Method for promoting purity of chlorine hydride recycled by reduction unit of polysilicon tail gas separating system
A separation system, hydrogen chloride technology, applied in separation methods, chlorine/hydrogen chloride, chemical instruments and methods, etc., can solve the problems of waste, environmental pollution, low purity of recovered hydrogen chloride, etc., and achieve the effect of improving the purity
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Embodiment 1
[0024] A method for improving the purity of hydrogen chloride recovered from a reduction unit of a polysilicon tail gas separation system, comprising the following steps:
[0025] (1) The hydrogen chloride gas from the reduction unit of the polysilicon tail gas dry separation system first enters the separator 1 of the hydrogenation unit of the separation system, and mixes with the gas (hydrogen chloride and hydrogen) of the hydrogenation unit itself of the polysilicon tail gas dry separation system. The gas includes hydrogen, hydrogen chloride, dichlorodihydrosilane, trichlorosilane, and silicon tetrachloride. The mixed gas is heat-exchanged through the gas-gas heat exchanger 2, and the mixed gas is exchanged through the first gas-gas heat exchanger 2. The temperature is -4°C and the pressure is 0.45MpaG. The mixed gas after heat exchange is pressurized by the compressor 3 to increase the pressure of the mixed gas. After the mixed gas is compressed to a temperature of 40°C and ...
Embodiment 2
[0029] A method for improving the purity of hydrogen chloride recovered from a reduction unit of a polysilicon tail gas separation system, comprising the following steps:
[0030] (1) The hydrogen chloride gas from the reduction unit of the polysilicon tail gas dry separation system first enters the separator 1 of the hydrogenation unit of the separation system, and mixes with the gas (hydrogen chloride and hydrogen) of the hydrogenation unit itself of the polysilicon tail gas dry separation system. The gas includes hydrogen, hydrogen chloride, dichlorodihydrosilane, trichlorosilane, and silicon tetrachloride. The mixed gas is heat-exchanged through the gas-gas heat exchanger 2, and the mixed gas is exchanged through the first gas-gas heat exchanger 2. The temperature is 10°C and the pressure is 0.45MpaG. After the heat exchange, the mixed gas is pressurized by compressor 3 to increase the pressure of the mixed gas. After the mixed gas is compressed to a temperature of 40°C and...
Embodiment 3
[0034] A method for improving the purity of hydrogen chloride recovered from a reduction unit of a polysilicon tail gas separation system, comprising the following steps:
[0035] (1) The hydrogen chloride gas from the reduction unit of the polysilicon tail gas dry separation system first enters the separator 1 of the hydrogenation unit of the separation system, and mixes with the gas (hydrogen chloride and hydrogen) of the hydrogenation unit itself of the polysilicon tail gas dry separation system. The gas includes hydrogen, hydrogen chloride, dichlorodihydrosilane, trichlorosilane, and silicon tetrachloride. The mixed gas is heat-exchanged through the gas-gas heat exchanger 2, and the mixed gas is exchanged through the first gas-gas heat exchanger 2. The temperature is 5°C and the pressure is 0.45MpaG. After the heat exchange, the mixed gas is pressurized by the compressor 3 to increase the pressure of the mixed gas. After the mixed gas is compressed to a temperature of 40°C an...
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