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Sustainability 2015, 7 15371 where the subscript e represents the expander. The regenerator is assumed to have an effectiveness of 0.8, implying that the actual amount of heat transferred is 80% of the possible energy transfer from states 2 to 3. The regenerator effectiveness is defined as: where ε = q, (16) q, q, = h − h (17) q. = h − h (18) State 3 is assumed to be at a temperature 5 °C higher than the condenser saturation temperature. Using an effectiveness (ε) of 0.8, state 6 is calculated with the equation above. An exergy rate balance for the regenerator can be written as: Ex + Ex = Ex + Ex +Ex (19) The condenser specific energy balance follows: The exergy rate balance for the condenser: where (20) Ex = Ex + Ex + Ex + Ex (21) q =h−h Ex = 1−T +273×Q −Q (22) T +273 Ex = 1− T +273 Q (23) T + 273 T, = (T + T) 2 (24) Q, =m(h−h) (25) Q =mq (26) The pump isentropic efficiency is taken to be 0.7, and the specific enthalpy at state 5 is calculated using: h =(h−h)× 1 +h (27) η where h is the ideal exit specific enthalpy if the pump is isentropic. The exergy rate balance for the pump can be written as: where Ex+W =Ex+Ex (28) W =m(h−h) (29) PDF Image | Selection of Optimum Working Fluid for Organic Rankine Cycles
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