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In a heat exchanger which involves a phase-change of one of the fluids, the effective specific heat for the phase-changing fluid is infinity; therefore, Cüg is the heat capacity of the non-phase changing fluid (waste heat and water) for both the evaporator and the condenser (Shah and Sekulic, 1998). The effectiveness (ε) of the heat exchangers was calculated using Equation 6-3 shown below: ε QQüfØ 6-3 Q Actual heat transfer rate in the heat exchanger where Q©p° Maximum heat transfer rate in the heat exchanger ©p° 2©|r' j|r , k|r( where j|r Inlet temperature of the hot ôluid to the heat exchanger Tk|r Inlet temperature of the cold ôluid to the heat exchanger 6.4.1 Entropy Generation Analysis of the Proposed Model 6-4 Entropy generation is a measure of dissipated useful energy and degradation of the performance of an engineering system (Demirel, 2002). It accounts for the extent of irreversibility present in such a system. This section shows the entropy generation analysis of the dual heat source ORC configurations proposed in this research. 130PDF Image | Northumbria Research Link
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