Dimethyl dichlorosilane hydrolysis method for directly producing gaseous hydrogen chloride
A dimethyldichlorosilane, hydrogen chloride technology, applied in chlorine/hydrogen chloride, chemical instruments and methods, organic chemistry and other directions, can solve the problems of low hydrogen chloride gas pressure, large occupation, pipeline blockage, etc., to improve product yield , Reasonable design, not easy to block the effect
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Embodiment 1
[0027] Concentrated hydrochloric acid circulates between the hydrolysis circulation pump and the separator, and a jet mixer and a static mixer are installed between the circulation pump and the separator. The jet mixer is purchased from the market, and the static mixer is made of graphite, ceramics, glass-lined , plastic or steel-lined plastic materials composed of one or more substances, dimethyl dichlorosilane is continuously fed into the jet mixer after being metered by a flow meter, and the concentrated hydrochloric acid circulation volume flow rate and dimethyl dichlorosilane in the jet mixer The volume flow ratio of dichlorosilane is 40:1; the mixed material undergoes a hydrolysis reaction at 40°C in a static mixer to generate methyl siloxane and gaseous hydrogen chloride, and the reaction mixture flows out of the static mixer and enters the gravity settling The gas-liquid separator performs three-phase separation of oil, acid and gas, and the gaseous hydrogen chloride ma...
Embodiment 2
[0030] Dimethyldichlorosilane is continuously fed into the jet mixer after being metered by a flowmeter. The volume flow ratio of concentrated hydrochloric acid circulation in the jet mixer to the volume flow ratio of dimethyldichlorosilane is 60:1; The hydrolysis reaction occurs in the mixer at 80°C, and the hydrolysis generates methyl siloxane and gaseous hydrogen chloride; the reaction mixture flows out of the static mixer and enters the gravity sedimentation gas-liquid separator for three-phase separation of oil, acid and gas, and the gaseous hydrogen chloride makes the separation The air pressure in the device reaches 0.4MPa (gauge pressure); when the gauge pressure is 0.4MPa, the mass concentration of circulating concentrated hydrochloric acid is 50%. The acid separated by the separator is returned to the hydrolysis circulation pump; the oil enters the atmospheric pressure hydrolysis system; the hydrogen chloride gas is cooled to remove water, purified and then sent to th...
Embodiment 3
[0033] Dimethyldichlorosilane is continuously fed into the jet mixer after being metered by a flowmeter. The volume flow ratio of concentrated hydrochloric acid circulation in the jet mixer to the volume flow ratio of dimethyldichlorosilane is 20:1; The hydrolysis reaction occurs in the mixer at 0°C, and the hydrolysis produces methyl siloxane and gaseous hydrogen chloride; the reaction mixture flows out of the static mixer and enters the gravity sedimentation gas-liquid separator for three-phase separation of oil, acid and gas, and the gaseous hydrogen chloride makes the separation The air pressure in the device reaches 0.1MPa (gauge pressure); when the gauge pressure is 0.1MPa, the mass concentration of circulating concentrated hydrochloric acid is 45%. The acid separated by the separator is returned to the hydrolysis circulation pump; the oil enters the atmospheric pressure hydrolysis system; the hydrogen chloride gas is cooled to remove water, purified and then sent to the ...
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