eveps Hysteresis epsilon at event points
20 # eviter Maximum number of event iterations
9.9999999999999995E-007 # delaym Minimum time increment in delay buffers
1 # fexcep 0/1 floating exception crashes/stops dymosim
1 # tscale clock-time = tscale*simulation-time, if grid = 5
# > 1: simulation too slow
# = 1: simulation-time = real-time
# < 1: simulation too fast
1 # shared (not used)
2473 # memkey (not used)
# Output parameters
int settings(13,1)
0 # lprec 0/1 do not/store result data in double
1 # lx 0/1 do not/store x (state variables)
1 # lxd 0/1 do not/store xd (derivative of states)
1 # lu 0/1 do not/store u (input signals)
1 # ly 0/1 do not/store y (output signals)
0 # lz 0/1 do not/store z (indicator signals)
1 # lw 0/1 do not/store w (auxiliary signals)
1 # la 0/1 do not/store a (alias signals)
0 # lperf 0/1 do not/store performance indicators
0 # levent 0/1 do not/store event point
1 # lres 0/1 do not/store results on result file
0 # lshare 0/1 do not/store info data for shared memory on dsshare.txt
1 # lform 0/1 ASCII/Matlab-binary storage format of results
# (for simulation/linearization; not for trimming)
# Names of initial variables
char initialName(118,41)
pressureIncrease.medium.rho
pressureIncrease.medium.cp
pressureIncrease.medium.cv
pressureIncrease.medium.lamda
pressureIncrease.medium.nue
pressureIncrease.m
pressureIncrease.T0
pressureIncrease.T0fixed
pressureIncrease.tapT
pressureIncrease.V_flow
pressureIncrease.Q_flow
pressureIncrease.T
pressureIncrease.der(T)
pressureIncrease.T_a
pressureIncrease.T_b
pressureIncrease.dT
pressureIncrease.h
pressureIncrease.der(h)
pressureIncrease.flowPort_a.medium.rho
pressureIncrease.flowPort_a.medium.cp
pressureIncrease.flowPort_a.medium.cv
pressureIncrease.flowPort_a.medium.lamda
pressureIncrease.flowPort_a.medium.nue
pressureIncrease.flowPort_a.m_flow
pressureIncrease.flowPort_a.h
pressureIncrease.flowPort_a.der(h)
pressureIncrease.flowPort_a.H_flow
pressureIncrease.flowPort_b.medium.rho
pressureIncrease.flowPort_b.medium.cp
pressureIncrease.flowPort_b.medium.cv
pressureIncrease.flowPort_b.medium.lamda
pressureIncrease.flowPort_b.medium.nue
pressureIncrease.flowPort_b.p
pressureIncrease.flowPort_b.h
pressureIncrease.flowPort_b.der(h)
pressureIncrease.flowPort_b.H_flow
pressureIncrease.usePressureIncreaseInput
pressureIncrease.constantPressureIncrease
heatedPipe.medium.rho
heatedPipe.medium.cp
heatedPipe.medium.cv
heatedPipe.medium.lamda
heatedPipe.medium.nue
heatedPipe.m
heatedPipe.T0
heatedPipe.T0fixed
heatedPipe.tapT
heatedPipe.dp
heatedPipe.V_flow
heatedPipe.Q_flow
heatedPipe.T
heatedPipe.der(T)
heatedPipe.T_a
heatedPipe.der(T_a)
heatedPipe.T_b
heatedPipe.der(T_b)
heatedPipe.dT
heatedPipe.der(dT)
heatedPipe.h
heatedPipe.der(h)
heatedPipe.flowPort_a.medium.rho
heatedPipe.flowPort_a.medium.cp
heatedPipe.flowPort_a.medium.cv
heatedPipe.flowPort_a.medium.lamda
heatedPipe.flowPort_a.medium.nue
heatedPipe.flowPort_b.medium.rho
heatedPipe.flowPort_b.medium.cp
heatedPipe.flowPort_b.medium.cv
