Combined method for synthesizing methyl chlorosilane
A technology of methyl chlorosilane and combined method, which is applied in the field of comprehensive utilization of by-products, can solve the problems of expensive catalysts, difficult regeneration and recycling of catalysts, etc., and achieve improved bed mass transfer and heat transfer, reduced impact, and high reactivity Effect
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Embodiment 1
[0025] The charging coefficient of aluminum powder in the stirred bed reactor is 0.5, the stirred bed reaction temperature is 280°C, the stirring speed is 80r / min, the stirred bed reaction pressure is 0.3MPa, the fixed bed reactor temperature is 300°C, the fixed bed reaction pressure 0.4MPa, control the mass ratio of methyl chloride and high boilers to be 2:1, collect the liquid phase product in the condenser after reacting for 4h, adopt gas chromatography internal standard method in combination with distillation to analyze its composition; wherein CH 3 SiHCl 2 3.67%, CH 3 SiCl 3 13.83%, (CH 3 ) 2 SiCl 2 is 23.91%, (CH 3 ) 3 SiCl is 28.24%, (CH 3 ) 4 Si is 0.89%; the high boiler conversion rate is 72.6% in the whole reaction process, CH3 The Cl conversion was 79.7%.
Embodiment 2
[0027] The charging coefficient of aluminum powder in the stirred bed reactor is 0.8, the stirred bed reaction temperature is 320°C, the stirring speed is 180r / min, the stirred bed reaction pressure is 0.8MPa, the fixed bed reactor temperature is 350°C, the fixed bed reaction pressure It is 1.0MPa, and the mass ratio of methyl chloride and high boiler is controlled to be 9:1, and the liquid phase product in the condenser is collected after 4 hours of reaction, and its composition is analyzed by gas chromatography internal standard method in conjunction with distillation; wherein CH 3 SiHCl 2 1.32%, CH 3 SiCl 3 7.73%, (CH 3 ) 2 SiCl 2 is 34.81%, (CH 3 ) 3 SiCl is 38.14%, (CH 3 ) 4 Si is 1.77%; the high boiler conversion rate is 84.3% in the whole reaction process, CH 3 The Cl conversion was 52.8%.
Embodiment 3
[0029] The charging coefficient of aluminum powder in the stirred bed reactor is 0.5, the stirred bed reaction temperature is 300°C, the stirring speed is 90r / min, the stirred bed reaction pressure is 0.5MPa, the fixed bed reactor temperature is 300°C, the fixed bed reaction pressure It is 0.4MPa, the mass ratio of control methyl chloride and low boiler is 2: 1, after reacting for 4h, collect the liquid phase product in the condenser and adopt gas chromatography internal standard method to analyze its composition; wherein CH 3 SiHCl 2 19.75%, CH 3 SiCl 3 7.63%, (CH 3 ) 2 SiCl 2 is 32.56%, (CH 3 ) 3 SiCl is 27.24%, (CH 3 ) 4 Si is 1.19%; the low boiler conversion rate is 88.1% in the whole reaction process, CH 3 The Cl conversion was 71.5%.
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