Method for preparing alkoxy silane from organic silicon by-product
A technology of alkoxysilane and silicon by-products, applied in the field of utilization of organic silicon by-products, can solve the problems of single, high processing cost, and ineffective utilization, and achieve low energy consumption, high purity, high economic and social benefits Effect
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Embodiment 1
[0037] Preparation of filler loaded with dehydrogenation catalyst: Add 300kg of methanol and 40kg of water into a 1000L hydrolysis kettle, keep the temperature in the kettle at 50°C, add 300kg of methyltrimethoxysilane dropwise, after the dropwise addition, keep the temperature in the kettle at 50°C and continue Stir the reaction for 8 hours to obtain an alkoxysilane hydrolyzate; add 30kg of nickel chloride to the hydrolyzate, stir evenly, then put the alkoxysilane hydrolyzate into the dipping tank, and put the porous ceramic filler into the Immerse it completely in the immersion tank for 16 hours, then take out the filler, put it into a dryer and dry it at 100°C for 4 hours, and then obtain the filler loaded with dehydrogenation catalyst.
[0038] Preparation of methyltrimethoxysilane: methyl dichlorosilane enters the reaction tower at a flow rate of 300k / kg, methanol enters the reaction tower after being vaporized, and the flow rate is 300k / kg; keep the temperature of the kettl...
Embodiment 2
[0042] Preparation of filler loaded with dehydrogenation catalyst: Add 300kg of methanol and 40kg of water into a 1000L hydrolysis kettle, keep the temperature in the kettle at 50°C, add 300kg of methyltrimethoxysilane dropwise, after the dropwise addition, keep the temperature in the kettle at 50°C and continue Stir the reaction for 8 hours to obtain an alkoxysilane hydrolyzate; add 30kg of nickel chloride to the hydrolyzate, stir evenly, then put the alkoxysilane hydrolyzate into the dipping tank, and put the porous ceramic filler into the Immerse it completely in the immersion tank for 16 hours, then take out the filler, put it into a dryer and dry it at 100°C for 4 hours, and then obtain the filler loaded with dehydrogenation catalyst.
[0043] Preparation of methyltrimethoxysilane: a mixture of 30% methyldichlorosilane and 70% methyltrichlorosilane enters the reaction tower at a flow rate of 300k / kg, and methanol enters the reaction tower after being vaporized with a flow ...
Embodiment 3
[0047] Preparation of filler loaded with dehydrogenation catalyst: Add 300kg of methanol and 40kg of water into a 1000L hydrolysis kettle, keep the temperature in the kettle at 50°C, add 300kg of methyltrimethoxysilane dropwise, after the dropwise addition, keep the temperature in the kettle at 50°C and continue Stir the reaction for 8 hours to obtain an alkoxysilane hydrolyzate; add 30kg of nickel nitrate to the hydrolyzate, stir evenly, then put the alkoxysilane hydrolyzate into the immersion tank, and put the porous ceramic filler into the immersion Immerse it completely in the tank for 16 hours, then take out the filler, put it in a dryer and dry it at 100°C for 4 hours, and then get the filler loaded with dehydrogenation catalyst.
[0048] Preparation of tetraethoxysilane: a mixture of 40% trichlorosilane and 60% silicon tetrachloride enters the reaction tower at a flow rate of 300k / kg, and the ethanol enters the reaction tower after being vaporized with a flow rate of 460...
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