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fact that for the higher values of the plant capital cost the cost of heat exchangers is a smaller fraction and therefore the total capital cost is not as sensitive to the increase of their cost. Thus, the optimum value of the total heat exchanger volume is higher. 1.05 1.04 1.03 1.02 1.01 1 0.99 0.98 Original Plant 1000 $/kWe Original Plant 1500 $/kWe Original Plant 2000 $/kWe 80 100 120 140 160 3 Total Heat Exchanger Volume (m ) 180 200 Figure 13.5 Optimum size of heat exchangers for recompression cycles The target capital cost for advanced reactors is on the order of 1,000 $/kWe. If we assume this cost for the plant employing supercritical CO2 then the optimum total volume of the heat exchangers is 140 m3. However, since the difference in cost between 120 and 140 m3 is negligibly small (1 $/kWe) and since larger heat exchangers will introduce higher costs for installation etc., which were fixed in this analysis, 120 m3 of total heat exchanger volume is used as the reference total heat exchanger volume. 13.1.4 Selection of Operating Conditions The effect of the compressor inlet temperature on the cycle efficiency is especially important for supercritical CO2 cycles because it significantly affects the compression process: much more than ideal gas Brayton cycles. Since the cycle takes advantage of the 275 Actual Cost ($/kWe)/ Original Cost ($/kWePDF Image | Advanced Nuclear Power Technology Program A Supercritical Carbon Dioxide Cycle for Next Generation Nuclear Reactors
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