Environment-friendly clean production method of high-purity cyanoacetic acid, cyanoacetate and malonate

A high-purity cyanoacetic acid and cyanoacetate technology, which is applied in chemical instruments and methods, carboxylate/lactone preparation, carboxylate preparation, etc., can solve the problem of cyanoacetic acid purification or high energy consumption and unclean salt separation , cumbersome operation and other problems, to achieve the effect of solving unclean salt separation, saving investment and reducing processing load

Inactive Publication Date: 2020-07-10
高春燕
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0016] Aiming at the deficiencies of current technology, the object of the present invention is to provide a kind of environment-friendly clean production method of high-purity cyanoacetic acid and cyanoacetic ester and malonate, to solve the problem of cyanoacetic acid purification or high energy consumption in the prior art, or operation cumbersome, serious decompos

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  • Environment-friendly clean production method of high-purity cyanoacetic acid, cyanoacetate and malonate

Examples

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Example Embodiment

[0056] Example 1: 1159.4kg of sodium cyanoacetate aqueous solution prepared by chloroacetic acid and sodium carbonate in water for neutralization reaction, and sodium cyanide solution for cyanation reaction (containing sodium cyanoacetate 23.33wt%, sodium chloride 12.88% , Water 61.47%), and 31wt% hydrochloric acid 296.4L for acidification reaction to obtain acidification solution containing cyanoacetic acid and sodium chloride (cyanoacetic acid 14.19wt%, sodium chloride 21.18wt%, water 63.43%), add salt precipitation agent The mass ratio of the amount of tert-butanol to the amount of water in the acidified liquid is 0.25:1, and about 80% of the sodium chloride in the acidified liquid is separated and filtered at 25°C. The washing liquid obtained by washing the solid sodium chloride with tert-butanol is used for reuse To the next salt precipitation, the filtrate after separating sodium chloride is about 1453kg (containing cyanoacetic acid 14.64wt%, sodium chloride 4.31wt%, water...

Example Embodiment

[0057] Example 2: As in Example 1, the desalinated solution with a salt content of less than 0.05% obtained from the shallow chamber by the above-mentioned electrodialysis desalination treatment was concentrated by vacuum evaporation until the water content of the concentrated solution was about 8wt%, and 1.8 times moles of cyanoacetic acid was added Add an amount of anhydrous methanol, drop an appropriate amount of 98wt% concentrated sulfuric acid catalyst, and control the temperature at 60~70℃ for esterification reaction. After the reaction is completed, the excess methanol is evaporated under negative pressure, and sodium carbonate solution is added for washing, neutralization, phase separation, and refinement. Distillation winner 234.7kg of high-purity methyl cyanoacetate with content ≥99.5%.

Example Embodiment

[0058] Example 3: As in Example 1, the desalinated solution with a salt content of less than 0.05% obtained from the desalination chamber by the above-mentioned electrodialysis desalination treatment was subjected to negative pressure evaporation and concentrated to a water content of about 12wt% in the concentrated solution, and 1.85 times moles of cyanoacetic acid was added Add an amount of absolute ethanol, drop an appropriate amount of 98wt% concentrated sulfuric acid catalyst, and control the temperature at 60~70℃ for esterification reaction. After the reaction is completed, the excess ethanol is evaporated under negative pressure, and sodium carbonate solution is added for washing, neutralization, phase separation, and refinement. 264.4kg of high-purity ethyl cyanoacetate with a content of ≥99.5%.

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Abstract

The invention discloses an environment-friendly clean production method of high-purity cyanoacetic acid, cyanoacetate and malonate. The method comprises the following steps: carrying out an acidification reaction on sodium cyanoacetate and hydrochloric acid or HCl gas to obtain an acidified solution, carrying out salt precipitation by using a salt precipitation agent, filtering to obtain a filtrate, carrying out electrodialysis and other desalination treatments to obtain a desalted solution, concentrating the desalted solution, and crystallizing to prepare high-purity cyanoacetic acid, or esterifying to prepare cyanoacetate, or carrying out acidolysis and esterification to prepare malonate. According to the method, cyanoacetic acid and sodium chloride are well separated by desalting methods such as electrodialysis after salt precipitation; and the problems of cyanoacetic acid decomposition caused by concentration separation of cyanoacetic acid and salt and sulfuric acid consumption andmixed salt wastewater treatment caused by residual sodium chloride during esterification in the prior art are avoided, so that the method is the environment-friendly and clean production method.

Description

technical field [0001] The invention relates to an environment-friendly and clean production method of high-purity cyanoacetic acid, cyanoacetate and malonate, belonging to the field of fine chemicals. Background technique [0002] Cyanoacetic acid is an important organic chemical intermediate with a wide range of uses. Its main downstream products include cyanoacetate and malonate. Cyanoacetate is an important intermediate of acrylic quick-drying adhesives. Malonate It is an important pharmaceutical and pesticide intermediate. [0003] At present, the industrial production of cyanoacetic acid uses chloroacetic acid as a raw material. The usual route is: neutralization reaction of chloroacetic acid and sodium carbonate (or sodium hydroxide) to obtain sodium chloroacetate, and then react with sodium cyanide to obtain sodium cyanoacetate and sodium chloride. , and then acidified with hydrochloric acid to obtain cyanoacetic acid and sodium chloride. It can be known from this ...

Claims

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Application Information

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IPC IPC(8): C07C253/30C07C253/34C07C255/19C07C51/09C07C55/08C07C67/08C07C69/38
CPCC02F2001/427C02F2103/36C07C51/09C07C67/08C07C253/30C07C253/34C07C255/19C07C55/08C07C69/38
Inventor 高春燕其他发明人请求不公开姓名
Owner 高春燕
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