Method for removing moisture in hydrogen chloride gas
A hydrogen chloride gas, hydrogen chloride technology, applied in separation methods, chlorine/hydrogen chloride, chlorine/hydrogen chloride purification and other directions, can solve problems such as difficult removal, and achieve the effects of large energy consumption, high removal efficiency, and low treatment costs.
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Embodiment 1
[0012] A chemical plant has an annual output of 20,000 tons of trichlorosilane, and hydrogen chloride gas, the raw material for the synthesis of trichlorosilane, is produced by hydrochloric acid deep analysis process. The analyzed hydrogen chloride has a water content of 400-800ppm after cryogenic separation. Adopt the present invention to process: the hydrogen chloride containing 400-800ppm moisture after cryogenic separation is passed into the bubble-cap drying tower from the bottom of the bubble-cap drying tower, and the mass fraction of entering from the top of the bubble-cap drying tower through pump circulation is 99.9% Silicon tetrachloride is contacted in countercurrent, and the gas flowing out of the top of the tower is filtered by a metal sintered filter element filter to obtain hydrogen chloride gas with a moisture content of less than 6ppm, and the silicon tetrachloride liquid flowing out from the bottom of the tower is pumped to the bubble tower The top loop is us...
Embodiment 2
[0014] A chemical plant synthesizes trichlorosilane, and the hydrogen chloride gas used is the by-product hydrogen chloride gas produced by the potassium sulfate plant. Adopt the present invention to process: the hydrochloric acid by-product of producing potassium sulfate device removes impurity oxygen, nitrogen, carbon dioxide contained therein through pressure swing adsorption and contains water 1800ppm, it is passed into bubble cap drying tower bottom from bubble cap drying tower, mass The silicon tetrachloride liquid with a fraction of 99.9% is introduced from the top of the bubble-cap drying tower. In the tower, hydrogen chloride and silicon tetrachloride are in countercurrent contact. The hydrogen chloride gas that meets the requirements is less than 8ppm, and the silicon tetrachloride liquid flowing out from the bottom of the tower is pumped to the top of the bubble column for recycling through a circulation pump.
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