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Power generation with ORC machines low-grade waste heat

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Power generation with ORC machines low-grade waste heat ( power-generation-with-orc-machines-low-grade-waste-heat )

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148 V. Minea / Applied Thermal Engineering 69 (2014) 143e154 2.5 2 1.5 1 0.5 0 ORC-50 30 25 20 15 10 5 0 ORC-50 80 85 90 95 100 105 110 115 120 Waste heat inlet temperature, °C (b) Variable feed pump speed: 0-60 Hz Cooling fluid inlet temperature = 15°C 30 C Variable feed pump speed: 0-60 Hz 30°C Cooling fluid inlet temperature = 15°C 80 85 90 95 100 105 110 115 120 Waste heat input temperature, °C (a) Fig. 4. Organic fluid flow rate (a) and superheating (b) as functions of waste heat and cooling fluid inlet temperatures, with feed pump operating at variable speed (0e60 Hz). 1.019 (133.2) 2s Dpev = 30 kPa 26°C 0.241 (20.3) Dpcd = 30 kPa 2a Tev = 90°C 4 94°C Evaporator 5 Preheater 3 Waste heat thermal power input 526.8 kW (5 616 kWh) 100% Electrical power output 39.9 kW (426 kWh) 7.57% 1 Tcd = 34.6°C Condenser 6a 6s 6 38°C Expander outlet state 6 – without liquid injection 6s – adiabatic expansion 6a – actual, with liquid injection 105°C / 20°C Mass enthalpy, kJ/kg (a) Test AD-14: energy balance (experimental error = 1%) Condenserthermalpowerrejection 0.18% 482.8 kW (5147 kWh) 91.6% (b) Fig. 5. (a) Typical thermodynamic cycle of test AD-14 using waste heat and cooling fluid inlet temperatures of 105 C and 20 C, respectively; (b) measured energetic balance; Tcd: condensing temperature; Tev: evaporating temperature; Dp: pressure drop. components causing irreversibility. Consequently, improving the evaporator and condenser design and thermal performance in or- der to reduce irreversibility is crucial in enhancing the ORC cycle’s overall performance. The ORC machines using low-temperature heat sources require large evaporator and condenser heat transfer areas to extract the same amount of energy as high-temperature systems. This limits the use of low-temperature resources and 50 ORC-50 emphasizes the necessity of optimum design and cost-effective ORC plants. Exergy destruction also occurs during the non-isentropic expansion process. For a given waste (source) heat inlet tempera- ture, as the inlet pressure and temperature of the organic fluid in the expander increase, the enthalpy drop increases and, corre- spondingly, the exergy destruction rate decreases, while the cycle 50 45 40 35 30 25 20 15 10 5 0 ORC-50 Feed pump electrical power input 0.96 kW (10.23 kWh) Variable feed pump speed: 0-60 Hz Cooling inlet temperature = 15°C 20°C 30°C Net power average decrease = 12.3% Waste heat inlet temperature 105°C 85°C Net power average decrease = 19.4% 45 40 35 30 25 20 15 10 5 0 80 85 90 95 100 105 110 115 120 Waste heat inlet temperature, °C (a) 10 15 20 25 30 35 Cooling fluid inlet temperature, °C (b) Fig. 6. (a) Net power output as a function of waste heat (a) and cooling fluid (b) inlet temperatures with the feed pump running at variable speed (0e60 Hz). Net power output, kW Net power output, kW Evaporator superheating, °C Pressure, MPa,a (psig) Organic fluid flow rate, kg/s

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