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CHAPTER 2: Organic Rankine Cycle – Literature Review same amount of thermal heat, lower water mass flow rate is required and consequently the pump power consumption is reduced compared to the ORC. Figure 2-7 Temperature-entropy diagram of water and some common organic working fluids Moreover, SRC often operates below the atmospheric pressure in order to enhance the thermal efficiency. The inevitable result of sub-atmospheric condensation is the infiltration of non-condensable gases into the system thus requiring the addition of de-aeration equipment or de-aerating feed-water heater (McMahan 2006). In contrast, with the availability of a wide range of organic fluids it is possible to select those with high condensation pressure and facilitate above-atmospheric condensation with no or little maintenance. Furthermore, with the characteristics of water (low density and large enthalpy drop), the expander design for SRC is often complex and costly with multi-stage (more than three) architecture and with extraction points between each stage to increase the cycle efficiency and remove the non-condensable gases. In contrast, with the characteristics of organic fluids (large density and small enthalpy drop), the ORC expander design is simpler with one or two stages and lower peripheral 21 | P a g ePDF Image | SMALL-SCALE RADIAL INFLOW TURBINE FOR WHR ORC
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