Cooling capacity cyclic utilization process for producing thionyl chloride
A thionyl chloride, cooling technology, applied in cooling fluid circulation devices, applications, thionyl chloride and other directions, can solve problems such as insufficient heat exchange, increased compressor load, and inability to condense exhaust gas, avoiding a large amount of evaporation, Reduce the operating load and ensure the effect of good operation
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Embodiment 1
[0025] Main parameter settings:
[0026] The liquid level of the cold liquid storage tank 1 is 100mm, and the pressure of the cold liquid storage tank 1 is 0.3Mpa;
[0027] The outlet temperature of heat exchanger 3 is 0°C, and the outlet pressure is ≤0.4Mpa;
[0028] The temperature of vaporizer 4 is 90°C, and the pressure is ≤0.4Mpa.
[0029] The refrigeration cycle utilization process of producing thionyl chloride of the present invention, the steps are as follows:
[0030] The cold liquid after being cryogenically cooled by the cold liquid storage tank 1 enters the heat exchanger 3, and the circulating pump pumps the water in the circulating pool 5 into the heat exchanger 3, and the cold liquid and the circulating water exchange heat in the heat exchanger 3, The cold liquid after heat exchange is vaporized by the vaporizer 4 and then enters the production system, and the circulating water after heat exchange enters the refrigerator 2 to reduce the return temperature of t...
Embodiment 2
[0032] Main parameter settings:
[0033] The liquid level of the cold liquid storage tank 1 is 700mm, and the pressure of the cold liquid storage tank 1 is 0.2Mpa;
[0034] The outlet temperature of heat exchanger 3 is 10°C, and the outlet pressure is ≤0.4Mpa;
[0035] The temperature of vaporizer 4 is 97°C, and the pressure is ≤0.4Mpa.
[0036] The refrigeration cycle utilization process of producing thionyl chloride of the present invention, the steps are as follows:
[0037] The cold liquid after being cryogenically cooled by the cold liquid storage tank 1 enters the heat exchanger 3, and the circulating pump pumps the water in the circulating pool 5 into the heat exchanger 3, and the cold liquid and the circulating water exchange heat in the heat exchanger 3, The cold liquid after heat exchange is vaporized by the vaporizer 4 and then enters the production system, and the circulating water after heat exchange enters the refrigerator 2 to reduce the return temperature of ...
Embodiment 3
[0039] Main parameter settings:
[0040] The liquid level of the cold liquid storage tank 1 is 1000mm, and the pressure of the cold liquid storage tank 1 is 0.2Mpa;
[0041] The outlet temperature of heat exchanger 3 is 20°C, and the outlet pressure is ≤0.4Mpa;
[0042] The vaporizer 4 has a temperature of 100°C and a pressure of ≤0.4Mpa.
[0043] The refrigeration cycle utilization process of producing thionyl chloride of the present invention, the steps are as follows:
[0044] The cold liquid after being cryogenically cooled by the cold liquid storage tank 1 enters the heat exchanger 3, and the circulating pump pumps the water in the circulating pool 5 into the heat exchanger 3, and the cold liquid and the circulating water exchange heat in the heat exchanger 3, The cold liquid after heat exchange is vaporized by the vaporizer 4 and then enters the production system, and the circulating water after heat exchange enters the refrigerator 2 to reduce the return temperature o...
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