Hot water supply system and method thereof
A technology of supply system and hot water, applied in residential hot water supply system, heating method, household heating and other directions, can solve the problems of primary energy efficiency restriction of power generation efficiency, reduced energy efficiency, rectification and other problems at the user end of the primary energy efficiency grid. Conducive to rational utilization, improved energy utilization efficiency, and the effect of improving energy efficiency
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example 1
[0076] Using commercial electricity as power, adopt the method of Example 8 to provide hot water, the flow rate ratio of the heat source water and the heated water, that is, the flow rate ratio of the tap water flowing through the evaporator and the condenser respectively is 15. The temperature of the water source water (tap water supplied by the municipality) is 15°C, the temperature of the hot water supplied is 50°C, the evaporation temperature of the refrigerant in the evaporator of the vapor compression heat pump circulation subsystem is 8.2°C, and the outlet temperature of the heat source water is 13.2°C, The condensing temperature of the refrigerant in the condenser is 55°C, the adiabatic efficiency of the compressor is 0.85, the COP of the vapor compression heat pump cycle subsystem in this embodiment is 4.85, and the primary energy efficiency of the overall system is 160%.
example 2
[0078] Adopt the method of embodiment 10 to provide hot water, the flow rate ratio of heat source water and heated water is 15. The evaporator is filled with paraffin wax with a carbon number of 15, and its freezing point and freezing heat are about 10°C and 170kJ / kg respectively. The temperature of the source water (tap water supplied by the municipality) is 15°C, the temperature of the hot water supplied is 50°C, the evaporation temperature of the refrigerant in the evaporator of the heat pump circulation subsystem is 8.4°C, and the outlet temperature of the heat source water is 13.4°C. The condensing temperature of the refrigerant is 49.3°C, and the adiabatic efficiency of the compressor is 0.85. The proton exchange membrane fuel cell power generation sub-system uses natural gas as raw material, its power generation efficiency is 37%, and the heat recovery efficiency is 40%. The COP of the vapor compression heat pump cycle subsystem in this embodiment is 5.60, and the prim...
example 3
[0080] The method in Example 10 is used to provide hot water, and the flow rate ratio of the heat source water to the heated water is 5. The evaporator is filled with paraffin wax with a carbon number of 15, and its freezing point and freezing heat are about 10°C and 170kJ / kg respectively. The temperature of the source water (tap water supplied by the municipality) is 15°C, the temperature of the hot water supplied is 50°C, the evaporation temperature of the refrigerant in the evaporator of the heat pump circulation subsystem is 5.3°C, and the outlet temperature of the heat source water is 10.3°C. The condensing temperature of the refrigerant is 49.0°C, and the adiabatic efficiency of the compressor is 0.85. The proton exchange membrane fuel cell power generation sub-system uses natural gas as raw material, its power generation efficiency is 37%, and the heat recovery efficiency is 40%. The COP of the vapor compression heat pump cycle subsystem in this embodiment is 5.22, and...
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