Preparation method of hexamethyldisiloxane
A technology of hexamethyldisiloxane and trimethylchlorosilane, which is applied in the field of preparation of hexamethyldisiloxane, can solve the problems of waste of chlorine, low concentration of hydrochloric acid, and high energy consumption of hydrogen chloride
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[0033] The invention provides a kind of preparation method of hexamethyldisiloxane, comprising the following steps:
[0034] A) Concentrated hydrochloric acid and trimethylchlorosilane are sequentially transported to a hydrolysis reactor to perform a hydrolysis reaction to obtain a hydrolyzate;
[0035] The pressure of the hydrolysis reaction is 0.05~0.2MPa;
[0036] B) The obtained hydrolyzate is transported to the heat exchanger for heating, then enters the gas-liquid separation tower, hydrogen chloride gas is separated from the hydrolyzate, enters the condenser, collects hydrogen chloride gas from the top of the condenser, and obtains hydrochloric acid from the bottom of the condenser Mixtures with hexamethyldisiloxane;
[0037] The mixture of hexamethyldisiloxane and concentrated hydrochloric acid is obtained at the bottom of the gas-liquid separation tower;
[0038] C) The mixture of hexamethyldisiloxane and concentrated hydrochloric acid obtained from the bottom of the...
Embodiment 1
[0068] Example 1 Production of hexamethyldisiloxane by continuous process.
[0069] 1) 108 parts of trimethylchlorosilane with a content of 99% are continuously transported to a mixer hydrolyzer with 36.5% concentrated hydrochloric acid at a pressure of 0.1 MPa with a canned pump, and hydrolyzed with water in hydrochloric acid to obtain Hexa A mixture of base disiloxane, concentrated hydrochloric acid, and hydrogen chloride gas produced by hydrolysis.
[0070] 2) The mixed material enters the heat exchanger through its own pressure and is heated to 50 degrees to enter the gas-liquid separation tower. 37 parts of hydrogen chloride gas are separated from the mixture, and 35 parts of hydrogen chloride gas are collected after entering the condenser for condensation and purification.
[0071] 3) 121 parts of hexamethyldisiloxane and concentrated hydrochloric acid mixture were obtained at the bottom of the gas-liquid separation tower, and mixed with 2 parts of recovered liquid in st...
Embodiment 2
[0076] Example 2 Batch production of hexamethyldisiloxane.
[0077] 1) 108 parts of trimethylchlorosilane with a content of 99% are continuously transported by a canned pump to a mixer containing 50 parts of 36.5% concentrated hydrochloric acid, and hydrolyzed with water in hydrochloric acid to obtain hexamethyldisiloxane The mixture of alkane, concentrated hydrochloric acid, and hydrogen chloride gas produced by hydrolysis is 158 parts, and the pressure of the mixer is continuously increased, finally reaching 0.12MPa.
[0078] 2) After feeding the trimethylchlorosilane, close the feeding valve and stop the delivery pump. The mixed material enters the heat exchanger to be heated to 50 degrees through its own pressure, and then enters the gas-liquid separation tower. 37 parts of hydrogen chloride gas are separated and desorbed from the mixture, and enter the condenser from the top of the tower. After condensation and purification, 35 parts of hydrogen chloride gas are collected...
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