modelTraceDecayAdsorberBed

Parameters

Type	Name	Default	Description
Integer	nV	1	# of volumes
Boolean	use_tau	true	=true to specify reference resident time else based on carbon mass
Integer	iC	1	Index of substance for basis of residence time (tu_res)
Real	parents	fill(0, Medium.nC, Medium.nC)	Matrix of parent sources (sum(column) = 0 or 1) for each fission product 'daughter'. Row is daughter, Column is parent.
Advanced › Dynamics
Dynamics	energyDynamics	Dynamics.DynamicFreeInitial	Formulation of energy balances
Initialization › Start Value: Temperature
SI.Temperature[nV]	Ts_start	linspace_1D(T_a_start, T_b_start, nV)	Temperature
SI.Temperature	T_a_start	Medium.T_default	Temperature at port a
SI.Temperature	T_b_start	T_a_start	Temperature at port b
Visualization
Boolean	showName	true
Advanced
Boolean	use_HeatPort	false	=true to toggle heat port

Type	Name	Default	Description
Interfaces.FluidPort_Flow	port_a
Interfaces.FluidPort_Flow	port_b
HeatAndMassTransfer.Interfaces.HeatPort_State	heatPorts

Type	Name	Default	Description
SIadd.InverseTime[Medium.nC]	lambdas	fill(1e-3, Medium.nC)	Decay constant of trace substances
SI.SpecificVolume[Medium.nC]	K	fill(1e3, Medium.nC)	Dynamic adsorption coefficient
SI.Energy[Medium.nC]	Qs_decay	fill(1, Medium.nC)	Energy released per decay
SI.Time	tau_res	from_hr(1)	Specified residence time for chosen substance (iC) or mass of carbon
SI.Mass	mAdsorber	V_flow*tau_res/K[iC]	Specify total mass of adsorber
Units.HydraulicResistance	R	1	Hydraulic resistance across adsorber bed
SI.Density	d_adsorber	500	Density of adsorber bed
SI.SpecificHeatCapacity	cp_adsorber	1000	Specific heat capacity of adsorber bed
SIadd.ExtraPropertyFlowRate[nV + 1,Medium.nC]	mC_flows		Trace substance flow rate between volumes
SIadd.ExtraPropertyFlowRate[nV,Medium.nC]	mCs_decay		Amount of substance decayed across each volume
SI.HeatFlowRate[nV,Medium.nC]	Qs_perC		Heat released from decay per volume per substance
SI.HeatFlowRate[nV]	Qs		Heat released from decay per volume
SI.PressureDifference	dp		Pressure drop across adsorber bed (dp = port_a.p - port_b.p)
Medium.ThermodynamicState	state_a		Thermodynamic state at port_a
Medium.ThermodynamicState	state_b		Thermodynamic state at port_b
SI.MassFlowRate	m_flow	port_a.m_flow	Mass flow rate of carrier fluid
SI.VolumeFlowRate	V_flow	m_flow/Medium.density(state_a)
SI.Time[Medium.nC]	taus	K.*mAdsorber./V_flow
SI.Temperature[nV]	Ts_adsorber		Temperature of adsorber
SI.EnthalpyFlowRate[nV + 1]	H_flows		Enthalpy flow rate across volumes due to fluid flow
SI.Pressure[nV]	ps		Pressure of volumes

Name	Description
Medium