modelPartialDiscretizedHEX
Extends from ThermofluidStream.Utilities.DropOfCommonsPlus.
Information
This is the partial parent class for undirected discretized heat exchangers. It contains the common equations, summary calculations and conduction elements used by the concrete heat exchanger models. The external rear and fore connectors are declared by the concrete models.
The conduction elements are computing a heat transfer coefficient between their heatport and the fluid contained. They are replaceable with a choice between a single-phase and a two-phase version, both can be further parametrized. Although the single-phase version works for two-phase media (not the other way around), using the two-phase one for two-phase media enables to set different heat transfer coefficients depending on the phase (liquid/gaseous/2-phase) state of the medium.
Note that since the model uses conductionElements as discrete control volumes that in turn assume quasi-stationary mass and, therefore, are part of a fluid stream rather than break it into two (like a full volume would), the same holds for both sides of the heat exchanger – they are part of a fluid stream and don't break it. The quasi-stationary mass assumption also implies that for (fast) changing masses/densities in any of the conduction elements the heat exchanger will (slightly) violate the conservation of energy. Furthermore, the conduction elements change their behavior for reversed mass flow, therefore, this model asserts for negative mass flow with the level "DropOfCommons.assertionLevel".
The parameters A (heat transferring area), k_wall (heat
transfer coefficient of the wall between the streams) and the heat transfer
coefficients in the conduction elements scale the transferred heat (the middle
only if the wall and the latter only of the heat transfer into a fluid is the
choke of the heatflow).
The parameter V determines the amount of fluid in the heat exchanger
and, therefore, the dynamic for non-steady states.
The "Initialization" tab allows for a mass flow initialization for both paths, as well as to determine from which direction the enthalpy in the control volumes should be initialized (fore/rear), or if it should start with a given enthalpy. The other option is to initialize the enthalpy with a given value.
The "Advanced" tab allows to modify the mass flow that triggers the reverse-mass-flow-assertion and has an option to enforce global conservation of energy. The latter is done by feeding back any energy the conduction elements accumulated over time, basically making it impossible to store energy in their fluid long-term. While this enforces long-term conservation of energy, it changes the medium-/short-term dynamics of the system and is, therefore, disabled by default.
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| Integer | nCells | 3 | Number of discretization elements |
| Boolean | calculate_efficiency | false | = true, if heat exchanger efficiency is calculated |
| Boolean | d1A | displayParameters and displayArea | displayArea at position 1 |
| Heat transfer parameters | |||
| SI.Area | A | 10 | Heat transfer area |
| SI.Volume | V_Hex | 0.001 | Volume for heat transfer calculation |
| SI.CoefficientOfHeatTransfer | k_wall | 100 | Coefficient of heat transfer of pipe wall |
| Initialization › Mass flow rate | |||
| Boolean | initializeMassFlow | false | = true, if inlet mass flow rates are initialized |
| SI.MassFlowRate | m_flow_0_A | 0 | Initial mass flow rate for side A |
| SI.MassFlowRate | m_flow_0_B | 0 | Initial mass flow rate for side B |
| Advanced | |||
| Boolean | enforce_global_energy_conservation | false | = true, if global conservation of energy is enforced |
| SI.MassFlowRate | m_flow_reg | dropOfCommons.m_flow_reg | Regularization mass flow to switch between positive- and negative-massflow model |
| Initialization › Enthalpy | |||
| ThermofluidStream.Undirected.Processes.Internal.InitializationMethodsCondElement | init_A | ThermofluidStream.Undirected.Processes.Internal.InitializationMethodsCondElement.h | Initialization method for h side A |
| MediumA.SpecificEnthalpy | h0_A | MediumA.h_default | Start value for specific enthalpy side A |
| ThermofluidStream.Undirected.Processes.Internal.InitializationMethodsCondElement | init_B | ThermofluidStream.Undirected.Processes.Internal.InitializationMethodsCondElement.h | Initialization method for h side B |
| MediumB.SpecificEnthalpy | h0_B | MediumB.h_default | Start value for specific enthalpy side B |
| Layout › Display parameters | |||
| Boolean | displayArea | true | = true, if heat transfer area A is displayed |
Components
| Type | Name | Default | Description |
|---|---|---|---|
| SI.HeatFlowRate | Q_flow_A | sum(thermalElementA.heatPort.Q_flow) | Heat flow rate into medium A |
| SI.HeatFlowRate | Q_flow_B | sum(thermalElementB.heatPort.Q_flow) | Heat flow rate into medium B |
| SI.MassFlowRate | m_flow_A | Mass flow rate on side A | |
| SI.MassFlowRate | m_flow_B | Mass flow rate on side B | |
| SI.Mass | M_A | sum(thermalElementA.M) | Mass on side A |
| SI.Mass | M_B | sum(thermalElementB.M) | Mass on side B |
| SI.Energy | deltaE_system | sum(thermalElementA.deltaE_system) + sum(thermalElementB.deltaE_system) | Error in global conservation of energy |
| ThermofluidStream.HeatExchangers.Internal.DiscretizedHEXSummary | summary | Summary record of quantities | |
| Modelica.Thermal.HeatTransfer.Components.ThermalConductor[nCells] | thermalConductor | ||
| ConductionElementA[nCells] | thermalElementA | ||
| ConductionElementB[nCells] | thermalElementB |
Contents
| Name | Description |
|---|---|
| MediumA | Medium model side A |
| MediumB | Medium model side B |
| ConductionElementA | |
| ConductionElementB | |
| efficiencyprotected |