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central cavity is reserved for the turbomachinery. The details of the recuperators and pre- cooler layouts are described in Chapter 10. Figure 9.4 shows the current operating experience with HEATRIC heat exchangers. Our intended application is well within the current operating limits. The maximum pressure required for the current reference design of the supercritical CO2 recompression cycle is 20 MPa. The recuperators operate with a maximum temperature on the order of 430oC. HEATRIC has supplied CO2 coolers for STATOIL operating at ~ 200oC. One 8 MW unit operated at 9 MPa, one 5 MW unit operated at 2.6 MPa and one 6 MW unit operated at 1.4 MPa. All the units perform well without any corrosion problems. Therefore, there is a successful operating experience with supercritical CO2 in HEATRIC heat exchangers. Figure 9.4 Current operating experience of HEATRIC PCHEs [from Dewson and Grady, 2003] 9.2.2 Effect of Conduction Length on the Heat Exchanger Volume An important issue is the heat conduction through the metal between the channels. Since the heat exchanger basic node is neither tube nor plate the conduction has to be 209PDF Image | Advanced Nuclear Power Technology Program A Supercritical Carbon Dioxide Cycle for Next Generation Nuclear Reactors
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