CN1340507A

CN1340507A - Process for preparing glyphosate

Info

Publication number: CN1340507A
Application number: CN 00125933
Authority: CN
Inventors: 季诚建; 任不凡; 周曙光; 翁路平; 邵振威; 江锋; 袁剑锋; 王萍; 黎显文
Original assignee: Zhejiang Xinan Chemical Industrial Group Co Ltd
Current assignee: Zhejiang Xinan Chemical Industrial Group Co Ltd
Priority date: 2000-08-31
Filing date: 2000-08-31
Publication date: 2002-03-20
Anticipated expiration: 2020-08-31
Also published as: CN1165540C

Abstract

A process for preparing glyphosate as herbicide from methylal as the by-product in productino of glyphosate includes oxidizing to obtain formaldehyde, dissolving it in alcohol solvent, adding glycine for addition reaction, then adding dimethyl phosphite for condensation reaction, acidic hydrolysis, and then removing solvent and acid to obtain the product. The advantages of product are high effect and broad spectrum.

Description

Preparation method of glyphosate

The invention belongs to a preparation method of glyphosate, in particular to a method for preparing glyphosate by using a product obtained by oxidizing methylal which is a byproduct in glyphosate production.

A process for the preparation of glyphosate (N-phosphonomethylglycine) is known from the document DE-OLSNo.p 2942898.6, which is: heating and dissolving paraformaldehyde or formaldehyde in an alcohol (such as methanol) solvent containing tertiary amine (such as triethylamine) for 5-15 minutes, then adding glycine and part of tertiary amine into the solution, dissolving at room temperature for 1-1.5 hours, or dissolving at reflux temperature for 15-20 minutes, maintaining reflux for 30-60 minutes, then adding dialkyl phosphite, condensing at 65-70 ℃, adding a proper amount of sodium hydroxide after 30-120 minutes to saponify the ester formed by condensation, saponifying for 1-2 hours, distilling at normal pressure after saponification is finished, recycling the alcohol and triethylamine, finally acidifying with hydrochloric acid with the same or slightly larger amount of the molar number of sodium hydroxide, and controlling the pH value of the solution to be between 1.0-1.9 to precipitate glyphosate. The known method has the defects that the cost of raw materials of the whole reaction is high, the yield of the glyphosate is not high, the yield can only reach 58-63 percent at most by the glycine, the whole system is required to be an anhydrous system, and the process conditions are harsh.

The invention aims to overcome the defects and provide a method for preparing glyphosate, which has high product yield and low raw material cost and is synthesized in an aqueous system.

The preparation method of the glyphosate has the technical scheme that formaldehyde obtained by oxidizing methylal which is a byproduct in glyphosate production is dissolved in an alcohol solvent, glycine is added into the obtained solution for addition reaction, dimethyl phosphite is added for condensation reaction, the reaction product is subjected to acidic hydrolysis, and the solvent and acid are removed after the hydrolysis to prepare the glyphosate.

The water content and the formaldehyde content of the reaction system are controlled to be 0.5-10% and 5-25% by weight respectively before the glycine is added.

The reaction is carried out in the presence of an organic base catalyst, preferably a tertiary amine, more preferably triethylamine.

The alcohol may be methanol, ethanol or propanol.

The formaldehyde is prepared by oxidizing methylal which is a byproduct of glyphosate production under the action of a catalyst, and water is generated at the same time, and the water is not easy to be removed completely. The known method considers that the glyphosate synthesis must be carried out in an anhydrous system, so the method has not been used for producing glyphosate. The inventor notices that a certain amount of water (0.5-10%) exists in the system in the glyphosate synthesis process by adopting the process route, glyphosate amine can be prepared by adjusting and optimizing process parameters such as reaction time, temperature, raw material ratio and the like, and the product yield is higher than the result reported in patent document DE-OLSNo.p 2942898.6.

The inventors have also noted that too much water content in the system directly affects the yield of the reaction product. The formaldehyde is soluble in alcohol solvents, so the invention adopts the alcohol solvents insteadof water to absorb formaldehyde which is gas generated by methylal oxidation, and the methylal oxidation reaction formula is as follows:

after formaldehyde is dissolved in alcohol, adding a certain amount of tertiary amine (catalyst) before addition reaction, and then adding a certain amount of alcohol, controlling the water content of the whole system to be 0.5-10% (W/W) and the formaldehyde content to be 5-25% (W/W), then adding glycine for addition reaction, wherein the reaction time is 30-100 minutes, and the addition reaction formula is as follows:

methanol is recommended to be used for absorbing and dissolving formaldehyde, and ethanol or propanol can also be used; triethylamine is recommended as the catalyst for the addition reaction, and tributylamine can also be used.

