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unit, where the waste heat from the exhaust to stack is used to preheat/evaporate the working fluid to the saturated vapour phase (state 4). The working fluid at the saturated vapour phase is passed through the turbine, where it is expanded to produce work. The work is transmitted to the generator via the connecting shaft to generate electricity. The working fluid exiting from the turbine (state 5) is sent to the condenser where heat is rejected from the working fluid to the condensing fluid. The loss of heat in the condenser causes the condensation of the working fluid back to the liquid phase to complete the cycle. 6.2 Waste Heat Quality 6.2.1 Waste Heat from Fryer Foul Gas The waste heat from the fryer foul gas is at a temperature of 120oC, a mass flow rate of 3.172 kg/s, and a mass composition of 60.6% H2O, 29.9% N2 and 9.5% O2. 6.2.2 Waste Heat from the Exhaust Stack The waste heat from the exhaust stack is at a temperature of 164oC, a mass flow rate of 10.51 kg/s and a mass composition of 5% CO2, 41.1% H2O, 50.6% N2 and 3.3% O2. 6.3 Building the IPSEpro Model of an ORC System Using IPSEpro PSE The developed MDK models presented above were put together in the IPSEpro PSE module in order to develop the entire ORC model. The model is developed using the following model parameter: 121PDF Image | OPTIMISING THERMAL ENERGY RECOVERY
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