Method for preparing silicon dioxide and hydrogen chloride by means of hydrolysis of polysilicon by-product silicon tetrachloride
A technology of silicon tetrachloride and silicon dioxide, which is used in the preparation of chloride, silicon dioxide, chlorine/hydrogen chloride, etc., can solve the problems of complex process, achieve simple process, simplify process, and facilitate production and implementation. Effect
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Embodiment 1
[0027] Add 80L mass concentration of 20% hydrochloric acid solution in the closed reaction kettle, add 10kg additive magnesium chloride, 3kg surfactant sodium dodecylbenzenesulfonate, stir thoroughly and then feed steam in the jacket for heating, control The reaction temperature was 35°C. Slowly add silicon tetrachloride into the reactor, control the flow rate of silicon tetrachloride at 0.6m 3 / h, during the addition process, the temperature of the reaction liquid in the kettle is controlled to be 35-42°C by adjusting the amount of circulating cooling water. The hydrogen chloride gas produced in the reaction is sent to the trichlorosilane production unit after filtering, dust removal and drying. After the silicon tetrachloride reaction is completed, the feed liquid is aged for 1 hour and then discharged to the filter equipment for separation and washing. The mother liquor water is sent to the mother liquor storage tank, and the washing water is sent to the lean liquor storag...
Embodiment 2
[0029] Add 50L mass concentration of 28% hydrochloric acid solution in the airtight reaction kettle, add 8kg of additives magnesium chloride and ammonium chloride mixture, wherein magnesium chloride and ammonium chloride each account for 4kg, 2kg surfactant OP-10, stir well and then add Steam was passed into the jacket for heating, and the reaction temperature was controlled at 45°C. Slowly add silicon tetrachloride into the reactor, control the flow of silicon tetrachloride at 0.5m 3 / h, during the addition process, the temperature of the reaction liquid in the kettle is controlled to be 45-50°C by adjusting the amount of circulating cooling water. The hydrogen chloride gas produced in the reaction is sent to the trichlorosilane production unit after filtering, dust removal and drying. After the silicon tetrachloride reaction is completed, the feed liquid is aged for 1 hour and then discharged to the filter equipment for separation and washing. The mother liquor water is sen...
Embodiment 3
[0031] Add 60L of hydrochloric acid solution with a mass concentration of 18% in a closed reaction kettle, add 4kg of additive ammonium chloride, 6kg of calcium chloride; Steam was passed into the medium for heating, and the reaction temperature was controlled at 25°C. Slowly add silicon tetrachloride into the reactor, control the flow rate of silicon tetrachloride at 0.6m 3 / h, during the addition process, the temperature of the reaction liquid in the kettle is controlled to be 25-32°C by adjusting the amount of circulating cooling water. The hydrogen chloride gas produced in the reaction is sent to the trichlorosilane production unit after filtering, dust removal and drying. After the silicon tetrachloride reaction is completed, the feed liquid is aged for 1 hour and then discharged to the filter equipment for separation and washing. The mother liquor water is sent to the mother liquor storage tank, and the washing water is sent to the lean liquor storage tank as mother liq...
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