modelSQThesisModel

Non-regenerative ORC with double-PID control system and variable Tev

Information

Dynamic model of a non-recuperative Organic Rankine Cycle with its control system.

Modeling assumptions

  • The pressure drops are lumped into two punctual pressure drop components in the vapor lines
  • The control is performed using two PI controllers
  • The superheating is controlled with the pump speed and the evaporation temperature is controlled with the expander speed.
  • The properties of R245fa are calculated using CoolProp
  • The volumetric pump and the scroll expander are modeled using efficiency curves derived from experimental data

Reference

Quoilin, S. (2011). Sustainable energy conversion through the use of Organic Rankine Cycles for waste heat recovery and solar applications. Doctoral thesis, University of Liège, ​Liège, ​​Belgium.

Components

TypeNameDefaultDescription
ThermoCycle.Components.Units.Tanks.Tanktank
ThermoCycle.Components.Units.ExpansionAndCompressionMachines.PumpPump
ThermoCycle.Components.FluidFlow.Reservoirs.Source_CdotHeat_source
ThermoCycle.Obsolete.Hx_06122013Evaporator
ThermoCycle.Components.Units.ExpansionAndCompressionMachines.ElectricDrivegenerator
ThermoCycle.Components.Units.ExpansionAndCompressionMachines.Expanderexpander
ThermoCycle.Obsolete.Hx_06122013Condenser
ThermoCycle.Components.FluidFlow.Reservoirs.Source_CdotHeat_sink
ThermoCycle.Components.FluidFlow.Sensors.SensPsensP
ThermoCycle.Components.HeatFlow.Sensors.SensTpsensTp
ThermoCycle.Components.FluidFlow.Sensors.SensMdotsensMdot
ThermoCycle.Components.HeatFlow.Sensors.SensTsfsensTsf
ThermoCycle.Components.Units.ControlSystems.SQThesisControllercontrol_unit1
ThermoCycle.Components.FluidFlow.Sources.inputsdata
ThermoCycle.Components.Units.PdropAndValves.DPDP_cd
ThermoCycle.Components.Units.PdropAndValves.DPDP_ev