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A kind of continuous recovery device and continuous recovery process of glyphosate hydrolysis gas phase

A recovery device and glyphosate technology are applied in the field of glyphosate by-product recovery, which can solve the problems of hazardous waste of methyl chloride, consumption of methyl chloride, loss of by-products, etc., so as to avoid hazardous waste, improve recovery rate, and improve product yield. rate effect

Active Publication Date: 2022-04-12
SHANDONG WEIFANG RAINBOW CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, in the above-mentioned process, the hydrolysis of methyl chloride in a high-temperature alkaline environment will occur during the gas phase process of adding alkali and neutralizing the hydrolysis, which will consume methyl chloride and cause by-product loss. In addition, salty wastewater will be produced, resulting in dangerous recovery of methyl chloride. Waste, not environmentally friendly, long process

Method used

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  • A kind of continuous recovery device and continuous recovery process of glyphosate hydrolysis gas phase

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Experimental program
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Effect test

Embodiment 1

[0121] S1. The glyphosate hydrolysis gas enters the deacidification tower, the temperature at the top of the tower is 63°C, the temperature at the bottom of the tower is 102°C, and the temperature of the refrigerant in the first condensing device at the top of the tower is 28°C. Part of the gas components are discharged from the top of the deacidification tower. After condensation, the condensed methanol is completely refluxed, and the non-condensable gas enters the demethanol tower. The water and methanol in the hydrolysis gas form a self-reflux, and the hydrogen chloride and water flow to the bottom of the tower. Acid absorber for absorption.

[0122] Among them, the theoretical plate number of the deacidification tower is 18, and the gas inlet of the glyphosate hydrolysis gas is at the 10th plate.

[0123] S2. The non-condensable gas from the deacidification tower enters the methanol removal tower, the temperature at the top of the tower is 38°C, the temperature at the bott...

Embodiment 2

[0131] S1. The glyphosate hydrolysis gas enters the deacidification tower, the temperature at the top of the tower is 60°C, the temperature at the bottom of the tower is 100°C, and the temperature of the refrigerant in the first condensing device at the top of the tower is 30°C. Part of the gas components are discharged from the top of the deacidification tower. After condensation, the condensed methanol is completely refluxed, and the non-condensable gas enters the demethanol tower. The water and methanol in the hydrolysis gas form a self-reflux, and the hydrogen chloride and water flow to the bottom of the tower. Acid absorber for absorption.

[0132] Among them, the theoretical plate number of the deacidification tower is 18, and the gas inlet of the glyphosate hydrolysis gas is at the 12th plate.

[0133] S2. The non-condensable gas from the deacidification tower enters the methanol removal tower, the temperature at the top of the tower is 36°C, the temperature at the bott...

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Abstract

The invention provides a continuous recovery device and continuous recovery process of glyphosate hydrolysis gas phase. The present invention uses water washing and rectification to remove hydrogen chloride and water in the glyphosate hydrolysis gas, compared with the prior art, which adopts the method of adding alkali for neutralization and deacidification, and avoids the occurrence of high-temperature alkalinity of methyl chloride in the process of alkali addition and neutralization The hydrolysis of the environment reduces the loss of methyl chloride, increases its yield, and does not produce saline wastewater; it also makes deacidification and dehydration a one-step operation, and the operation is simple; the invention also recovers glyphosate by means of absorption + rectification The methyl chloride in the phosphine hydrolysis gas can avoid the hazardous waste produced by the drying of concentrated sulfuric acid in the prior art and improve the product yield; the present invention also uses the methylal component separated from the glyphosate hydrolysis gas itself as an absorbent and puts it into the methyl chloride for absorption Absorption and separation of methyl chloride in the tower eliminates the need to introduce additional absorbents, which reduces costs; and no other materials with new components are introduced for absorption, which can avoid the introduction of impurities and improve the purity of methyl chloride products.

Description

technical field [0001] The invention relates to the field of recovery of glyphosate by-products in chemical production, in particular to a continuous recovery device and continuous recovery process of glyphosate hydrolysis gas phase. Background technique [0002] As a non-selective, non-residue herbicide, glyphosate is very effective especially for perennial root weeds, especially because of its high efficiency, low toxicity, broad spectrum, and no residue, it has been more and more popular. high attention. It was developed by Monsanto in the early 1970s, and it is generally used as isopropylamine salt or sodium salt. Wherein, during the production of glyphosate by the glycine method, a large amount of methyl chloride will be produced by-product, and its preparation route is roughly as follows: using glycine+paraformaldehyde+dialkyl phosphite (such as dimethyl phosphite) as raw material, in methanol A condensation reaction occurs under the action of a solvent and a triethy...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C17/38C07C17/383C07C29/76C07C41/58C07F9/38C07C19/03C07C43/30C07C31/04
CPCC07C17/38C07C17/383C07F9/3813C07C41/58C07C29/76C07C19/03C07C43/30C07C31/04
Inventor 袁良国侯永生王亮孙国杰单志松迟志龙
Owner SHANDONG WEIFANG RAINBOW CHEM
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