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ORC Power Systems: History, Status, Perspectives 300 250 200 150 100 50 −0.6 −0.4 −0.2 0 0.2 0.4 0.6 0.8 Fluid saturation line ORC process Regeneration process 1,2 3 6 4 5 Entropy [kJ/kg K] (a) (b) 300 250 200 150 100 50 0 500 1000 1500 2000 2500 3000 3500 300 250 200 150 100 50 0 500 1000 1500 2000 2500 3000 Thermal power [kW] Working fluid Heat source Working fluid Heat source Thermal power [kW] (c) (d) Figure 2.1: The processes forming an exemplary superheated/regenerated Organic Rankine cycle power plant in the T − s thermodynamic plane of the working fluid 2.1a, together with the corre- sponding process flow diagram 2.1b. 2.1c: Q − T diagram of the ORC evaporator, assuming that the energy source is flue gas at 300 oC, compared to the Q − T diagram of the boiler of a simple steam power plant 2.1d having as energy input flue gas at the same conditions. 15 Temperature [◦C] Temperature [◦C] Temperature [◦C]PDF Image | New Concepts FOR Organic Rankine Cycle Power Systems
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