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Method and device for synthesizing chloromethane

A technology for the synthesis reaction of methyl chloride, which is applied in the field of preparing methane chloride, can solve the problems of high energy consumption, low-concentration hydrochloric acid, and long process, and achieve the effects of energy consumption, high conversion rate, and reduced pressure on waste acid treatment

Pending Publication Date: 2022-01-07
XINJIANG JINGSHUO NEW MATERIALS CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, regardless of the gas-phase method or the liquid-phase method, the reaction between methanol and hydrogen chloride will generate impurity dimethyl ether and the remaining unreacted hydrogen chloride gas. Therefore, it is usually necessary to wash with water, wash with alkali, and finally dry with concentrated sulfuric acid. Dehydration and removal of dimethyl ether and other devices will produce a large amount of low-concentration hydrochloric acid and alkali-containing waste liquid
At the same time, in the process of using methanol and hydrogen chloride to synthesize methyl chloride, it is necessary to continuously heat or cool the raw materials, thereby consuming a large amount of energy
It can be seen that the existing process for producing methyl chloride has many problems such as long process, numerous auxiliary materials, many by-products or three wastes, and high energy consumption.

Method used

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  • Method and device for synthesizing chloromethane

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Experimental program
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Effect test

Embodiment 1

[0049] (1) 15% of gaseous hydrogen chloride is mixed with 35% hydrochloric acid solution and preheated gaseous methanol into the first reaction kettle 5 for synthesis reaction through preheated concentration, wherein the total moles of hydrogen chloride in gaseous hydrogen chloride and hydrochloric acid solution amount, the ratio with the molar amount of gaseous methanol is 1.05:1; the liquid level in the first reaction kettle 5 is controlled at 50%, the pressure in the kettle is 2barg, and the temperature is 120°C. During the reaction, the amount of hydrochloric acid solution is adjusted , preheating temperature, or the preheating temperature of methanol gas maintains the reaction temperature in the first reactor 5, and the conversion rate of hydrogen chloride in the first reactor 5 is 90%;

[0050] (2) Methane chloride at the outlet of the first reactor 5, and the mixed gas of unreacted excess hydrogen chloride and a very small amount of unreacted methanol gas are passed into...

Embodiment 2

[0052] (1) gaseous hydrogen chloride is mixed with 18% through the preheated concentration that is 35% hydrochloric acid solution, the gaseous methanol through preheating is passed in the first reactor 5 and carry out synthetic reaction, wherein the total mole of hydrogen chloride in gaseous hydrogen chloride and hydrochloric acid solution amount, the ratio with the molar amount of gaseous methanol is 1.1:1; the liquid level in the first reaction kettle 5 is controlled at 50%, the pressure in the kettle is 3barg, and the temperature is 120°C. During the reaction, the amount of hydrochloric acid solution is adjusted , preheating temperature, or the preheating temperature of methanol gas maintains the reaction temperature in the first reactor 5, and the conversion rate of hydrogen chloride in the first reactor 5 is 86%;

[0053] (2) Methane chloride at the outlet of the first reactor 5, and the mixed gas of unreacted excess hydrogen chloride and a very small amount of unreacted m...

Embodiment 3

[0055] (1) 20% of gaseous hydrogen chloride is mixed with 35% hydrochloric acid solution through preheated concentration, and gaseous methanol through preheating is passed in the first reactor 5 to carry out synthesis reaction, wherein the total moles of hydrogen chloride in gaseous hydrogen chloride and hydrochloric acid solution amount, the ratio with the molar amount of gaseous methanol is 1.05:1; the liquid level in the first reaction kettle 5 is controlled at 50%, the pressure in the kettle is 2barg, and the temperature is 140°C. , preheating temperature, or the preheating temperature of methanol gas maintains the reaction temperature in the first reactor 5, and the conversion rate of hydrogen chloride in the first reactor 5 is 88%;

[0056] (2) Methane chloride at the outlet of the first reactor 5, and the mixed gas of unreacted excess hydrogen chloride and a very small amount of unreacted methanol gas are passed into the second reactor 6 to continue the reaction. At the...

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Abstract

The invention provides a method and a device for synthesizing chloromethane. The method comprises the following steps of: introducing gaseous hydrogen chloride, a preheated hydrochloric acid solution and preheated gaseous methanol as raw materials into a first reaction kettle for a synthesis reaction, and in the reaction process, adjusting the proportion of the hydrochloric acid solution in the raw materials and / or the preheating temperature of the hydrochloric acid solution and / or the preheating temperature of the gaseous methanol according to the reaction temperature in the first reaction kettle; and adding a hydrochloric acid solution into a second reaction kettle, introducing a mixed gas of chloromethane, hydrogen chloride and methanol at an outlet of the first reaction kettle into the second reaction kettle, and introducing liquid methanol for a synthesis reaction. The method does not need to additionally consume energy for heating or cooling, and greatly saves energy. Meanwhile, the double kettles are connected in series for continuous reaction, so that the high conversion rate of the raw materials is ensured. Moreover, waste acid is basically not generated, and the pressure of treating waste acid in a rear-end system is reduced.

Description

technical field [0001] The invention relates to the technical field of preparing methane chloride, in particular to a method and device for synthesizing methyl chloride. Background technique [0002] Chloromethane is an important raw material in the organic synthesis industry, and is mainly used to produce methyl green silane, a raw material for organic silicon compounds. Its synthesis process has been continuously developed in the past 30 years. At present, the mainstream development process in China mainly includes liquid-phase catalytic method and gas-solid-phase catalytic method. However, regardless of the gas-phase method or the liquid-phase method, the reaction between methanol and hydrogen chloride will generate impurity dimethyl ether and the remaining unreacted hydrogen chloride gas. Therefore, it is usually necessary to wash with water, wash with alkali, and finally dry with concentrated sulfuric acid. Dehydration and removal of dimethyl ether and other devices wi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C17/16C07C19/03B01J19/24
CPCC07C17/16B01J19/245C07C19/03
Inventor 李宏强王三跃高军锋马伟斌杨银银
Owner XINJIANG JINGSHUO NEW MATERIALS CO LTD
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