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Figure 4.4: The division of the tube length according to heat transfer regime in SoSaT . The shell-and-tube steam generator model assumes that sodium will flow in a uniform manner downward through a cylindrical shell. There is no option for baffles in the current steam generator model. Upward flow of water is contained in a hexagonally pitched bank of smooth surfaced tubes. The tubes are assumed to be double wall tubes and can be constructed of several materials. These are 9Cr-1Mo steel, 304 SS, and 316 SS. The code begins by calculating what the sodium outlet temperature must be, assuming that all of the designated power is transferred as heat to the water. Based on the sodium inlet conditions, the heat transferred is given by π = πππ ππ ππ£π βπ Eqn. 4-30 By assuming that the specific heat capacity of sodium does not change appreciably with temperature, the outlet temperature is calculated from Eqn. 4-30, using the userβs input of total heat to be transferred. The specific heat of sodium at each temperature is calculated based on known fluid properties from an Argonne National Laboratory study [Fink and Leibowitz, 1995] 96PDF Image | Supercritical Carbon Dioxide Cycle Analysis
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