Method for producing cyanoethylalkoxysilane by atmospheric distillation reaction
A technology of cyanoethylalkoxysilane and cyanoethyltrichlorosilane is applied in the field of producing cyanoethylalkoxysilane, and can solve the problems of inability to continuously produce for a long time, excessive use of entrainers, low production capacity and the like, Achieve the effect of large production capacity, reduced energy consumption and low acid value
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specific Embodiment approach 1
[0017] Specific embodiment one: the device for producing cyanoethyl alkoxysilane by atmospheric distillation reaction in this embodiment, the device includes a tower kettle 1, a packed tower 2, a first storage tank 3, a second storage tank 4 and a first replacement tank Heater 5, described tower reactor 1 and packed tower 2 form tower reactor 6, the first heat exchanger 5 links to each other with tower reactor 1 and packed tower 2 respectively, and first storage tank 3 and second storage tank 4 are respectively connected with The packed towers 2 are connected, the first pump 7, the first flow meter 8 and the second heat exchanger 9 are arranged between the first storage tank 3 and the packed tower 2, and the second storage tank 4 and the packed tower 2 are arranged Two pumps 10, a second flowmeter 11 and a third heat exchanger 12, the top of the packed tower 2 is provided with a tail gas pipe 14, the tail gas pipe 14 is provided with a fourth heat exchanger 13, the tail gas pip...
specific Embodiment approach 2
[0018] Specific embodiment two: the method for the production of cyanoethylalkoxysilane by atmospheric distillation reaction in this embodiment is carried out according to the following steps:
[0019] 1. First, lay the bottom of cyanoethyl alkoxysilane on the bottom of tower reactor 6 and tank 1, and pass the entrainer into tower reactor 6 until the temperature of tower tank 1 is 220°C-240°C, of which cyanoethyl alkoxysilane The mass ratio of base alkoxysilane to entrainer is 10-20:1;
[0020] Two, from the bottom of the tower reactor 6 to the tower reactor 1 of the tower reactor 6, the monohydric aliphatic alcohol is continuously passed into the tower reactor 6 at a rate of 128g / h-256g / h, from the top of the tower reactor 6 to the tower reactor 6 Continuously feed cyanoethyltrichlorosilane at a rate of 175g / h-350g / h, and react under the condition that the temperature in the atmospheric column tank 1 is 100-120°C, and during the reaction, use 5g / h- Supplement entrainer at ...
specific Embodiment approach 3
[0022] Embodiment 3: The difference between this embodiment and Embodiment 2 is that the entrainer described in step 1 and step 2 is toluene, acetonitrile, n-hexane or cyclohexane. Others are the same as in the second embodiment.
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