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

Active Publication Date: 2010-09-01
HANGZHOU JINFADA CHEM IND
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  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] (1) The consumption of raw materials is high, and the unit consumption of dimethyldichlorosilane for the production of methylchlorosilane is above 1.78t
Since the hydrogen chloride generated during hydrolysis is discharged out of the system in the form of hydrochloric acid, part of the hydrogen chloride is removed by the desorption tower and then returned to the system, so the amount of hydrochloric acid discharged from the hydrolysis system is relatively large, and there are 4.2 tons of hydrochloric acid for every 1t of dimethyldichlorosilane consumed. Outflow, due to the limitation of hydrochloric acid settling time in the hydrolysis system, some siloxanes in the effluent hydrochloric acid have not been separated, and it needs to settle for more than 50 hours before it can be used for desorption. The siloxanes separated by sedimentation are all in acid Polymerized into polymers with higher molecular weight under the same conditions, the market value is lower
Moreover, siloxane in hydrochloric acid will also accumulate on the inner wall of the pipeline, causing pipeline blockage
[0006] (2) Because hydrogen chloride dissolves in water is a strong exothermic process, the hydrolysis process needs to be cooled with a large amount of water, and an average of 50 tons of cooling water is required for hydrolysis per ton of dimethyldichlorosilane. Because the hydrolysis temperature should not be too high, it cannot be used Circulating water is used as the coolant. If there is no low-temperature natural water and chilled water is used as the coolant, the energy consumption will be greater
[0008] (4) Since the hydrochloric acid discharged from hydrolysis needs to be settled, it is necessary to set up more large-volume hydrochloric acid settling tanks, which need to occupy a large area of ​​land for layout, and the polymers polymerized in hydrochloric acid need to be cleaned regularly. The emitted hydrogen chloride will cause certain pollution to the atmosphere
[0009] In view of the above defects in dilute acid hydrolysis, domestic enterprises have introduced concentrated acid hydrolysis technology from abroad, but there are disadvantages of low pressure of hydrogen chloride gas, low purity of hydrogen chloride gas, and expensive equipment, and industrial production is not very stable.

Method used

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  • Dimethyl dichlorosilane hydrolysis method for directly producing gaseous hydrogen chloride
  • Dimethyl dichlorosilane hydrolysis method for directly producing gaseous hydrogen chloride

Examples

Experimental program
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Effect test

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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Abstract

The invention discloses a dimethyl dichlorosilane hydrolysis method for directly producing gaseous hydrogen chloride, and belongs to the technical field of hydrolysis during the production of methyl chlorosilane. The method comprises the following steps of: pre-mixing the dimethyl dichlorosilane and concentrated hydrochloric acid through a jet mixer and then feeding the mixture into a static mixer for hydrolysis of concentrated hydrochloric acid with pressure so as to obtain a reaction mixture; introducing the reaction mixture into a combined separator with a plate type tower; separating the acid oil, acid and gas from the reaction mixture; and processing the acid oil, the acid and the gas respectively. The method ensures complete reaction and complete separation so as to obtain relatively pure hydrogen chloride gas and ensure difficult blockage of a methyl chloride synthesizer and pipelines thereof through forcible hydrolysis of the static mixer and separation of the combined separator with the plate tower in coordination with water removal by condensation; and the hydrogen chloride per se has pressure so as to realize the gravity feed of the hydrogen chloride. The method can obviously improve the product yield; and the unit consumption of the dimethyl dichlorosilane per ton of methyl siloxane is below 1.7 tons.

Description

technical field [0001] The invention belongs to the technical field of hydrolysis in the production process of methylchlorosilane, and in particular relates to a hydrolysis method of dimethyldichlorosilane capable of directly generating gaseous hydrogen chloride. Background technique [0002] Dimethyldichlorosilane is an important step in the production of organosilicon monomers. The methylsiloxane produced by hydrolysis is the main raw material for the production of a series of downstream products of organosilicon. [0003] The hydrolysis of dimethyldichlorosilane is usually hydrolyzed with dilute acid under normal pressure. The dilute hydrochloric acid is forced to circulate in the reaction system under the action of the circulation pump, and the dimethyldichlorosilane is sent into the inlet of the pump, which is realized under the high-speed cutting of the pump impeller. Fully mixed with hydrochloric acid and hydrolyzed, the hydrolyzed product is settled by gravity, hydro...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B7/01C07F7/16
Inventor 孔鑫明周海杨刘劭农周锦枫邓青松程晨杰汤晓娟江钧钧张俊杰
Owner HANGZHOU JINFADA CHEM IND
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