Novel process and synthesis device for preparing glyphosate by hydrolyzing by-product acid instead of hydrochloric acid

A technology of glyphosate and by-product acid, which is applied in the field of new glyphosate preparation process and synthesis device by hydrolysis of by-product acid instead of hydrochloric acid, which can solve the constraints of glyphosate synthesis process optimization, difficulty in transporting to the reaction system, and difficulty in hydrogen chloride Problems such as metering, to achieve the effect of reducing raw material and equipment investment costs, shortening condensation reaction time, increasing production capacity and purity

Pending Publication Date: 2021-01-08
ZHENJIANG JIANGNAN CHEM
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  • Abstract
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  • Application Information

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Problems solved by technology

[0003] However, the traditional hydrolysis process is complicated, and the reaction between by-products or between by-products and raw materials seriously restricts the further optimization of glyphosate synthesis process.
Moreover, hydrochloric acid mainly comes from the recovery and reuse of dimethyl phosphite by-product hydrogen chloride, which needs to be condensed, washed with water and alkaline, and the refining process is complicated
Chinese patent application number 201910453082.8 discloses a method and device for applying dimethyl phosphite hydrogen chloride tail gas to the synthesis of glyphosate, and proposes to directly use hydrogen chloride instead of hydrochloric acid for hydrolysis to reduce waste water discharge. However, the utilization rate of hydrogen chloride It is only 20%. In addition, hydrogen chloride is not easy to measure as a gas, and it is difficult to transport it to the reaction system, and it consumes a lot of energy.
Therefore, how to effectively avoid the hydrolysis of other by-products containing methoxy groups in the esterification stage through temperature control in the desolventization stage, and precisely improve the directional production of glyphosate is a major problem in the glyphosate industry; Formaldehyde and dimethyl phosphite are usually added in excess, which makes the intermediate reaction more complicated; it is generally believed that side reactions are positively correlated with temperature, but many other processes reported ignore this, such as the feeding temperature of dimethyl phosphite , if it is too high, it will lead to the formation of intermediates such as dimethyl hydroxymethyl phosphate, which will seriously affect the yield, which is also the deficiency of previous studies

Method used

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  • Novel process and synthesis device for preparing glyphosate by hydrolyzing by-product acid instead of hydrochloric acid

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Experimental program
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Embodiment 1

[0023] A synthesis device for preparing glyphosate by hydrolysis of hydrochloric acid instead of by-product acid, comprising a first synthesis reactor 1, a balance tank 2, a hydrolysis reactor 3 and a crystallization reactor 4 connected in series in sequence; the first synthesis reactor 1 Feed inlet is communicated with methanol metering tank 11, triethylamine metering tank 12, paraformaldehyde metering tank 13, glycine metering tank 14 and dimethyl phosphite metering tank 15 respectively through feed pipe; The feed port of the hydrolysis reactor 3 is communicated with the hydrochloric acid metering tank 31, the liquid alkali metering tank 32 and the water metering tank 33 respectively through pipelines; and tail gas absorption tank 35; the bottom outlet of the crystallization reactor 4 is connected to the mother liquor large tank 41 and the washing machine 42 through pipelines respectively, and the liquid outlet of the washing machine 42 is connected to the mother liquor large...

Embodiment 2

[0026]Prepare 4.5mol and 0.41mol of the raw materials in the methanol metering tank and the triethylamine metering tank respectively, put the measured solvent methanol and catalyst triethylamine into the first synthesis reaction kettle, and start stirring; then put the prepared material in the paraformaldehyde metering tank 0.12mol of paraformaldehyde is put into the first synthesis reaction kettle, and the temperature is controlled at 32-42°C to start the depolymerization reaction. After the paraformaldehyde is completely dissolved, put 0.43mol of glycine prepared in the glycine metering tank into the first synthesis reaction kettle, and react at a temperature of 37-52°C for 30-55min; mol dimethyl phosphite is quickly added to the first synthesis reaction kettle in batches, the temperature is controlled at 47-60°C, and triethylamine and dimethyl phosphite are added after holding the temperature for 8-10 minutes to adjust the pH of the system to 7.5-7.8. After 50-100 minutes, ...

Embodiment 3

[0028] Prepare 4.5mol and 0.41mol of the raw materials in the methanol metering tank and the triethylamine metering tank respectively, put the measured solvent methanol and catalyst triethylamine into the first synthesis reaction kettle, and start stirring; then put the prepared material in the paraformaldehyde metering tank 0.12mol of paraformaldehyde is put into the first synthesis reaction kettle, and the temperature is controlled at 36-40°C to start the depolymerization reaction. After the paraformaldehyde is completely dissolved, put 0.43mol of glycine prepared in the glycine metering tank into the first synthesis reaction kettle, and react at a temperature of 37-52°C for 30-55min; mol dimethyl phosphite is quickly added to the first synthesis reaction kettle in batches, the temperature is controlled at 47-60°C, and triethylamine and dimethyl phosphite are added after holding the temperature for 8-10 minutes to adjust the pH of the system to 7.5-7.8. After 50-100 minutes,...

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Abstract

The invention discloses a novel process and a synthesis device for preparing glyphosate by hydrolyzing by-product acid instead of hydrochloric acid. The novel process comprises the steps of (1) preparing a synthetic liquid L1 by taking glycine, dimethyl phosphite and paraformaldehyde as raw materials, methanol as a solvent and triethylamine as a catalyst; (2) adding post-treatment hydrochloric acid into the synthetic liquid L1 for hydrolysis and desolvation, and adding alkali to adjust the pH after hydrolysis and desolvation; and (3) adding deionized water, cooling, stirring and crystallizingto obtain a crystallization solution L2, washing and drying to obtain a glyphosate finished product. According to the invention, improvement is carried out on the basis of glyphosate production by a glycine alkyl ester method, a by-product hydrochloric acid for preparing phosphorus trichloride is adopted to replace hydrochloric acid to hydrolyze a synthetic liquid after post-treatment, and meanwhile, each key process index parameter is optimized, so that the utilization rate of the by-product acid in a chemical industrial park is increased, and the yield and the purity of the glyphosate raw powder are greatly improved. Meanwhile, because a large amount of water carried by the introduction of hydrochloric acid is avoided, the recovery energy consumption of by-products such as methanol and the like and the discharge amount of wastewater are also reduced.

Description

technical field [0001] The invention relates to the technical field of glyphosate pesticide production, in particular to a new process and synthesis device for preparing glyphosate by hydrolysis of by-product acid instead of hydrochloric acid. Background technique [0002] Glyphosate, the English common name glyphosate, alias N-(phosphonic acid methyl) glycine, also known as zhencaoning, Benda, etc., is an agricultural chemical, which is a low-toxic systemic conduction type broad-spectrum weed control agent. It is mainly used in commercial crop gardens such as orchards, and has a significant effect on the control of perennial malignant weeds. At present, there are two mainstream production routes at home and abroad. One is to use iminodiacetic acid (IDA) as raw material. The process is simple, the process conditions are relatively mild, and the product yield is high. There are few restrictions in domestic application. At present, large foreign companies mostly use this proc...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07F9/38
CPCC07F9/3813
Inventor 王群孝朱建民范淑芬王垚车骏秦虹张建民沈玉香
Owner ZHENJIANG JIANGNAN CHEM
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