Supergravity thermal drive refrigeration device and method
A refrigeration device and supergravity technology, applied in the field of supergravity heat-driven refrigeration devices, can solve the problems of low efficiency, low efficiency, complex system, etc., and achieve the effect of high efficiency and few system links
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Embodiment 1
[0019] Embodiment 1, figure 1 A high-gravity heat-driven refrigeration device and method are provided.
[0020] The supergravity heat-driven refrigeration device includes a refrigeration device with working medium flow and a supergravity generating device; the supergravity generating mechanism is a base 1 arranged on a rotating shaft 2, and the rotation of the rotating shaft 2 drives the base 1 to rotate at a corresponding angular velocity. The refrigerating device is a closed-loop structure composed of a heater 6, an evaporator 3, a condenser 4, and a liquid pump 5 connected in sequence; the evaporation pipeline of the evaporator 3 and the connecting condenser 4 are connected to each other through a pipeline I; The heating pipeline and the evaporation pipeline of the evaporator 3 are connected to each other through pipeline IV. The condenser 4 and the liquid pump 5 are connected to each other through the pipeline II; the liquid pump 5 and the heating pipeline of the heater 6...
Embodiment 1
[0030] The calculation parameters for implementing Example 1 are shown in Table 1 (for 1kg of working fluid R134a). The design conditions are: the working fluid is R134a, the heater temperature is 60°C, the heater pressure is 1.678Mpa, the condensation temperature is 31.5°C, the evaporation temperature is 0°C, and the turning diameter is 1.6m. The system COP (defined as the ratio of the heat absorbed by the evaporator to the heating capacity of the heater) calculated in Example 1 is 0.66, the rotating speed at this moment is 2448 rpm, the heat absorbed by the evaporator is 105.5kJ / kg, the condenser The exhausted heat is 175.8kJ / kg, the dryness of the refrigerant at the outlet of the heater is 0.45, the dryness of the refrigerant at the inlet of the evaporator is 0.65, the transmitted inertial potential energy is 21kJ / kg, and the theoretical power consumption of the liquid pump is 0.739kJ / kg.
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