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analysis than a final plant design. Therefore, it is better if the thermodynamic results are not biased by the different heat exchanger costs at this point. The rest of this section explains in detail the behavior of the cycle parameters with respect to the total heat exchanger volume. Figure 6.11 shows the value of the optimum pressure ratio for different total heat exchanger volumes. Unlike the case of the normal Brayton cycle the optimum pressure ratio is constant (the analysis was performed with a pressure ratio step of 0.05) at the value 2.6. 3 2.75 2.5 2.25 2 80 110 140 170 200 Total Heat Exchanger Volume (m3) Figure 6.11 Optimum pressure ratio for recompression cycle Compared to the normal Brayton cycle the recompression cycle has another parameter that has to be evaluated, the recompressed fraction, i.e. the fraction of flow that is recompressed in the recompressing compressor and does not go through the pre-cooler. Once the high and low temperature recuperator volumes are selected the recompressed fraction is fixed as well. Figure 6.12 shows the resulting value of the recompressed fraction for the range of 80 to 200 m3 of total heat exchanger volume. Its value varies between ~ 0.37 and ~ 0.42. The effectiveness of the low temperature recuperator starts at 124 Optimum Pressure RatioPDF Image | Advanced Nuclear Power Technology Program A Supercritical Carbon Dioxide Cycle for Next Generation Nuclear Reactors
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