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configured by Shaikh in 2011 and uses R134a as a working fluid. Before Shaikh (2011), Tarique (2011) obtained the compressor and configured it for expander duty. It was tested solely for expander performance as part of a comparison with other expanders. While the expander is small for practical uses it provides a good medium to experiment and understand the operation of scroll expanders. The expander is rated at 1500W input for compressor duty, and is expected to produce less during expander operation. This is due to losses internally, such as friction and leakages. Figure 4.1 shows the system used in analysis and assumptions are outlined below: • The efficiency of the generator is considered to be constant at 80%. • The inlet temperature to the expander is constant at 110 ̊C. • The isentropic efficiency of the pump is considered to be constant at 70%. • The environment temperature and pressure are set to 25 ̊C and 101.325 kPa. • All heat losses from the turbine, piping and pump are considered to be negligible. • The regenerator has an effectiveness of 0.8. • The temperature at state 3 is 5 ̊C higher than the temperature at state 4. • The source temperature is 120 ̊C. • The system is considered to be at steady state operation. 33PDF Image | Exergoeconomic Analysis and Optimization of ORC
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