| Real | pi (from Flow1DBase) | Modelica.Constants.pi | |
| Integer | N (from Flow1DBase) | 2 | Number of nodes for thermal variables |
| Integer | Nw (from Flow1DBase) | N - 1 | Number of volumes on the wall interface |
| Integer | Nt (from Flow1DBase) | 1 | Number of tubes in parallel |
| SI.Distance | L (from Flow1DBase) | | Tube length |
| SI.Position | H (from Flow1DBase) | 0 | Elevation of outlet over inlet |
| SI.Area | A (from Flow1DBase) | | Cross-sectional area (single tube) |
| SI.Length | omega (from Flow1DBase) | | Perimeter of heat transfer surface (single tube) |
| SI.Length | Dhyd (from Flow1DBase) | omega/pi | Hydraulic Diameter (single tube) |
| Medium.MassFlowRate | wnom (from Flow1DBase) | | Nominal mass flowrate (total) |
| SI.PressureDifference | dpnom (from Flow1DBase) | 0 | Nominal pressure drop (friction term only!) |
| SI.PerUnit | Kfc (from Flow1DBase) | 1 | Friction factor correction coefficient |
| Boolean | DynamicMomentum (from Flow1DBase) | false | Inertial phenomena accounted for |
| ThermoPower.Choices.Flow1D.HCtypes | HydraulicCapacitance (from Flow1DBase) | ThermoPower.Choices.Flow1D.HCtypes.Downstream | Location of the hydraulic capacitance |
| Boolean | avoidInletEnthalpyDerivative (from Flow1DBase) | true | Avoid inlet enthalpy derivative |
| Boolean | allowFlowReversal (from Flow1DBase) | system.allowFlowReversal | = true to allow flow reversal, false restricts to design direction |
| SI.PerUnit | wnf (from Flow1DBase) | 0.02 | Fraction of nominal flow rate at which linear friction equals turbulent friction |
| SI.Acceleration | g (from Flow1DBase) | Modelica.Constants.g_n | |
| SI.PerUnit | dzdx (from Flow1DBase) | H/L | Slope |
| SI.Length | l (from Flow1DBase) | L/(N - 1) | Length of a single volume |
| SI.Volume | V (from Flow1DBase) | Nt*A*L | Total volume (all Nt tubes) |
| SI.PerUnit | alpha (from Flow1DFEM) | 1 | Numerical stabilization coefficient |
| SI.PerUnit | ML (from Flow1DFEM) | 0 | Mass Lumping Coefficient |
| SI.PerUnit | wnf_bc (from Flow1DFEM) | 0.01 | Fraction of the nominal total mass flow rate for boundary condition FEM regularization |
| SI.PerUnit | wnf_alpha (from Flow1DFEM) | 0.01 | Fraction of the nominal total mass flow rate for stabilization parameter regularization |
| Boolean | regularizeBoundaryConditions (from Flow1DFEM) | false | Regularize boundary condition matrices |
| Boolean | idealGasDensityDistribution (from Flow1DFEM) | false | Assume ideal-gas-type density distributions for mass balances |
| Boolean | evenN (from Flow1DFEM) | (div(N, 2)*2 == N) | The number of nodes is even |
| SI.Length | omega2 | omega | Perimeter of heat transfer surface wall 2 (single tube) |
| SI.Length | Dhyd2 | omega2/pi | Hydraulic Diameter wall2 (single tube) |
| Initialisation |
| Choices.FluidPhase.FluidPhases | FluidPhaseStart (from Flow1DBase) | Choices.FluidPhase.FluidPhases.Liquid | Fluid phase (only for initialization!) |
| Medium.AbsolutePressure | pstart (from Flow1DBase) | 1e5 | Pressure start value |
| Medium.SpecificEnthalpy | hstartin (from Flow1DBase) | if FluidPhaseStart == Choices.FluidPhase.FluidPhases.Liquid then 1e5 else if FluidPhaseStart == Choices.FluidPhase.FluidPhases.Steam then 3e6 else 1e6 | Inlet enthalpy start value |
| Medium.SpecificEnthalpy | hstartout (from Flow1DBase) | if FluidPhaseStart == Choices.FluidPhase.FluidPhases.Liquid then 1e5 else if FluidPhaseStart == Choices.FluidPhase.FluidPhases.Steam then 3e6 else 1e6 | Outlet enthalpy start value |
| Medium.SpecificEnthalpy[N] | hstart (from Flow1DBase) | linspace(hstartin, hstartout, N) | Start value of enthalpy vector (initialized by default) |
| Choices.Init.Options | initOpt (from Flow1DBase) | system.initOpt | Initialisation option |
| Boolean | noInitialPressure (from Flow1DBase) | false | Remove initial equation on pressure |
HeatTransfer2