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70 5 Siloxanes as working fluids in mini ORC systems 15 14 13 12 11 10 9 8 7 6 Case1 PL included Case1 no PL included Case2 PL included Case2 no PL included MDM D4 D5 D6 MD2M MD3M MD4M MM toluene Figure 5.2: ORC process net electric power, Pe,net. 26 24 22 20 18 16 14 12 10 Case1 PL included Case1 no PL included Case2 PL included Case2 no PL included MDM D4 D5 D6 MD2M MD3M MD4M MM toluene Figure 5.3: ORC process net electric efficiency, ηe,net. The enthalpy drop over the turbine, working fluid mass flow rate, volume flow at the tur- bine outlet, and recuperator effectiveness associated with the various working fluids are presented in Table 5.3. The fluid state at the turbine inlet and the condensation pressure at the corresponding condensation temperature of 50 ◦C (Case1) and 90 ◦C (Case2) are shown in Table 5.4. η ,% e,net P , kW e,netPDF Image | WORKING FLUID SELECTION AND DESIGN OF SMALL-SCALE WASTE HEAT RECOVERY SYSTEMS BASED ON ORGANIC RANKINE CYCLES
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