A kind of method that utilizes organosilicon azeotrope to produce ethyl orthosilicate
A technology of tetraethyl orthosilicate and azeotrope, which is applied in the field of reuse of by-products in the synthesis and production of organic silicon monomers in the chemical industry, to achieve the effects of sufficient supply, stable process and high yield
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Embodiment 1
[0045] (1) By-product azeotrope [(CH 3 ) 3 SiCl: 51.27wt%, SiCl 4 : 40.23wt%, CH 3 SiHCl 2 : 5.67wt%, HSiCl 3 : 1.12wt%, (CH 3 ) 2 SiHCl: 1.54wt%] was added to a still-type device with a packed tower for heating and distillation. Control the temperature at the bottom of the tower to 70-80°C, and the temperature at the top of the tower to about 40°C, and sequentially separate light components such as methylhydrogendichlorosilane, trichlorosilane, and dimethylhydrogenchlorosilane with a boiling point lower than 40°C. Obtain the intermediate mixture of silicon tetrachloride and trimethylchlorosilane in the kettle;
[0046] (2) Put the intermediate mixture obtained in step (1) into the esterification reaction kettle. At 25°C, first drop 1 / 3 of the ethanol used in this step into the intermediate mixture at 200L / h. Reflux reaction at 40°C for 2 hours, and then at 40°C, drop 2 / 3 of the ethanol used in this step into the partial esterification reaction solution at 300L / h, and ...
Embodiment 2
[0051] (1) By-product azeotrope [(CH 3 ) 3 SiCl: 50.12wt%, SiCl 4 : 40.77wt%, CH 3 SiHCl 2 : 6.37wt%, HSiCl 3 : 1.31wt%, (CH 3 ) 2 SiHCl: 1.43wt%] was added to a still-type device with a packed tower for heating and distillation. Control the temperature of the tower kettle at 70-80°C, and the temperature at the top of the tower at about 40°C, and sequentially separate light components such as methyldichlorosilane, trichlorosilane, and dimethylhydrochlorosilane with boiling points lower than 40°C. Obtain the intermediate mixture of silicon tetrachloride and trimethylchlorosilane in;
[0052] (2) Put the intermediate mixture obtained in step (1) into the esterification reaction kettle. At 30°C, first drop 1 / 2 of the ethanol used in this step into the intermediate mixture at 250L / h. Reflux reaction at 45°C for 1 hour, and then at 45°C, drop 1 / 2 of the ethanol used in this step into the partial esterification reaction solution at 350L / h, and raise the temperature to 50°C f...
Embodiment 3
[0057] (1) By-product azeotrope [(CH 3 ) 3 SiCl: 53.41wt%, SiCl 4 : 38.59wt%, CH 3 SiHCl 2 : 5.37wt%, HSiCl 3 : 1.31wt%, (CH 3 ) 2 SiHCl: 1.16wt%] was added to a still-type device with a packed tower for heating and distillation. Control the temperature of the tower kettle at 70-80°C, and the temperature at the top of the tower at about 40°C, and sequentially separate light components such as methyldichlorosilane, trichlorosilane, and dimethylhydrochlorosilane with boiling points lower than 40°C. Obtain the intermediate mixture of silicon tetrachloride and trimethylchlorosilane in;
[0058] (2) Put the intermediate mixture obtained in step (1) into the esterification reaction kettle. At 25°C, first drop 1 / 2 of the ethanol used in this step into the intermediate mixture at 250L / h. Reflux reaction at 40°C for 2 hours, and then at 40°C, drop 1 / 2 of the ethanol used in this step into the partial esterification reaction solution at 300L / h, and then raise the temperature to ...
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