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Glufosinate separation and purification method

A technology for separation and purification and glufosinate-ammonium, which is applied in the field of separation and purification of glufosinate-ammonium, can solve the problems of wasting raw materials, prolonging the number of processes, time, and low yield, and achieves the effect of improving the yield.

Active Publication Date: 2015-08-26
石家庄瑞凯化工有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] At present, there are many technical routes related to glufosinate-ammonium at home and abroad, among which the Stryker-Zelinsky method is more suitable for industrial production, but when it synthesizes glufosinate-ammonium, it will generate NH 4 Cl or NaCl and other by-products, and the separation and purification of glufosinate-ammonium by the usual crystallization method requires multiple recrystallizations to achieve the required purity requirements, and the more times of recrystallization, the lower the yield. The chemical reaction method represented by No. 201110160129.5 achieves the purpose of purifying glufosinate through the chemical reaction of esterification and hydrolysis. It needs two or three steps to complete the separation, which wastes raw materials, prolongs the number and time of processes, and due to the chemical reaction reduced yield

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0051] Step 1. Preparation of reaction solution: add 1900L of hydrochloric acid with a mass fraction of 30% to 2300Kg of 1-(methylethoxyphosphono)-butyronitrile solution, then reflux acid hydrolysis at 104-110°C for 3.5h to obtain 4650Kg Glufosinate-ammonium hydrochloride reaction solution; at this time, the content of glufosinate-ammonium hydrochloride in the detection reaction solution was 13.8%, and the mass of glufosinate-ammonium hydrochloride in the reaction solution was calculated to be 641.7Kg, and recorded;

[0052] Step 2. Concentration under reduced pressure: Distill the glufosinate-ammonium hydrochloride reaction solution obtained in Step 1 under vacuum conditions of -0.095MPa to remove dilute hydrochloric acid, stop the distillation when the temperature of the kettle rises to 75°C, and obtain concentrated solution A (The ingredients contained in the concentrate A include glufosinate-ammonium hydrochloride and secondary salt);

[0053] Step 3, adjust pH: in the con...

Embodiment 2

[0058] Step 1. Preparation of reaction solution: add 1900L of hydrochloric acid with a mass fraction of 30% to 2300Kg of 1-(methylethoxyphosphono)-butyronitrile solution, then reflux acid hydrolysis at 104-110°C for 3.5h to obtain 4650Kg Glufosinate-ammonium hydrochloride reaction solution; at this time, the content of glufosinate-ammonium hydrochloride in the detection reaction solution was 13.8%, and the mass of glufosinate-ammonium hydrochloride in the reaction solution was calculated to be 641.7Kg, and recorded;

[0059] Step 2. Concentration under reduced pressure: Distill the glufosinate-ammonium hydrochloride reaction solution obtained in step 1 under vacuum conditions of -0.095MPa to remove dilute hydrochloric acid, and stop the distillation when the temperature of the kettle rises to about 75°C to obtain a concentrated solution A (concentrate A contains ingredients including glufosinate-ammonium hydrochloride B and secondary salt),

[0060] Step 3, adjust pH: in the c...

Embodiment 3

[0065] Step 1. Preparation of reaction solution: add 1900L of hydrochloric acid with a mass fraction of 30% to 2300Kg of 1-(methylethoxyphosphono)-butyronitrile solution, then reflux acid hydrolysis at 104-110°C for 3.5h to obtain 4650Kg Glufosinate-ammonium hydrochloride reaction solution; at this time, the content of glufosinate-ammonium hydrochloride in the detection reaction solution was 13.8%, and the mass of glufosinate-ammonium hydrochloride in the reaction solution was calculated to be 641.7Kg, and recorded;

[0066] Step 2. Concentration under reduced pressure: Distill the reaction solution of glufosinate-ammonium hydrochloride obtained in Step 1 under a vacuum condition of -0.095MPa to remove dilute hydrochloric acid, and stop the distillation when the temperature of the kettle rises to about 75°C to obtain concentrated solution A (Concentrated solution A contains ingredients including glufosinate-ammonium hydrochloride and secondary salt);

[0067]Step 3, adjusting ...

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PUM

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Abstract

The invention belongs to the field of pesticide production and particularly relates to a glufosinate separation and purification method. According to the method, the separation and purification is started when a glufosinate hydrochloride reaction solution in the steps of distilling the glufosinate hydrochloride reaction solution under reduced pressure to remove dilute hydrochloric acid, adding ammonia water to adjust the pH to maximally produce ammonium chloride, distilling under reduced pressure to remove water, adding a flotation solvent for dispersion, placing the material into a chute at specific temperature and speed, performing flotation separation according to the difference in the proportion of a principal component and subsidiary salt, removing the solvent, dissolving the material in aqueous methanol to remove trace ammonium chloride, filling ammonia gas to adjust the pH value to 8, performing centrifugation and drying to obtain a final product. The glufosinate separation and purification method uses a flotation method for separating the principal component glufosinate and an intermediate of the principal component from the subsidiary salt ammonium chloride and the aqueous methanol for purification and is high in yield, good in purity, simple in process, low in cost and is suitable for industrial production.

Description

technical field [0001] The invention relates to the field of pesticide production, in particular to a separation and purification method for glufosinate-ammonium. Background technique [0002] Glufosinate-ammonium (glufosinate-ammonium or glufosinate) is a highly efficient, low toxicity, non-selective (killing) contact organophosphorus herbicide with partial systemic action. It has low toxicity, relatively safe, easy to degrade in soil, safe for crops, small drift, wide herbicidal spectrum, high activity, less dosage, less environmental pressure, and rapid weed killing, so it has broad market prospects. [0003] At present, there are many technical routes related to glufosinate-ammonium at home and abroad, among which the Stryker-Zelinsky method is more suitable for industrial production, but when it synthesizes glufosinate-ammonium, it will generate NH 4 Cl or NaCl and other by-products, and the separation and purification of glufosinate-ammonium by the usual crystallizati...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07F9/30
Inventor 张战刚许丽王收强肖丽彬成梦昭张明亮
Owner 石家庄瑞凯化工有限公司
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