heatedPipe.flowPort_b.medium.lamda
heatedPipe.flowPort_b.medium.nue
heatedPipe.V_flowLaminar
heatedPipe.dpLaminar
heatedPipe.V_flowNominal
heatedPipe.dpNominal
heatedPipe.frictionLoss
heatedPipe.pressureDrop
heatedPipe.Q_friction
heatedPipe.dpNomMin
heatedPipe.k
heatedPipe.h_g
heatedPipe.heatPort.Q_flow
heatCapacitorPCMLike00_1.C
heatCapacitorPCMLike00_1.T
heatCapacitorPCMLike00_1.der(T)
heatCapacitorPCMLike00_1.cp_h2o
heatCapacitorPCMLike00_1.cp_PCM
heatCapacitorPCMLike00_1.rho_h2o
heatCapacitorPCMLike00_1.rho_PCM
heatCapacitorPCMLike00_1.V_tank
heatCapacitorPCMLike00_1.fracPCM_vol
heatCapacitorPCMLike00_1.hfg_pcm
heatCapacitorPCMLike00_1.T_sc
heatCapacitorPCMLike00_1.T_melt
pressureSensor.medium.rho
pressureSensor.medium.cp
pressureSensor.medium.cv
pressureSensor.medium.lamda
pressureSensor.medium.nue
pressureSensor.flowPort.medium.rho
pressureSensor.flowPort.medium.cp
pressureSensor.flowPort.medium.cv
pressureSensor.flowPort.medium.lamda
pressureSensor.flowPort.medium.nue
pressureSensor.flowPort.m_flow
pressureSensor.flowPort.H_flow
absolutePressure.medium.rho
absolutePressure.medium.cp
absolutePressure.medium.cv
absolutePressure.medium.lamda
absolutePressure.medium.nue
absolutePressure.p
absolutePressure.flowPort.medium.rho
absolutePressure.flowPort.medium.cp
absolutePressure.flowPort.medium.cv
absolutePressure.flowPort.medium.lamda
absolutePressure.flowPort.medium.nue
absolutePressure.flowPort.m_flow
absolutePressure.flowPort.H_flow
double initialValue(118,6)
-1 9.9560000000000002E+002 0 1.0000000000000000E+100
1 280 # pressureIncrease.medium.rho
-1 4177 0 0
1 280 # pressureIncrease.medium.cp
-1 4177 0 0
1 280 # pressureIncrease.medium.cv
-1 6.1499999999999999E-001 0 0
1 280 # pressureIncrease.medium.lamda
-1 7.9999999999999996E-007 0 1.0000000000000000E+100
1 280 # pressureIncrease.medium.nue
0 1 0 1.0000000000000000E+100
6 256 # pressureIncrease.m
-1 2.9314999999999998E+002 0 1.0000000000000000E+100
1 280 # pressureIncrease.T0
0 0 0 0
6 257 # pressureIncrease.T0fixed
0 1 0 1
6 256 # pressureIncrease.tapT
0 0 0 0
6 256 # pressureIncrease.V_flow
0 0 0 0
6 256 # pressureIncrease.Q_flow
-1 0 0 1.0000000000000000E+100
2 272 # pressureIncrease.T
0 0 0 0
3 256 # pressureIncrease.der(T)
0 2.8814999999999998E+002 0 1.0000000000000000E+100
6 256 # pressureIncrease.T_a
0 2.8814999999999998E+002 0 1.0000000000000000E+100
6 256 # pressureIncrease.T_b
0 0 0 0
6 256 # pressureIncrease.dT
0 0 0 0
6 1280 # pressureIncrease.h
0 0 0 0
6 1280 # pressureIncrease.der(h)
0 0 0 1.0000000000000000E+100
6 256 # pressureIncrease.flowPort_a.medium.rho
0 0 0 0
6 256 # pressureIncrease.flowPort_a.medium.cp
0 0 0 0
6 256 # pressureIncrease.flowPort_a.medium.cv
0 0 0 0
6 256 # pressureIncrease.flowPort_a.medium.lamda
0 0 0 1.0000000000000000E+100
6 256 # pressureIncrease.flowPort_a.medium.nue
0 0 0 0
6 388 # pressureIncrease.flowPort_a.m_flow
0 0 0 0
6 260 # pressureIncrease.flowPort_a.h
0 0 0 0
6 260 # pressureIncrease.flowPort_a.der(h)
0 0 0 0
