7.9. Variable types¶
7.9.1. Overview¶
- variable_types.time_t = daeVariableType(name="time_t", units=(s ** (1)), lowerBound=0, upperBound=1e+20, initialGuess=0, absoluteTolerance=1e-05, valueConstraint=0)¶
- variable_types.length_t = daeVariableType(name="length_t", units=(m ** (1)), lowerBound=0, upperBound=100000, initialGuess=0.5, absoluteTolerance=1e-05, valueConstraint=0)¶
- variable_types.area_t = daeVariableType(name="area_t", units=(m ** (2)), lowerBound=0, upperBound=100000, initialGuess=1, absoluteTolerance=1e-05, valueConstraint=0)¶
- variable_types.volume_t = daeVariableType(name="volume_t", units=(m ** (3)), lowerBound=0, upperBound=100000, initialGuess=1, absoluteTolerance=1e-06, valueConstraint=0)¶
- variable_types.velocity_t = daeVariableType(name="velocity_t", units=(m ** (1))*(s ** (-1)), lowerBound=-1e+10, upperBound=1e+10, initialGuess=0.001, absoluteTolerance=1e-05, valueConstraint=0)¶
- variable_types.pressure_t = daeVariableType(name="pressure_t", units=(Pa ** (1)), lowerBound=100, upperBound=1e+10, initialGuess=100000, absoluteTolerance=1e-05, valueConstraint=0)¶
- variable_types.temperature_t = daeVariableType(name="temperature_t", units=(K ** (1)), lowerBound=0, upperBound=100000, initialGuess=300, absoluteTolerance=0.01, valueConstraint=0)¶
- variable_types.fraction_t = daeVariableType(name="fraction_t", units=, lowerBound=-0.1, upperBound=2, initialGuess=0.25, absoluteTolerance=1e-06, valueConstraint=0)¶
- variable_types.no_t = daeVariableType(name="no_t", units=, lowerBound=-1e+20, upperBound=1e+20, initialGuess=0, absoluteTolerance=1e-05, valueConstraint=0)¶
- variable_types.moles_t = daeVariableType(name="moles_t", units=(mol ** (1)), lowerBound=0, upperBound=1e+20, initialGuess=1, absoluteTolerance=1e-05, valueConstraint=0)¶
- variable_types.molar_flux_t = daeVariableType(name="molar_flux_t", units=(m ** (-2))*(mol ** (1))*(s ** (-1)), lowerBound=-1e+20, upperBound=1e+20, initialGuess=0.001, absoluteTolerance=1e-05, valueConstraint=0)¶
- variable_types.molar_concentration_t = daeVariableType(name="molar_concentration_t", units=(m ** (-3))*(mol ** (1)), lowerBound=0, upperBound=1e+10, initialGuess=1, absoluteTolerance=1e-05, valueConstraint=0)¶
- variable_types.molar_flowrate_t = daeVariableType(name="molar_flowrate_t", units=(mol ** (1))*(s ** (-1)), lowerBound=-1e+10, upperBound=1e+10, initialGuess=0, absoluteTolerance=1e-05, valueConstraint=0)¶
- variable_types.heat_t = daeVariableType(name="heat_t", units=(J ** (1)), lowerBound=-1e+20, upperBound=1e+20, initialGuess=1000, absoluteTolerance=1e-05, valueConstraint=0)¶
- variable_types.heat_flux_t = daeVariableType(name="heat_flux_t", units=(W ** (1))*(m ** (-2)), lowerBound=-1e+20, upperBound=1e+20, initialGuess=0, absoluteTolerance=1e-05, valueConstraint=0)¶
- variable_types.heat_transfer_coefficient_t = daeVariableType(name="heat_transfer_coefficient_t", units=(K ** (-1))*(W ** (1))*(m ** (-2)), lowerBound=0, upperBound=1e+10, initialGuess=100, absoluteTolerance=1e-05, valueConstraint=0)¶
- variable_types.power_t = daeVariableType(name="power_t", units=(W ** (1)), lowerBound=-1e+20, upperBound=1e+20, initialGuess=0, absoluteTolerance=1e-05, valueConstraint=0)¶
- variable_types.specific_heat_capacity_t = daeVariableType(name="specific_heat_capacity_t", units=(J ** (1))*(K ** (-1))*(kg ** (-1)), lowerBound=0, upperBound=1e+20, initialGuess=1000, absoluteTolerance=1e-05, valueConstraint=0)¶
- variable_types.density_t = daeVariableType(name="density_t", units=(kg ** (1))*(m ** (-3)), lowerBound=0, upperBound=1e+20, initialGuess=1000, absoluteTolerance=1e-05, valueConstraint=0)¶
- variable_types.thermal_conductivity_t = daeVariableType(name="thermal_conductivity_t", units=(K ** (-1))*(W ** (1))*(m ** (-1)), lowerBound=0, upperBound=1e+10, initialGuess=1, absoluteTolerance=1e-05, valueConstraint=0)¶
- variable_types.dynamic_viscosity_t = daeVariableType(name="dynamic_viscosity_t", units=(Pa ** (1))*(s ** (1)), lowerBound=0, upperBound=1e+10, initialGuess=0.001, absoluteTolerance=1e-06, valueConstraint=0)¶
- variable_types.diffusivity_t = daeVariableType(name="diffusivity_t", units=(m ** (2))*(s ** (-1)), lowerBound=0, upperBound=100000, initialGuess=0.001, absoluteTolerance=1e-08, valueConstraint=0)¶
- variable_types.amount_adsorbed_t = daeVariableType(name="amount_adsorbed_t", units=(kg ** (-1))*(mol ** (1)), lowerBound=-1e+20, upperBound=1e+20, initialGuess=1, absoluteTolerance=1e-05, valueConstraint=0)¶