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The lower condensing temperature Tg increases the capacity of the evaporator. Thus, refrigerant mass flow rate mR can be reduced to maintain the same suction pressure and heating load. The lower discharge pressure at the compressor de creases the power requirement for the compressor. Thus, a substantial portion of the condenser performance is reflected in the improved (COP)s of the refrigera tion system. Comparative performance of the refrigeration system for chlorine storage with each of four condenser types is shown in Table 2. Power consumption of components is listed for each system. Coefficient of performance for each sys tem is defined as: where (COP) s Qe = heat of evaporation; EP = Total power consumption for the system.* R-12 RESERVOIR \ THROTTLE VALVE PUMP From OH Storage EVAPORATIVE CONDENSER I T ype 2 ) Figure 17. Refrigeration system for chlorine storage with Type 2 evaporative condenser (Design conditions remain the same as in Figure 16). B-20PDF Image | Development of the Zinc-Chlorine Battery for Utility
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