6 388 # pressureIncrease.flowPort_a.H_flow
0 0 0 1.0000000000000000E+100
6 256 # pressureIncrease.flowPort_b.medium.rho
0 0 0 0
6 256 # pressureIncrease.flowPort_b.medium.cp
0 0 0 0
6 256 # pressureIncrease.flowPort_b.medium.cv
0 0 0 0
6 256 # pressureIncrease.flowPort_b.medium.lamda
0 0 0 1.0000000000000000E+100
6 256 # pressureIncrease.flowPort_b.medium.nue
0 0 0 0
6 260 # pressureIncrease.flowPort_b.p
0 0 0 0
6 260 # pressureIncrease.flowPort_b.h
0 0 0 0
6 260 # pressureIncrease.flowPort_b.der(h)
0 0 0 0
6 388 # pressureIncrease.flowPort_b.H_flow
0 0 0 0
6 257 # pressureIncrease.usePressureIncreaseInput
-1 20000 0 0
1 280 # pressureIncrease.constantPressureIncrease
-1 9.9560000000000002E+002 0 1.0000000000000000E+100
1 280 # heatedPipe.medium.rho
-1 4177 0 0
1 280 # heatedPipe.medium.cp
-1 4177 0 0
1 280 # heatedPipe.medium.cv
-1 6.1499999999999999E-001 0 0
1 280 # heatedPipe.medium.lamda
-1 7.9999999999999996E-007 0 1.0000000000000000E+100
1 280 # heatedPipe.medium.nue
0 10 0 1.0000000000000000E+100
6 256 # heatedPipe.m
-1 2.9314999999999998E+002 0 1.0000000000000000E+100
1 280 # heatedPipe.T0
0 0 0 0
6 257 # heatedPipe.T0fixed
-1 1 0 1
1 280 # heatedPipe.tapT
0 0 0 0
6 256 # heatedPipe.dp
0 0 0 0
6 288 # heatedPipe.V_flow
0 0 0 0
6 256 # heatedPipe.Q_flow
-1 0 0 1.0000000000000000E+100
2 272 # heatedPipe.T
0 0 0 0
3 256 # heatedPipe.der(T)
0 2.8814999999999998E+002 0 1.0000000000000000E+100
6 256 # heatedPipe.T_a
0 0 0 0
6 256 # heatedPipe.der(T_a)
0 2.8814999999999998E+002 0 1.0000000000000000E+100
6 256 # heatedPipe.T_b
0 0 0 0
6 256 # heatedPipe.der(T_b)
0 0 0 0
6 256 # heatedPipe.dT
0 0 0 0
6 256 # heatedPipe.der(dT)
0 0 0 0
6 1280 # heatedPipe.h
0 0 0 0
6 1280 # heatedPipe.der(h)
0 0 0 1.0000000000000000E+100
6 256 # heatedPipe.flowPort_a.medium.rho
0 0 0 0
6 256 # heatedPipe.flowPort_a.medium.cp
0 0 0 0
6 256 # heatedPipe.flowPort_a.medium.cv
0 0 0 0
6 256 # heatedPipe.flowPort_a.medium.lamda
0 0 0 1.0000000000000000E+100
6 256 # heatedPipe.flowPort_a.medium.nue
0 0 0 1.0000000000000000E+100
6 256 # heatedPipe.flowPort_b.medium.rho
0 0 0 0
6 256 # heatedPipe.flowPort_b.medium.cp
0 0 0 0
6 256 # heatedPipe.flowPort_b.medium.cv
0 0 0 0
6 256 # heatedPipe.flowPort_b.medium.lamda
0 0 0 1.0000000000000000E+100
6 256 # heatedPipe.flowPort_b.medium.nue
0 1.6666666666667000E-005 9.9999999999999997E-061 1.0000000000000000E+100
6 256 # heatedPipe.V_flowLaminar
-1 30000 0 0
1 280 # heatedPipe.dpLaminar
-1 8.3333333333333005E-005 0 0
1 280 # heatedPipe.V_flowNominal
-1 3.0000000000000000E+005 0 0
1 280 # heatedPipe.dpNominal
-1 0 0 1
1 280 # heatedPipe.frictionLoss
0 0 0 0
6 256 # heatedPipe.pressureDrop
0 0 0 0
6 256 # heatedPipe.Q_friction
0 0 0 0
6 1280 # heatedPipe.dpNomMin
0 0 0 0
6 1280 # heatedPipe.k
-1 0 0 0
1 280 # heatedPipe.h_g
0 0 0 0
6 388 # heatedPipe.heatPort.Q_flow
0 0 0 0
6 320 # heatCapacitorPCMLike00_1.C
0 3.3314999999999998E+002 0 1.0000000000000000E+100
6 256 # heatCapacitorPCMLike00_1.T
0 0 0 0
6 256 # heatCapacitorPCMLike00_1.der(T)
