Process for producing precipitated white carbon black by silicon tetrachloride
A technology for precipitating white carbon black and silicon tetrachloride, applied in the direction of silicon oxide, silicon dioxide, etc., can solve the problems of ineffective treatment, waste of environment, high cost, simple production equipment and process control, and small investment scale , the effect of reducing processing costs
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Embodiment 1
[0015] Add 60L of hydrochloric acid solution with a mass concentration of 29% in the reaction kettle, add 3.6g of sodium dodecylbenzenesulfonate dispersant, stir well, and heat through steam in the jacket, and the temperature is controlled at 40°C. Slowly add silicon tetrachloride into the reaction kettle, and control the flow rate of silicon tetrachloride at 0.8m 3 / h, adjust the amount of cooling water at any time during the addition process, and control the temperature in the kettle at 41-45°C. After the hydrogen chloride gas produced in the reaction is treated by filtration, adsorption, separation and other devices, the qualified hydrogen chloride is sent to the PVC or trichlorosilane production device for use, and the unqualified hydrogen chloride is absorbed by water and then replenished to the mother liquid storage tank; continuous sampling during the reaction process Analyze the purity of hydrogen chloride, when the hydrogen chloride purity ≥ 95%, it can all be recover...
Embodiment 2
[0017] Add 60L of hydrochloric acid solution with a mass concentration of 31% in the reaction kettle, add 4.8g of hexadecyltrimethylammonium bromide dispersant, stir well, pass steam into the jacket for heating, and control the temperature at 38°C . Slowly add silicon tetrachloride into the reactor, and control the flow rate of silicon tetrachloride at 1.0m 3 / h, adjust the amount of cooling water at any time during the addition process, and control the temperature in the kettle at 36-40°C. After the hydrogen chloride gas produced in the reaction is treated by filtration, adsorption, separation and other devices, the qualified hydrogen chloride is sent to the PVC or trichlorosilane production device for use, and the unqualified hydrogen chloride is absorbed by water and then replenished to the mother liquid storage tank; continuous sampling during the reaction process Analyze the purity of hydrogen chloride, when the hydrogen chloride purity ≥ 95%, it can all be recovered, an...
Embodiment 3
[0019] Add 60L of hydrochloric acid solution with a mass concentration of 33% in the reaction kettle, add 7.2g of cetyltrimethylammonium bromide dispersant, stir well, pass steam into the jacket for heating, and control the temperature at 32°C . Slowly add silicon tetrachloride into the reactor, control the flow of silicon tetrachloride at 1.2m 3 / h, adjust the amount of cooling water at any time during the addition process, and control the temperature in the kettle at 28-34°C. After the hydrogen chloride gas produced in the reaction is treated by filtration, adsorption, separation and other devices, the qualified hydrogen chloride is sent to the PVC or trichlorosilane production device for use, and the unqualified hydrogen chloride is absorbed by water and then replenished to the mother liquid storage tank; continuous sampling during the reaction process Analyze the purity of hydrogen chloride, when the hydrogen chloride purity ≥ 95%, it can all be recovered, and when the hy...
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