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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A few simplifying assumptions were made: 1. The total mass flow rate is uniformly distributed among the channels. 2. The temperature distribution in the heat exchanger is periodic with the period of two plates (one hot and one cold). 3. Hot and cold side channel and plate geometry is the same. 4. The wall channel temperature is uniform along channel periphery at every axial location. 5. The heat conduction area is assumed to be equal to the heat transfer area in the channel. 6. The heat conduction length is equal to the distance between the hot and cold channel (t in Figure 3.2). Based on the assumption 1, 2 and 3 it is sufficient to model a single channel on the hot side and a single channel on the cold sides because all the other hot and cold channels are identical with those that are modeled. Since the hot and cold side geometry is the same there is the same number of channels on the hot and cold sides. Therefore, the total heat exchanger performance can be calculated based on the performance of one hot and one cold channel by simply multiplying by the number of channels in the heat exchanger. i-1 i i+1 Hot side in Hot side out Heat Exchanger Hot End Heat Exchanger Cold End Cold side out 1 2 3 ...... j-1 j j+1 ...... N Figure 3.3 Heat exchanger nodalization Cold side in Node j Hot End 54 Node j Cold End

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