modelBaseFilmModel
base class for film model where no source term for the reaction exists
Information
Base class for a film model. It provides the interface for all film models.
Additionally the balance equations at the phase boundary are written here: since the phase boundary is always calculated steady-state, the molar flow rates and the energy flow rates sum up to zero. Also the equations for the phase boundary molar flow rates of inert components are written in this class, namely:
N_flow_inert_PB = 0
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| Integer | nSL | MediumLiquid.nSubstance | |
| Integer | nSV | MediumVapour.nSubstance | |
| Boolean | enableDialog | true | |
| Boolean | StartUp_CCS | false | |
| Boolean | EQ | ||
| Propagated from Column › These variables are propagated from the column model and do not have to be set by the user! | |||
| Boolean[nSV] | inertVapour | fill(false, nSV) | |
| Boolean[nSL] | inertLiquid | fill(false, nSL) | |
| Integer | n | ||
| Integer | nS | ||
| Integer[nS,2] | mapping | {{i, i} for i in 1:nS} | |
| SI.Temperature | T_ref | ||
| Boolean | considerStartUp | false | |
| SI.Time | delay_startUp | 200 | |
| Boolean | smooth_startUp | false | |
| Boolean[nSV] | lowBoilingPoint | fill(false, nSV) | |
Components
| Type | Name | Default | Description |
|---|---|---|---|
| MediumVapour.ThermodynamicProperties | propsVap | ||
| SI.MoleFraction[n,nSV] | x_v_star | ||
| MediumVapour.ThermodynamicState | stateVap | ||
| SI.MoleFraction[nSV] | x_v_in | ||
| SI.Concentration[n,nSV] | c_v_star | ||
| SI.MoleFraction[n,nSL] | x_l | ||
| SI.MoleFraction[n,nSV] | x_v | ||
| SI.Pressure[n,nSL] | p_sat | ||
| MediumLiquid.ThermodynamicProperties | propsLiq | ||
| MediumLiquid.ThermodynamicState | stateLiq | ||
| SI.MoleFraction[n,nSL] | x_l_star | ||
| SI.Concentration[n,nSL] | c_l | ||
| SI.Concentration[n,nSL] | c_l_star | ||
| Real[n,nSL] | eta_comp | ||
| Real[n,nSL] | gamma | ||
| SI.MoleFraction[n,nS] | x_vap_liq | ||
| SI.Concentration[nSV] | c_v_in | ||
| SI.Concentration[n,nSV] | c_v | ||
| SI.VolumeFlowRate | Vdot_v_in | ||
| SI.VolumeFlowRate[n] | Vdot_v | ||
| SI.VolumeFlowRate[n] | Vdot_l | ||
| Real[n] | eps_liq | ||
| SI.MolarFlowRate[n,nSL] | Ndot_l_transfer | ||
| SI.MolarFlowRate[n,nSV] | Ndot_v_transfer | positive when entering the bulk phase | |
| SI.HeatFlowRate[n] | Edot_l_transfer | ||
| SI.HeatFlowRate[n] | Edot_v_transfer | ||
| SI.Pressure[n + 1] | p_hyd | ||
| SI.Pressure[n + 1] | p_v | ||
| SI.Temperature[n] | T_star | ||
| Real[n] | omega | ||
| Boolean[n] | startUp | ||
| Boolean[n] | before_transition | ||
| Real | k | ||
| Real[n,nSL] | rel_dev_liq | relative deviation from equilibrium, liquid | |
| Real[n,nSV] | rel_dev_vap | relative deviation from equilibrium, vapour | |
| Real | max_rel_dev_liq | max(rel_dev_liq) | maximum relative deviation from equilibrium, liquid |
| Real | max_rel_dev_vap | max(rel_dev_vap) | maximum relative deviation from equilibrium, vapour |
| HomotopyMethod | homotopyMethod |
Contents
| Name | Description |
|---|---|
| Reaction | |
| MediumLiquid | |
| MediumVapour | |
| BaseGeometry | |
| HomotopyMethod |