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Perfect Gas Condensation Recompression Partial Cycle Cycle Cycle Condensation Cycle Partial Condensation Cycle with Improved Regeneration Figure 13.3 Comparison of cycle losses [from Angelino, 1969] Probably the best way to display the effect of each component on cycle efficiency and to assess the cycle potential is to track the effect of each component on the deviation of the cycle from the Carnot cycle. Figure 13.3 shows this comparison as obtained by Angelino [Angelino, 1969]. He concluded that at turbine inlet pressures around 20 MPa the recompression cycle achieves the highest efficiency among the studied cycle layouts. At lower pressures the more complicated partial cooling cycle with improved regeneration performs the best. Since 20 MPa is a manageable pressure it was decided to adopt the recompression cycle for further investigation. Figure 13.4 shows the layout of the supercritical CO2 recompression cycle: note the split of the recuperator into two units and the use of a recompressing compressor. 13.1.3 Selection of the Optimum Heat Exchanger Volume As a larger total volume of heat exchangers is provided, the cycle efficiency is improved, but the efficiency improvement rate is decreasing with increasing volume. Therefore at some point the efficiency improvement is offset by the additional cost of the heat exchangers. In order to find the optimum volume of heat exchangers that minimize the capital cost per kWe the following analysis was performed. 273PDF Image | Advanced Nuclear Power Technology Program A Supercritical Carbon Dioxide Cycle for Next Generation Nuclear Reactors
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