Modeling of a Low Temperature Rankine Cycle for Small Scale Cogen

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Modeling of a Low Temperature Rankine Cycle for Small Scale Cogen ( modeling-low-temperature-rankine-cycle-small-scale-cogen )

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Sylvain Quoilin Chapter 5 : Models The mechanical losses are defined by : where T m is the friction torque. The fictitious wall temperature is calculated by a heat balance between the mechanical losses, the heat exchanges between the wall and the fluid and between the wall and the ambient air : The mechanical power is equal to the internal expansion power minus the mechanical losses : Parameters of the model : This model is based on a 8 parameters that depend on the physical characteristics of the expander. Those parameters are : Swept volume of the scroll machine, in compressor mode. This volume is linked to the swept volume in expander mode by the built­in volume ratio. Built­in volume ratio Fictitious leakage area Nominal heat transfer coefficient for the supply fictitious heat exchanger. This coefficient is defined for a nominal flow rate. It has to be adapted to the real flow rate. Nominal heat transfer coefficient for the exhaust fictitious heat exchanger. Friction torque of the expander, determining the mechanical losses. Heat transfer coefficient for the ambient losses. Throat diameter of the fictitious nozzle introduced to model the pressure drops 78

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