Process for producing high-purity methane chloride

A technology of monochloromethane and methyl chloride, which is applied in the field of methane chloride production technology, can solve the problems of increasing equipment investment, increasing operating costs, and relatively high requirements for rectification tower materials, and achieves the effect of increasing equipment investment and increasing content

Inactive Publication Date: 2011-08-17
于淑芳
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although this method increases the content of monochloromethane, because there is no alkali washing process in the production process of the crude product of monochloromethane, the acidity in the crude product of monochloromethane is relatively high, and the requirements for the material of the rectifying tower are relatively high duri

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] Methanol and hydrogen chloride react in the gas phase under the condition of 210°C and 0.18MpaG in the presence of activated alumina catalyst to generate monochloromethane and water. The temperature of the gaseous product was quenched by dilute hydrochloric acid and dropped to 50°C. The liquid phase after chilling is 20% dilute hydrochloric acid, and the gas phase passes through the pickling tower, the alkali washing tower and the sulfuric acid drying tower successively, and is compressed and condensed to obtain crude monochloromethane. Absorb the unreacted hydrogen chloride in the reaction gas with chilled dilute hydrochloric acid in the pickling tower, and neutralize the unabsorbed hydrogen chloride in the reaction gas with 10% sodium hydroxide in the alkali washing tower. 22% of the hydrochloric acid out of the pickling tower produces 31% of hydrochloric acid, and about 3-5% of the alkali out of the alkali washing tower enters the exhaust gas scrubbing system to neut...

Embodiment 2

[0025] Methanol and hydrogen chloride react in the gas phase at 300°C and 0.38MpaG in the presence of an activated alumina catalyst to produce methylene chloride and water. The gas phase product was quenched by dilute hydrochloric acid and the temperature was lowered to 80°C. The liquid phase after chilling is 20% dilute hydrochloric acid, and the gas phase passes through the pickling tower, the alkali washing tower and the sulfuric acid drying tower successively, and is compressed and condensed to obtain crude monochloromethane. Absorb the unreacted hydrogen chloride in the reaction gas with chilled dilute hydrochloric acid in the pickling tower, and neutralize the unabsorbed hydrogen chloride in the reaction gas with 10% sodium hydroxide in the alkali washing tower. 22% of the hydrochloric acid out of the pickling tower produces 31% of hydrochloric acid, and about 3-5% of the alkali out of the alkali washing tower enters the exhaust gas scrubbing system to neutralize the aci...

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Abstract

The invention provides a process for producing high-purity methane chloride. The process comprises the following steps of: introducing vaporized and overheated methanol and hydrogen chloride a reactor containing an alumina catalyst and reacting in the reactor to generate a mixture of methane chloride, methane, chloroethane and dichloromethane; introducing the generated mixture to a chilling device, carrying out chilling separation and then introducing into an acid-washing tower, an alkaline washing tower and a sulfuric acid drying system, compressing to prepare coarse methane chloride; leading the coarse methane chloride into a treating column and separating out heavy components from the bottom of the treating column; evaporating light-component methane and methane chloride to the top of the treating column together; then performing water cooling and deep freezing so that the methane chloride is liquefied, completely discharging the methane which is not liquefied into an exhaust washing tower by a deep freezer so as to separate methane chloride from methane and finally obtain high-purity methane chloride. In the invention, a single-tower rectification manner is adopted, therefore, equipment investment is not increased greatly, but also the content of methane chloride is increased to be higher than 99.98%.

Description

technical field [0001] The invention relates to a production process of methane chloride, in particular to a production method of high-purity monochloromethane. Background technique [0002] With the development of the organosilicon industry and the continuous development of downstream products of monochloromethane, the demand for commercial quantities of monochloromethane is increasing, but at this stage most of the production facilities for monochloromethane are only produced as supporting equipment, and the quality of monochloromethane Difficult to meet market requirements. At present, the synthesis of monochloromethane adopts gas-solid phase catalysis and liquid phase catalysis. In the production process of gas-solid catalysis, there are two production methods: [0003] One is that the crude monochloromethane that has undergone catalytic reaction is quenched, washed with water, washed with alkali, dried with sulfuric acid, and then compressed to obtain methyl chloride. ...

Claims

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Application Information

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IPC IPC(8): C07C19/03C07C19/043C07C17/10
Inventor 于淑芳
Owner 于淑芳
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