modelPressurizer_withWall

Parameters

TypeNameDefaultDescription
SI.SpecificHeatCapacitycp_wallHeat capacity of pressurizer wall
SI.Densityrho_wallDensity of pressurizer wall
SI.VolumeV_wallVolume of pressurizer wall
Assumptions
BooleanallowFlowReversalsystem.allowFlowReversal= true to allow flow reversal, false restrics to design direction
Assumptions › Dynamics
Types.DynamicsenergyDynamicssystem.energyDynamicsFormulation of energy balance
Types.DynamicsmassDynamicssystem.massDynamicsFormulation of mass balance
Initialization
RealVfrac_liquid_start0.5Initial fraction of volume in the liquid phase
SI.Pressurep_startsystem.p_startPressure start value
SI.SpecificEnthalpyh_liquid_startMedium.bubbleEnthalpy(Medium.setSat_p(p_start))Liquid specific enthalpy start value
SI.SpecificEnthalpyh_vapor_startMedium.dewEnthalpy(Medium.setSat_p(p_start))Vapour specific enthalpy start value

Connectors

TypeNameDefaultDescription
Interfaces.FluidPort_StatesprayPort
Interfaces.FluidPort_StatereliefPort
Interfaces.FluidPort_StatesurgePort
Modelica.Thermal.HeatTransfer.Interfaces.HeatPort_bheatTransfer_wall
Modelica.Thermal.HeatTransfer.Interfaces.HeatPort_aliquidHeater
Modelica.Thermal.HeatTransfer.Interfaces.HeatPort_avaporHeater

Components

TypeNameDefaultDescription
Modelica.Fluid.SystemsystemSystem properties
TRANSFORM.Fluid.Volumes.Pressurizerdrum2Phase
Modelica.Thermal.HeatTransfer.Components.HeatCapacitorCapacitance_wall

Contents

NameDescription
Medium
DrumType1. Select model 2. Set parameters (Total volume must match V_total)
BulkEvaporationVapor bubble transport from liquid to vapor phase
BulkCondensationLiquid droplet transport from vapor to liquid phase
MassTransfer_VLVapor-liquid interface mass transport coefficient
HeatTransfer_VLVapor-liquid interface heet transfer coefficient
HeatTransfer_WLWall-vapor heat transfer coefficient
HeatTransfer_WVWall-liquid heat transfer coefficient