modelVolumeATh
Mixing flue gases volume with 2 inlets and 2 outlets and thermal input
Information
## Copyright © EDF 2002 - 2026 ## ThermoSysPro Version 4.2
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| Units.SI.Volume | V | 1 | Volume |
| Units.SI.AbsolutePressure | P0 | 1e5 | Initial fluid pressure (active if dynamic_mass_balance=true and steady_state=false) |
| Units.SI.Temperature | T0 | 400 | Initial fluid temperature (active if steady_state=false) |
| Boolean | dynamic_mass_balance | false | true: dynamic mass balance equation - false: static mass balance equation |
| Boolean | dynamic_composition_balance | false | true: dynamic fluid composition balance equation - false: static fluid composition balance equation |
| Boolean | steady_state | true | true: start from steady state - false: start from (P0, h0) |
| Units.SI.Density | p_rho | 0 | If > 0, fixed fluid density |
| Units.SI.SpecificEnthalpy | hr | 2501569 | Water/steam reference specific enthalpy at 0.01°C |
| Real | Xco20 | 0.0 | CO2 mass fraction (active if steady_state=false) |
| Real | Xh2o0 | 0.05 | H20 mass fraction (active if steady_state=false) |
| Real | Xo20 | 0.23 | O2 mass fraction (active if steady_state=false) |
| Real | Xso20 | 0 | SO2 mass fraction (active if steady_state=false) |
Connectors
| Type | Name | Default | Description |
|---|---|---|---|
| Connectors.FlueGasesInlet | Ce1 | ||
| Connectors.FlueGasesOutlet | Cs2 | ||
| Connectors.FlueGasesOutlet | Cs1 | ||
| Thermal.Connectors.ThermalPort | Cth | ||
| Connectors.FlueGasesInlet | Ce2 |
Components
| Type | Name | Default | Description |
|---|---|---|---|
| Units.SI.Temperature | T | Fluid temperature | |
| Units.SI.AbsolutePressure | P | Fluid pressure | |
| Units.SI.SpecificEnthalpy | h | Fluid specific enthalpy | |
| Units.SI.Density | rho | Fluid density | |
| Units.SI.SpecificHeatCapacity | cp | Fluid spécific heat capacity | |
| Real | Xco2 | CO2 mass fraction | |
| Real | Xh2o | H20 mass fraction | |
| Real | Xo2 | O2 mass fraction | |
| Real | Xso2 | SO2 mass fraction | |
| Real | Xn2 | N2 mass fraction | |
| Units.SI.MassFlowRate | BQ | Right hand side of the mass balance equation | |
| Units.SI.Power | BH | Right hand side of the energybalance equation | |
| Units.SI.MassFlowRate | BXco2 | Right hand side of the CO2 balance equation | |
| Units.SI.MassFlowRate | BXh2o | Right hand side of the H2O balance equation | |
| Units.SI.MassFlowRate | BXo2 | Right hand side of the O2 balance equation | |
| Units.SI.MassFlowRate | BXso2 | Right hand side of the SO2 balance equation | |
| Units.SI.SpecificEnthalpy | he1 | Fluid specific enthalpy at inlet #1 | |
| Units.SI.SpecificEnthalpy | he2 | Fluid specific enthalpy at inlet #2 | |
| Units.SI.SpecificEnthalpy | hs1 | Fluid specific enthalpy at outlet #1 | |
| Units.SI.SpecificEnthalpy | hs2 | Fluid specific enthalpy at outlet #2 |
Revisions
Authors Daniel Bouskela Baligh El Hefni