Liu BT. Effect of working fluids in organic Rankine cycle for waste heat recovery, Energy 29 (2004): 1207–1217 Abstract ๏ท Analysis of the performance of an ORC ๏ influence of working fluids. ๏ท Investigated effects on thermal efficiency ๐๐กโ and total heat-recovery efficiency ๐๐ก . ๏ท Presence of Hydrogen bond (in H2O, NH3 and ethanol) ๏ wet fluid conditions due to >> vaporizing enthalpy ๏จ inappropriate for ORC systems. ๏ท Calculations: o ๐๐กโ is a weak function of ๐๐๐๐๐ก . o Max of ๐๐ก occurs at the appropriate ๐๐๐ฃ๐๐ between ๐๐๐,๐ค๐๐ ๐ก๐ โ๐๐๐ก and ๐๐๐๐๐ . o Max of ๐๐ก ↑ if ๐๐๐๐๐๐ก,๐๐ป ↑ o Max of ๐๐ก ↓ by using working fluids with a lower ๐๐๐๐๐ก . Results ๏ท ๐๐กโ is a weak function of ๐๐๐๐๐ก , although ๐๐กโ for working fluids with a lower ๐๐๐๐๐ก is lower. Conclusion ๏ท ๏ท The presence of hydrogen bond in certain molecules, such as water, ammonia, and ethanol results in wet fluids due to larger vaporizing enthalpy, and is regarded as inappropriate for ORC systems. Thermal efficiency for various working fluids is a weak function of the critical temperature, regardless of the fact that the thermal efficiency for working fluids with the lower critical temperature is lower. ๏ท ๏ท In general, the maximum value of total heat-recovery efficiency occurs at the appropriate evaporating temperature that is between the inlet temperature of waste heat and the condensing temperature. The maximum value of total heat-recovery efficiency increases with the increase of the inlet temperature of the waste heat ๐๐๐๐๐๐ก,๐ค๐๐ ๐ก๐ โ๐๐๐ก and decreases it by using working fluids of the lower critical temperature ๐๐๐๐๐ก . Analysis using a constant waste heat temperature or based on thermal efficiency may result in considerable deviation for system design relative to the varying temperature conditions of the actual waste heat recovery.