Preparation method of dimethyl dimethoxy triacetoxy
A technology of dimethyldimethoxysilane and dimethyldichlorosilane, which is applied in the field of compound preparation, can solve the problems of difficult operation, long process flow, heavy pollution, etc., and achieves reduction of operating cost and change of process flow. The effect of shortening and reducing production costs
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Embodiment 1 2
[0025] The preparation of embodiment 1 dimethyldimethoxysilane
[0026] ①Response: first at 1m 3 Put 500kg of dimethyldichlorosilane and 700kg of urea into the enamel stirred tank. Then 500 kg of methanol was added dropwise under stirring, and the addition was required to be completed within 2 hours. The reaction was carried out at -200 mm Hg, and the temperature was controlled at 58° C., and the temperature control was realized by dropping speed or using jacketed cold water to cool down. After the reaction, the stirring was stopped, and the layers were separated for 30 minutes, and the acidic liquid at the bottom was released. The upper crude product is introduced into the neutralization kettle.
[0027] ②Neutralization: Before neutralization, the content of dimethyl-methoxychlorosilane and hydrogen chloride in the crude product should be analyzed to determine the amount of neutralizing agent sodium methoxide added. The amount of sodium methoxide added requires an excess ...
Embodiment 2 2
[0036] The preparation of embodiment 2 dimethyldimethoxysilane
[0037] The steps in the preparation method are the same as in Example 1, except that the amount of raw materials is different, which are respectively: dimethyldichlorosilane 100kg, methanol 48kg; wherein the hydrogen chloride absorbent is a sufficient amount of ammonia; the reaction pressure is -1 mmHg , the temperature is 40°C. In addition, during the neutralization process, the neutralizer is magnesium powder.
Embodiment 3 2
[0038] The preparation of embodiment 3 dimethyldimethoxysilane
[0039] The steps in the preparation method are the same as in Example 1, except that the amount of raw materials is different, which are respectively: 800 kg of dimethyldichlorosilane and 320 kg of methanol; wherein the hydrogen chloride absorbent is a sufficient amount of aluminum; the reaction pressure is -100 mmHg , the temperature is 45°C. In addition, in the neutralization process, the neutralizing agent is sodium.
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