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Figure 2-3: P-h diagram of a typical organic Rankine cycle demonstrated with R245fa. The lower vaporization temperature of organic fluids allows the application of the RC to low-grade heat sources and the conventional RC becomes economically impractical at input temperatures below 370 °C [6]. The slope of the vapor saturation line in relation to the isentropes eliminates the need for a high level of superheat. Working fluids with a vapor saturation line with a smaller slope than the isentropes in the area are considered “dry” because at the end of expansion, state 4, the working fluid is a superheated vapor. In a properly designed RC, vapor exits the expander at 100% quality, that is, state 4 is outside the vapor dome. If the working fluid crosses into the vapor dome during expansion, blade erosion and considerable stress can occur on the expander. Figure 2-3 shows no superheat is required to operate the ORC with a dry working fluid, whereas Figure 2-2 shows a significant amount of superheat is required to 6PDF Image | ORC WASTE HEAT RECOVERY SYSTEM WITH A TESLA-HYBRID
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