“…The method of finite time thermodynamic analysis has been also applied to the performance studies of simple endoreversible [10][11][12] and irreversible [13][14][15][16][17] Brayton refrigeration cycles, as well as regenerated endoreversible [18] and irreversible [19][20][21] Brayton refrigeration cycles. For a fixed total heat-exchanger inventory of heat exchangers (i.e., the sum of heat conductances of the all heat exchangers) in the refrigeration cycle, the optimum performance of the cycle can be obtained by optimizing the distribution of the heat exchanger inventory between the hot-and cold-side heat-exchangers [10,[20][21][22][23][24][25]. Wu et al [10] studied the optimum allocation of heat-exchanger inventory, the optimum thermalNomenclature C thermal-capacity rate, kW/K c thermal-capacity rate matching, dimensionless E 1 effectiveness of heat exchanger, dimensionless k ratio of principal specific heats, dimensionless m (k À 1)/k, dimensionless N 1 number of heat-transfer units, dimensionless Q rate of heat transfer, kW R cooling load, kW T temperature, K U heat conductance, kW/K u distribution of heat conductances, dimensionless x isentropic temperature ratio of working fluid, dimensionless…”