-1 4.1769999999999996E+000 0 0
1 280 # heatCapacitorPCMLike00_1.cp_h2o
-1 2.8999999999999999E+000 0 0
1 280 # heatCapacitorPCMLike00_1.cp_PCM
-1 995 0 0
1 280 # heatCapacitorPCMLike00_1.rho_h2o
-1 900 0 0
1 280 # heatCapacitorPCMLike00_1.rho_PCM
-1 1 0 0
1 280 # heatCapacitorPCMLike00_1.V_tank
-1 5.9999999999999998E-001 0 0
1 280 # heatCapacitorPCMLike00_1.fracPCM_vol
-1 100 1.0000000000000000E-002 1.0000000000000000E+100
1 280 # heatCapacitorPCMLike00_1.hfg_pcm
0 358 0 1.0000000000000000E+100
6 256 # heatCapacitorPCMLike00_1.T_sc
0 364 0 1.0000000000000000E+100
6 256 # heatCapacitorPCMLike00_1.T_melt
-1 9.9560000000000002E+002 0 1.0000000000000000E+100
1 280 # pressureSensor.medium.rho
-1 4177 0 0
1 280 # pressureSensor.medium.cp
-1 4177 0 0
1 280 # pressureSensor.medium.cv
-1 6.1499999999999999E-001 0 0
1 280 # pressureSensor.medium.lamda
-1 7.9999999999999996E-007 0 1.0000000000000000E+100
1 280 # pressureSensor.medium.nue
0 0 0 1.0000000000000000E+100
6 256 # pressureSensor.flowPort.medium.rho
0 0 0 0
6 256 # pressureSensor.flowPort.medium.cp
0 0 0 0
6 256 # pressureSensor.flowPort.medium.cv
0 0 0 0
6 256 # pressureSensor.flowPort.medium.lamda
0 0 0 1.0000000000000000E+100
6 256 # pressureSensor.flowPort.medium.nue
0 0 0 0
6 388 # pressureSensor.flowPort.m_flow
0 0 0 0
6 388 # pressureSensor.flowPort.H_flow
-1 9.9560000000000002E+002 0 1.0000000000000000E+100
1 280 # absolutePressure.medium.rho
-1 4177 0 0
1 280 # absolutePressure.medium.cp
-1 4177 0 0
1 280 # absolutePressure.medium.cv
-1 6.1499999999999999E-001 0 0
1 280 # absolutePressure.medium.lamda
-1 7.9999999999999996E-007 0 1.0000000000000000E+100
1 280 # absolutePressure.medium.nue
-1 10000 0 0
1 280 # absolutePressure.p
0 0 0 1.0000000000000000E+100
6 256 # absolutePressure.flowPort.medium.rho
0 0 0 0
6 256 # absolutePressure.flowPort.medium.cp
0 0 0 0
6 256 # absolutePressure.flowPort.medium.cv
0 0 0 0
6 256 # absolutePressure.flowPort.medium.lamda
0 0 0 1.0000000000000000E+100
6 256 # absolutePressure.flowPort.medium.nue
0 0 0 0
6 388 # absolutePressure.flowPort.m_flow
0 0 0 0
6 388 # absolutePressure.flowPort.H_flow
# Matrix with 6 columns defining the initial value calculation
# (columns 5 and 6 are not utilized for the calculation but are
# reported by dymosim via dymosim -i for user convenience):
#
# column 1: Type of initial value
# = -2: special case: for continuing simulation (column 2 = value)
# = -1: fixed value (column 2 = fixed value)
# = 0: free value, i.e., no restriction (column 2 = initial value)
# > 0: desired value (column 1 = weight for optimization
# column 2 = desired value)
# use weight=1, since automatic scaling usually
# leads to equally weighted terms
# column 2: fixed, free or desired value according to column 1.
