modelBaseReboiler_test2
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| Boolean | delta_hv_medium | MediumVapour.delta_hv_medium | |
| SI.Temperature | T_v_start | T_vapour_start | |
| SI.Temperature | T_l_start | T_liquid_start | |
| Integer[nS,2] | mapping | {{1, 2}, {3, 1}} | parameter to map the different medium vectors one to another |
| Boolean[nSV] | inertVapour | {false, true, false, true} | |
| Boolean[nSL] | inertLiquid | {false, false, true} | |
| Integer | nS | 2 | number of species which are equal in vapour and liquid phase |
| Integer | nL | MediumLiquid.nSubstance - nS | number of additional substances which are only in liquid phase |
| Integer | nV | MediumVapour.nSubstance - nS | number of additional substances which are only in the vapour phase |
| Integer | nSL | MediumLiquid.nSubstance | |
| Integer | nSV | MediumVapour.nSubstance | |
| Real | eps_vap_start | 0.5 | |
| Boolean | fixedCirculation | false | |
| SI.Volume | V | Modelica.Constants.pi/4*(d_HX^2 - d_tube^2*n)*length_HX | |
| Real | zeta | 8.6 | |
| SI.Diameter | d_tube | 0.025 | outer diameter of tubes |
| SI.Diameter | d_HX | 0.35 | inner diameter of heat exchanger |
| Integer | Nw | 9 | number of rows in flow direction |
| Integer | n | 76 | number of tubes |
| SI.Length | length_HX | 0.75 | length of tubes |
| SI.Length | t_tube | 0.002 | wall thickness of the tubes |
| SI.Area | A_HT | Modelica.Constants.pi*(2*d_tube - t_tube)/2*length_HX*n | mean heat transfer area |
| Advanced | |||
| SI.Temperature | T_ref | systemTS.T_ref | reference temperature |
| Initialization | |||
| SI.MoleFraction[nSL] | x_l_start | {2e-2, 1 - 2e-2 - 0.057, 0.057} | |
| SI.MoleFraction[nSV] | x_v_start | {1 - 0.1 - 0.001, 0.0005, 0.01, 0.0005} | |
| SI.Temperature | T_vapour_start | 95 + 273.15 | |
| SI.Temperature | T_liquid_start | 95 + 273.15 | |
| Real | eps_liq_start | 0.071204 | |
| Boolean | initEQ | true | |
| InitOption | initOption | InitOption.initEQ | different initialization options |
| SI.Pressure | p_start | 1.025e5 | |
Components
| Type | Name | Default | Description |
|---|---|---|---|
| ThermalSeparation.SystemTS | systemTS | ||
| MediumVapour.BaseProperties | mediumVapour | ||
| MediumLiquid.BaseProperties | mediumLiquid | ||
| MediumLiquid.BaseProperties | mediumLiquidIn | ||
| SI.Density | rho_v | mediumVapour.d | density of the vapour, all components |
| SI.MolarMass | MM_v | mediumVapour.MM | molar mass of the vapour mixture |
| ThermalSeparation.Units.MolarEnthalpy | h_v | mediumVapour.h | |
| SI.MolarInternalEnergy | u_v | mediumVapour.u | |
| SI.Density | rho_l | mediumLiquid.d | density of the liquid, all components |
| SI.Density | rho_l_in | mediumLiquidIn.d | |
| SI.MolarMass | MM_l | mediumLiquid.MM | molar mass of the liquid mixture |
| SI.MolarMass | MM_l_in | mediumLiquidIn.MM | |
| ThermalSeparation.Units.MolarEnthalpy | h_l | mediumLiquid.h | |
| ThermalSeparation.Units.MolarEnthalpy | h_l_in | mediumLiquidIn.h | |
| SI.MolarInternalEnergy | u_l | mediumLiquid.u | |
| SI.Concentration[nSL] | c_l | ||
| SI.MoleFraction[nSL] | x_l | ||
| SI.Concentration[nSL] | c_l_in | ||
| SI.MoleFraction[nSL] | x_l_in | ||
| SI.Concentration[nSV] | c_v | ||
| SI.MoleFraction[nSV] | x_v | ||
| SI.Temperature | T_l_in | ||
| SI.Temperature | T_l | ||
| SI.Temperature | T_v | ||
| SI.VolumeFlowRate | Vdot_v | ||
| SI.VolumeFlowRate | Vdot_l | ||
| SI.VolumeFlowRate | Vdot_l_in | ||
| Real | eps_liq | ||
| Real | eps_vap | ||
| SI.MoleFraction[nSL] | x_l_star | ||
| SI.HeatFlowRate | Qdot_wall | ||
| SI.Pressure | p_out | ||
| SI.Pressure | p_in | ||
| SI.Pressure | p | ||
| PressureLoss | pressureLoss | ||
| SI.Pressure | p_initial | initial pressure in column | |
| SI.Pressure[2] | p_hyd | hydraulic pressure | |
| SI.Pressure | wassersaeule | eps_liq*d_HX*Modelica.Constants.g_n*rho_l |
Contents
| Name | Description |
|---|---|
 MediumVapour | |
| MediumLiquid | |
| PressureLoss |