Multi-connected unit phase change energy storage hot liquid defrosting system
A technology of phase change energy storage and hydrothermal defrosting, which is applied in energy recovery systems for ventilation and heating, air conditioning systems, ventilation systems, etc. Slow down and other problems, to improve reliability, speed up defrosting speed, prolong life
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specific Embodiment approach 1
[0009] Specific implementation mode one: combine figure 1 Describe this embodiment. The system of this embodiment includes a compressor unit 1, an oil separator 2, a four-way reversing valve 3, a liquid receiver 6, a subcooler 7, an outdoor electronic expansion valve 9, an outdoor heat exchanger 10, The gas-liquid separator 11 and the indoor unit 26, the outlet end of the compressor unit 1 communicates with the inlet end of the oil separator 2, and the outlet end of the oil separator 2 communicates with one of the through holes of the four-way reversing valve 3, the system It also includes a phase change heat accumulator 8, a first solenoid valve 12, a second solenoid valve 13, a third solenoid valve 14, a fourth solenoid valve 15, a fifth solenoid valve 16, a sixth solenoid valve 24, and a seventh solenoid valve 17 , the first main road 18, the first branch pipeline 19, the second branch pipeline 20, the second main road 21, the third main road 22 and the fourth main road 23,...
specific Embodiment approach 2
[0014] Specific implementation mode two: combination figure 1 To illustrate this embodiment, the phase change material in the phase change heat accumulator 8 of this embodiment is CaCl 2 ·6H 2 O or Na 2 SHO 4 10H 2 O, because this system requires the temperature range of the phase change material in the phase change heat accumulator 8 to be 20-35 degrees Celsius, the latent heat of phase change per unit volume should not be less than 250KJ / L, and the thermal conductivity should not be less than 0.5W / mK, so the above-mentioned Inorganic phase change material, mixed with a small amount of additives to prevent supercooling and phase separation. to CaCl 2 ·6H 2 O can add BaCO with a mass fraction of about 2% 3 and 2% SrCl 2 ; to Na 2 SHO 4 10H 2 O can add mass fraction about 2% borax 2% superabsorbent resin. Phase-change temperature heat accumulator structure: The heat accumulator should not adopt the spiral tube and casing type structure, because the resistance is lar...
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