# column 3: Minimum value (ignored, if Minimum >= Maximum).
# column 4: Maximum value (ignored, if Minimum >= Maximum).
# Minimum and maximum restrict the search range in initial
# value calculation. They might also be used for scaling.
# column 5: Category of variable.
# = 1: parameter.
# = 2: state.
# = 3: state derivative.
# = 4: output.
# = 5: input.
# = 6: auxiliary variable.
# column 6: Data type of variable.
# = 0: real.
# = 1: boolean.
# = 2: integer.
#
# Initial values are calculated according to the following procedure:
#
# - If parameters, states and inputs are FIXED, and other variables
# are FREE, no special action takes place (default setting).
#
# - If there are only FIXED and FREE variables and the number of
# FREE parameters, states and inputs is IDENTICAL to the number of
# FIXED state derivatives, outputs and auxiliary variables, a non-linear
# equation is solved to determine a consistent set of initial conditions.
#
# - In all other cases the following optimization problem is solved:
# min( sum( weight(i)*( (value(i) - DESIRED(i))/scale(i) )^2 ) )
# under the constraint that the differential equation is fulfilled
# at the initial time. In most cases weight(i)=1 is sufficient, due
# to the automatic scaling (if DESIRED(i) is not close to zero,
# scale(i) = DESIRED(i). Otherwise, the scaling is based on the
# nominal value (and maybe minimum and maximum values given in
# column 3 and 4). If these values are zero, scale(i)=1 is used).
#
char initialDescription(118,72)
Density [kg/m3|g/cm3]
Specific heat capacity at constant pressure [J/(kg.K)]
Specific heat capacity at constant volume [J/(kg.K)]
Thermal conductivity [W/(m.K)]
Kinematic viscosity [m2/s]
Mass of medium [kg]
Initial temperature of medium [K|degC]
Initial temperature guess value or fixed [:#(type=Boolean)]
Defines temperature of heatPort between inlet and outlet temperature
Volume flow a->b [m3/s]
Heat exchange with ambient [W]
Outlet temperature of medium [K|degC]
der(Outlet temperature of medium) [K/s]
Temperature at flowPort_a [K|degC]
Temperature at flowPort_b [K|degC]
Temperature increase of coolant in flow direction [K,]
Medium's specific enthalpy [J/kg]
der(Medium's specific enthalpy) [m2/s3]
Density [kg/m3|g/cm3]
Specific heat capacity at constant pressure [J/(kg.K)]
Specific heat capacity at constant volume [J/(kg.K)]
Thermal conductivity [W/(m.K)]
Kinematic viscosity [m2/s]
[kg/s]
[J/kg]
[m2/s3]
[W]
Density [kg/m3|g/cm3]
Specific heat capacity at constant pressure [J/(kg.K)]
Specific heat capacity at constant volume [J/(kg.K)]
Thermal conductivity [W/(m.K)]
Kinematic viscosity [m2/s]
[Pa|bar]
[J/kg]
[m2/s3]
[W]
Enable / disable pressure increase input [:#(type=Boolean)]
