modelTank

Ice tank with performance based on performance curves

Extends from Buildings.Fluid.Interfaces.TwoPortHeatMassExchanger (Partial model transporting one fluid stream with storing mass or energy).

Information

This model implements an ice tank model whose performance is computed based on performance curves.

The model is based on the implementation of Guowen et al., 2020 and similar to the detailed EnergyPlus ice tank model ThermalStorage:Ice:Detailed.

The governing equations are as follows:

The mass of ice in the storage mice is calculated as

d SOC/dt = Q̇/(Hf   mice,max)

mice = SOC   mice,max

where SOC is state of charge, is the heat transfer rate of the ice tank, positive for charging and negative for discharging, Hf is the fusion of heat of ice and mice,max is the nominal mass of ice in the storage tank.

The heat transfer rate of the ice tank is computed using

Q̇ = Qsto,nom   q*,

where Qsto,nom is the storage capacity and q* is a normalized heat flow rate. The storage capacity is

Qsto,nom = Hf   mice,max,

where Hf is the latent heat of fusion of ice and mice,max is the maximum ice storage capacity.

The normalized heat flow rate is computed using performance curves for charging (freezing) or discharging (melting). For charging, the heat transfer rate q* between the chilled water and the ice in the thermal storage tank is calculated using

q* Δt = C1 + C2x + C3 x2 + [C4 + C5x + C6 x2]ΔTlmtd*

where Δt is the time step of the data samples used for the curve fitting, C1-6 are the curve fit coefficients, x is the fraction of charging, also known as the state-of-charge, and Tlmtd* is the normalized LMTD calculated using Buildings.Fluid.Storage.Ice.BaseClasses.calculateLMTDStar. Similarly, for discharging, the heat transfer rate q* between the chilled water and the ice in the thermal storage tank is

- q* Δt = D1 + D2(1-x) + D3 (1-x)2 + [D4 + D5(1-x) + D6 (1-x)2]ΔTlmtd*

where Δt is the time step of the data samples used for the curve fitting, D1-6 are the curve fit coefficients.

The normalized LMTD ΔTlmtd* uses a nominal temperature difference of 10 Kelvin. This value must be used when obtaining the curve fit coefficients.

The log mean temperature difference is calculated using

ΔTlmtd* = ΔTlmtd/Tnom

ΔTlmtd = (Tin - Tout)/ln((Tin - Tfre)/(Tout - Tfre))

where Tin is the inlet temperature, Tout is the outlet temperature, Tfre is the freezing temperature and Tnom is a nominal temperature difference of 10 Kelvin.

Usage

This model requires the fluid to flow from port_a to port_b. Otherwise, the simulation stops with an error.

Reference

Strand, R.K. 1992. “Indirect Ice Storage System Simulation,” M.S. Thesis, Department of Mechanical and Industrial Engineering, University of Illinois at Urbana-Champaign.

Guowen Li, Yangyang Fu, Amanda Pertzborn, Jin Wen and Zheng O'Neill. An Ice Storage Tank Modelica Model: Implementation and Validation. Modelica Conferences. 2021. doi:10.3384/ecp21181177.

