Supercritical Carbon Dioxide Cycle for Next Generation Nuclear Reactors

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Supercritical Carbon Dioxide Cycle for Next Generation Nuclear Reactors ( supercritical-carbon-dioxide-cycle-next-generation-nuclear-r )

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for that analysis. Re-heat was investigated only for the 120m3 case of total heat exchanger volume (not including the volume of re-heaters, which will be estimated in Chapter 7). The pressure drops in the intermediate heat exchanger and the re-heaters was varied in order to capture the effect of pressure drops on the cycle efficiency in the same manner as in the non-re-heated recompression cycle. The results will be used for the optimization of the intermediate heat exchangers and re-heaters in Chapter 7. Figure 6.43 shows the effect of one and two stages of re-heat on the cycle efficiency for zero pressure drop in the intermediate heat exchanger and re-heaters. The behavior is similar to that of the simple Brayton cycle. The first stage of re-heating introduces about 1.2 % efficiency improvement, while the second only 0.46%. This indicates that using more than one stage of re-heat may not be economically attractive. This question will be answered in Chapter 7, where the benefit of re-heating is evaluated based on the cost of the re-heaters. 48 46 44 42 Pressure Drops: IHX = 500 kPa 1st Reheater = 0kPa 2nd Reheater = 500 kPa Pressure Drops: IHX = 0 kPa 1st Reheater = 500 kPa 2nd Reheater = 500 kPa Two re-heats Pressure Drops: IHX = 500 kPa 1st Reheater = 500 kPa 2nd Reheater = 0 kPa 0 400 800 1200 1600 Total Pressure Drop (kPa) Figure 6.44 Efficiency for different total pressure drops in IHX and re-heaters Figure 6.44 plots the cycle efficiency vs. the sum of the intermediate heat exchanger and re-heaters’ pressure drops. It shows that each of these heat exchanger pressure drops has a different effect on the cycle efficiency. That is why we can see different cycle 152 Efficiency (%)

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