Pressure increase [Pa|bar]
Density [kg/m3|g/cm3]
Specific heat capacity at constant pressure [J/(kg.K)]
Specific heat capacity at constant volume [J/(kg.K)]
Thermal conductivity [W/(m.K)]
Kinematic viscosity [m2/s]
Mass of medium [kg]
Initial temperature of medium [K|degC]
Initial temperature guess value or fixed [:#(type=Boolean)]
Defines temperature of heatPort between inlet and outlet temperature
Pressure drop a->b [Pa|bar]
Volume flow a->b [m3/s]
Heat exchange with ambient [W]
Outlet temperature of medium [K|degC]
der(Outlet temperature of medium) [K/s]
Temperature at flowPort_a [K|degC]
der(Temperature at flowPort_a) [K/s]
Temperature at flowPort_b [K|degC]
der(Temperature at flowPort_b) [K/s]
Temperature increase of coolant in flow direction [K,]
der(Temperature increase of coolant in flow direction) [K/s]
Medium's specific enthalpy [J/kg]
der(Medium's specific enthalpy) [m2/s3]
Density [kg/m3|g/cm3]
Specific heat capacity at constant pressure [J/(kg.K)]
Specific heat capacity at constant volume [J/(kg.K)]
Thermal conductivity [W/(m.K)]
Kinematic viscosity [m2/s]
Density [kg/m3|g/cm3]
Specific heat capacity at constant pressure [J/(kg.K)]
Specific heat capacity at constant volume [J/(kg.K)]
Thermal conductivity [W/(m.K)]
Kinematic viscosity [m2/s]
Laminar volume flow [m3/s|l/min]
Laminar pressure drop [Pa|kPa]
Nominal volume flow [m3/s|l/min]
Nominal pressure drop [Pa|kPa]
Part of friction losses fed to medium [1]
[Pa|bar]
[W]
[Pa|bar]
[Pa.s2/m6]
Geodetic height (heigth difference from flowPort_a to flowPort_b) [m]
Heat flow rate (positive if flowing from outside into the component) [W]
Heat capacity of element (= cp*m) [J/K]
Temperature of element [K|degC]
der(Temperature of element) [K/s]
spec heat cap water
spec heat cap paraffin
density water
density PCM
density PCM
fraction of volume that is PCM
[kJ/kg]
lowest subcooling temperature [K|degC]
highest melting temperature [K|degC]
Density [kg/m3|g/cm3]
Specific heat capacity at constant pressure [J/(kg.K)]
Specific heat capacity at constant volume [J/(kg.K)]
Thermal conductivity [W/(m.K)]
Kinematic viscosity [m2/s]
Density [kg/m3|g/cm3]
Specific heat capacity at constant pressure [J/(kg.K)]
Specific heat capacity at constant volume [J/(kg.K)]
Thermal conductivity [W/(m.K)]
Kinematic viscosity [m2/s]
[kg/s]
[W]
Density [kg/m3|g/cm3]
Specific heat capacity at constant pressure [J/(kg.K)]
Specific heat capacity at constant volume [J/(kg.K)]
Thermal conductivity [W/(m.K)]
Kinematic viscosity [m2/s]
Pressure ground [Pa|bar]
Density [kg/m3|g/cm3]
Specific heat capacity at constant pressure [J/(kg.K)]
Specific heat capacity at constant volume [J/(kg.K)]
Thermal conductivity [W/(m.K)]
Kinematic viscosity [m2/s]
[kg/s]
[W]