Parameters

TypeNameDefaultDescription
BooleanhomotopyInitialization (from TwoPortHeatMassExchanger)true= true, use homotopy method
Buildings.Fluid.Storage.Ice.Data.Tank.GenericperPerformance data
Modelica.Units.SI.SpecificHeatCapacitycpMedium.specificHeatCapacityCp(Medium.setState_pTX(p = Medium.p_default, T = 273.15, X = Medium.X_default))Specific heat capacity of working fluid
Assumptions
BooleanallowFlowReversal (from PartialTwoPort)true= false to simplify equations, assuming, but not enforcing, no flow reversal
Nominal condition
Modelica.Units.SI.MassFlowRatem_flow_nominal (from PartialTwoPortInterface)Nominal mass flow rate
Modelica.Units.SI.PressureDifferencedp_nominal (from TwoPortFlowResistanceParameters)Pressure difference
Advanced
Modelica.Units.SI.MassFlowRatem_flow_small (from PartialTwoPortInterface)1E-4*abs(m_flow_nominal)Small mass flow rate for regularization of zero flow
Advanced › Diagnostics
Booleanshow_T (from PartialTwoPortInterface)false= true, if actual temperature at port is computed
Flow resistance
BooleancomputeFlowResistance (from TwoPortFlowResistanceParameters)true=true, compute flow resistance. Set to false to assume no friction
Booleanfrom_dp (from TwoPortFlowResistanceParameters)false= true, use m_flow = f(dp) else dp = f(m_flow)
Realn (from TwoPortFlowResistanceParameters)2Flow exponent, n=1 for laminar, n=2 for turbulent
BooleanlinearizeFlowResistance (from TwoPortFlowResistanceParameters)false= true, use linear relation between m_flow and dp for any flow rate
RealdeltaM (from TwoPortFlowResistanceParameters)0.1Fraction of nominal flow rate where flow transitions to laminar
Dynamics › Nominal condition
Modelica.Units.SI.Timetau (from TwoPortHeatMassExchanger)30Time constant at nominal flow (if energyDynamics <> SteadyState)
Dynamics › Conservation equations
Modelica.Fluid.Types.DynamicsenergyDynamics (from TwoPortHeatMassExchanger)Modelica.Fluid.Types.Dynamics.DynamicFreeInitialType of energy balance: dynamic (3 initialization options) or steady state
Initialization
Medium.AbsolutePressurep_start (from TwoPortHeatMassExchanger)Medium.p_defaultStart value of pressure
Medium.TemperatureT_start (from TwoPortHeatMassExchanger)Medium.T_defaultStart value of temperature
Medium.MassFraction[Medium.nX]X_start (from TwoPortHeatMassExchanger)Medium.X_defaultStart value of mass fractions m_i/m
Medium.ExtraProperty[Medium.nC]C_start (from TwoPortHeatMassExchanger)fill(0, Medium.nC)Start value of trace substances
RealSOC_startStart value for state of charge
Dynamics heat exchanger › Conservation equations
Modelica.Fluid.Types.DynamicsenergyDynamicsHexModelica.Fluid.Types.Dynamics.DynamicFreeInitialFormulation of energy balance for heat exchanger internal fluid mass
Modelica.Units.SI.TimetauHex30Time constant of working fluid through the heat exchanger at nominal flow

Connectors

TypeNameDefaultDescription
Modelica.Fluid.Interfaces.FluidPort_aport_a (from PartialTwoPort)Fluid connector a (positive design flow direction is from port_a to port_b)
Modelica.Fluid.Interfaces.FluidPort_bport_b (from PartialTwoPort)Fluid connector b (positive design flow direction is from port_a to port_b)
Modelica.Blocks.Interfaces.RealOutputSOCstate of charge
Modelica.Blocks.Interfaces.RealOutputTTemperature of the fluid leaving at port_b
Modelica.Blocks.Interfaces.RealOutputmIceMass of remaining ice
Modelica.Blocks.Interfaces.RealOutputQ_flowHeat flow rate, positive during charging, negative when melting the ice

Components

TypeNameDefaultDescription
Modelica.Units.SI.MassFlowRatem_flow (from PartialTwoPortInterface)port_a.m_flowMass flow rate from port_a to port_b (m_flow > 0 is design flow direction)
Modelica.Units.SI.PressureDifferencedp (from PartialTwoPortInterface)port_a.p - port_b.pPressure difference between port_a and port_b
Medium.ThermodynamicStatesta_a (from PartialTwoPortInterface)if allowFlowReversal then Medium.setState_phX(port_a.p, noEvent(actualStream(port_a.h_outflow)), noEvent(actualStream(port_a.Xi_outflow))) else Medium.setState_phX(port_a.p, noEvent(inStream(port_a.h_outflow)), noEvent(inStream(port_a.Xi_outflow)))Medium properties in port_a
Medium.ThermodynamicStatesta_b (from PartialTwoPortInterface)if allowFlowReversal then Medium.setState_phX(port_b.p, noEvent(actualStream(port_b.h_outflow)), noEvent(actualStream(port_b.Xi_outflow))) else Medium.setState_phX(port_b.p, noEvent(port_b.h_outflow), noEvent(port_b.Xi_outflow))Medium properties in port_b
Buildings.Fluid.MixingVolumes.MixingVolumevol (from TwoPortHeatMassExchanger)
Buildings.Fluid.FixedResistances.PressureDroppreDro (from TwoPortHeatMassExchanger)Flow resistance

Revisions

  • January 26, 2022, by Michael Wetter:
    Refactored model to new architecture. Changed model to allow idealized control. Avoided SOC to be outside [0, 1].
  • December 14, 2021, by Yangyang Fu:
    First implementation.