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.
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