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this pressure drop. For zero pressure drop there is a slight change; the reason why the effect is not seen at higher pressure drop values is the crude step that was used in the optimization. If an infinitely small change was used a very slight change in the optimum volume fractions would be visible. The same is true for the optimum heat exchanger length. Figure 6.40 shows a very slight decrease of the optimum length of the high temperature recuperator and an even smaller increase of the pre-cooler length with the primary system pressure drop. In Chapter 4 it was demonstrated that a small deviation from the optimum volume fractions and optimum heat exchanger lengths does not significantly compromise the cycle efficiency. Therefore, it can be concluded that primary system pressure drop does not significantly affect the optimum cycle design and therefore the heat exchangers do not have to be redesigned for different primary system pressure drops. 2.2 1.9 1.6 1.3 1 Pre-cooler HT Recuperator LT Recuperator 0 100 200 300 400 500 Primary System Pressure Drop (kPa) Figure 6.40 Effect of primary system pressure drop on the optimum heat exchanger length 149 Optimum HX Length (m)PDF Image | Advanced Nuclear Power Technology Program A Supercritical Carbon Dioxide Cycle for Next Generation Nuclear Reactors
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