High purity 3,4-dimethyl benzaldehyde preparation method

A high-purity technology of dimethylbenzaldehyde, which is applied in the direction of carbon monoxide reaction preparation and organic chemistry, can solve problems such as difficult separation, high technical difficulty, and low product purity, and achieve mild reaction conditions, high product selectivity, and catalytic Performance-specific effects

Active Publication Date: 2006-11-22
溧阳常大技术转移中心有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The synthesis and generation process of 3,4-dimethylbenzaldehyde mainly include incomplete oxidation method, chloromethylation method, bromination hydrolysis method and carbonylation method to synthesize 3,4-dimethylbenzaldehyde method, and the obtained product It often contains a large amount of isomers of 3,4-dimethylbenzaldehyde and 3,4-dimethylbenzoic acid. The product components are relatively complicated, and there are more than ten kinds of by-products. The boiling point of a few by-products is very close to that of 3,4-dimethylbenzaldehyde, which is difficult to separate. The overall yield of the process is relatively low. The purity of the product after distillation and separation is still low. The cost of product separation is high and the technology is very difficult.
[0008] The catalytic hydrolysis of benzylidene dichloride or substituent benzylidene dichloride has been reported (GB899953, US3087967, US3524885, US4229379, US5347054), and the hydrolysis catalyst selects soluble zinc salt, and its yield is more than 95%, but zinc salt catalyst is in Excessive water is easy to deactivate, affecting product quality, and seriously causing heavy metal pollution to the environment
The patent US4229379 uses concentrated hydrochloric acid as a catalyst, and the yield is high, but the amount of water required for hydrogen chloride gas to be absorbed and recycled through a packed tower is large, reaching 10 to 25 times the stoichiometric amount, and the utilization rate of the reactor is low

Method used

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Examples

Experimental program
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Effect test

Embodiment 1

[0026] In a 1000ml four-neck flask, add weighed 216g o-xylene and 450g 1,2-dichloroethane, start the stirrer, add ice brine into the brine pot, and cool the contents of the reaction flask to Below -5℃, then add 30g cuprous chloride and 280g anhydrous aluminum trichloride in sequence, strictly control the operating temperature at -10~0℃, then open the CO cylinder valve, then open the hydrogen chloride generator concentrated sulfuric acid valve, slowly Drop concentrated sulfuric acid into the concentrated hydrochloric acid and sodium chloride bottles. At this time, there is hydrogen chloride gas overflowing from the liquid. Strictly control the volume flow ratio of CO and HCl to 1:1. The reaction takes about 8 hours, and continuous sampling and tracking at the end of the reaction Analysis shows that when the conversion rate of the reaction reaches 70%, the reaction is stopped, the CO and HCl vent valves are closed, and stirring is continued for 15 minutes, and then the above-mention...

Embodiment 2

[0028]In the same device as in Example 1, add the same amount of o-xylene and 1,2-dichloroethane as in Example 1, turn on the stirrer, add ice brine to the brine pot, and pre-load the contents of the reaction flask. Cool to below -5°C, then add 27g magnesium sulfate and 260g ferric chloride in sequence, strictly control the operating temperature at -10~0°C, then open the CO cylinder valve, then open the concentrated sulfuric acid valve of the hydrogen chloride generator, and add slowly Concentrated sulfuric acid is put into the concentrated hydrochloric acid and sodium chloride bottle, and the volume flow ratio of CO and HCl is strictly controlled at 1:1. The reaction takes about 8 hours. Continuous sampling and tracking analysis. When the single-pass conversion rate of o-xylene reaches 70% or more, Pour the above reactants slowly into a prepared 10%-20% 1500ml ice brine flask, extract, separate the lower acid water, put the upper oily substance in a rectifying flask, and then per...

Embodiment 3

[0030] In the same device as in Example 1, 216g o-xylene and 450g 1,2-dichloroethane were sequentially added, and then 30g cuprous chloride and 300g anhydrous cobalt acetate were sequentially added. The operating temperature was strictly controlled at -10~ 0℃, then open the CO cylinder valve, then open the concentrated sulfuric acid valve of the hydrogen chloride generator, slowly drop the concentrated sulfuric acid into the concentrated hydrochloric acid and sodium chloride bottles, strictly control the volume flow ratio of CO and HCl to 1:1, the reaction is about It takes 8 hours for continuous sampling and tracking analysis. When the end point is reached, slowly pour the above-mentioned reactants into a prepared 10%-20% 1500ml ice brine flask, extract, separate the lower acid water, and put the upper oily substance. Into the rectification flask, and then carry out vacuum distillation. The fractions are collected, and continuous sampling is performed for chromatographic tracking...

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PUM

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Abstract

This invention relates to a method for producing high-purity 3,4-dimethylbenzaldehyde, characterizing: in the four-hole bottle, add in weighted ortho-xylene and 1,2- dichloroethane, turn on the agitator, add ice salt water to the salt water boiler, pre-cool the material in the reaction bottle to -10-0DegC, and add sequentially Lewis salt compound catalyst, with operation temperature at -10-0Deg C, and then in CO atmosphere, dropwise add concentrated sulfuric acid, when the reaction conversion rate attains up to 70%, stop the reaction, turn off the CO and HCl gas valve, continue agitation, and then pour the above reactant material into already charged ice salt water boiling flask, after agitatation, put it in the separating funnel for extraction, mix homogeneously, stewing for stratification, remove the lower acidic water, put the above oil material to the distillation bottle, turn on the vacuum pump for pressure-decreasing distillation, collect the distillant and obtain the finished product. This invention is characterized of mild reaction condition, high catalyst activity, specific catalyst effect, high product selectivity, 'clean' process and easy separation.

Description

Technical field [0001] The invention relates to a process technology for preparing dialkylbenzaldehyde compounds by a low-temperature carbonylation method, specifically using o-xylene, CO, and HCl as raw materials, 1,2-dichloroethane as a solvent, and Lewis acid as a compound The preparation method of the catalyst for formylation reaction to synthesize high-purity 3,4-dimethylbenzaldehyde. Background technique [0002] 3,4-Dimethylbenzaldehyde is a new type of fine chemical intermediate, which plays an important role in fine organic synthesis. Mainly used in the synthesis of polyolefin transparent nucleating agent DMDBS [bis(3,4-dimethyldibenzylidene)sorbitol], and also used as raw materials for medicine and daily chemicals, such as viscosity modifiers and organic pollutants Coagulant, curing agent for pharmaceuticals and cosmetics, etc. [0003] The synthesis and production processes of 3,4-dimethylbenzaldehyde mainly include incomplete oxidation method, chloromethylation method...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C47/542C07C45/49
Inventor 张跃刘宇严生虎王芳马锦国石占崇沈介发刘建武
Owner 溧阳常大技术转移中心有限公司
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