Low-Grade Heat Conversion into Power Using Small Scale Organic Rankine Cycles

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Low-Grade Heat Conversion into Power Using Small Scale Organic Rankine Cycles ( low-grade-heat-conversion-into-power-using-small-scale-organ )

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5.4.3 Heat source temperature and pinch point temperature difference Figure 5.8 shows the influence of the heat source temperature on the system performance. The pinch point and the temperature difference between the heat reservoir and the turbine inlet are kept at 3 °C and 10 °C, respectively, and the turbine inlet point is maintained on the saturation curve while the temperature of the water is increased. The increase in heat source temperature is followed by a decrease in exergetic efficiency while the energy efficiency remains almost constant. The degree of thermodynamic perfection decreases and passes through a minimum. 20 86 18 85 16 14 12 10 83 R600 Thermal eff. (%) Exergy eff. (%) Degree of therm. perf. (%) 8 6 4 2 84 82 81 0 80 60 65 70 75 80 85 90 95 100 Heat source temperature (°C) Figure 5.8 - Variation of the performance parameters with the temperature of the heat source On Figures 5.9 and 5.10, the influence of the pinch point temperature difference can be appreciated. The increase of the pinch point reduces the exergetic efficiency but at the same time improves the thermodynamic behavior of the system. These graphs reveal an opposition between both exergetic efficiency and degree of thermodynamic efficiency; what was observed earlier on Figures 5.7b and 5.7c. Page | 128 Energy and Exergy efficiencies (%) Degree of thermodynamic perfection (%)

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