After the addition reaction is finished, adding dimethyl phosphite (the addition amount is 0.9-1.5 times of that of glycine by mol) into the system, heating for condensation reaction, wherein the reaction time is 0.5-2.5 hours, and the reaction formula is as follows:

the inventor notices that the acid hydrolysis is used for replacing the sodium hydroxide saponification to be beneficial to improving the yield of the glyphosate, so after the condensation reaction is finished, the cooling and the acid addition are carried out for hydrolysis, and the reaction formula is as follows:

the hydrolysis temperature is 40-50 ℃, and the hydrolysis time is 0.5-1 hour. And (3) distilling at normal pressure after hydrolysis is finished, recovering the solvent and methylal, refluxing for 1-2 hours afterdesolventizing is finished, deacidifying in vacuum, adding a proper amount of water to obtain glyphosate precipitate, and separating to obtain powdery glyphosate with the purity of 90-95% after post-treatment including standing, suction filtration and the like of materials.

The acid dosage has great influence on the yield of the glyphosate, the excessive high or insufficient low is unfavorable for improving the yield of reaction products, and the preferred acid dosage is 3 to 5 times of the mole number of the glycine.

The invention takes 1 mol of glycine, 0.70-1.2 mol of triethylamine and 0.90-1.5 mol of dimethyl phosphite.

The by-product methylal generated in the preparation process of the glyphosate can be oxidized to prepare formaldehyde for recycling.

Compared with the prior art, the method utilizes formaldehyde generated by oxidizing methylal which is a byproduct in glyphosate production to replace paraformaldehyde to produce glyphosate, so that the raw material cost is lower, the reaction is carried out in a system with a certain water content, the requirements on process conditions are not strict, the production cost is favorably reduced, and the yield (calculated by glycine) of the glyphosate can be improved from 58-63% (calculated by the prior art) to 75-78%.

The following describes embodiments of the present invention.

Example 1 formaldehyde gas generated by the oxidation of 0.68 mole of methylal was dissolved in 460ml of methanol, and the solution was charged into a four-necked flask equipped with a stirring and refluxing device, and 1 mole of triethylamine was added thereto, wherein 0.15 mole of water was contained in the system, and the amount of water was about 0.5% by weight based on the total weight of the system, and the formaldehyde content was 10.5%. Starting stirring, heating to 40 ℃ and maintaining for 15 minutes, adding 1 mol of glycine, preserving heat for 1.5 hours at 47 ℃ for addition reaction, then adding 1.4 mol of dimethyl phosphite, preserving heat for 1.5 hours at 60 ℃ for condensation reaction, finishing the reaction, cooling the system, dropwise adding 36% hydrochloric acid 270ml, stirring for 30 minutes, heating for desolventizing, recovering methanol and methylal at normal pressure, heating to 110 ℃, refluxing at the temperature for 1-2 hours, refluxing at the vacuum degree of 0.8Mpa for 1-2 hours, adding water for crystallization, precipitating and precipitating, standing for several hours, separating out crystals, and drying to obtain white powdery glyphosate with the purity of 90-95% and the yield of 76-78%.

Example 2 the procedure was as in example 1 except that the condensation reaction time was changed to 1 hour and, when 1 mole of glycine was used, the amounts of the respective substances and the amounts present were: 0.7 mol of methylal, 1350ml of methanol and 0.95 mol of triethylamine, wherein the content of formaldehyde (formaldehyde obtained by oxidizing methylal) in the system is 4.5 percent (W/W), the water content is 2.5 mol and accounts for about 4.5 percent (W/W) of the total amount of the system, 1.2 mol of dimethyl phosphite and 270ml of 36 percent hydrochloric acid, and the product yield is 75-76 percent.

Example 3 the procedure was as in example 1, except that when 1 mole of glycine was used, the amounts and amounts of the substances present were: 1 mol of methylal, 160ml of methanol and 1 mol of triethylamine, wherein the content of formaldehyde (formaldehyde obtained by methylal oxidation) in the system is 25% (W/W), the water content is 2.0 mol and is about 10% (W/W) of the total amount of the system, 1.3 mol of dimethyl phosphite and 270ml of 36% hydrochloric acid are adopted, and the product yield is 76-77%.

Example 4 the procedure was as in example 1, with 1 mole of glycine being used in the amounts and amounts of the substances present: 0.68 mol of methylal, 600ml of methanol and 1 mol of triethylamine, wherein the content of formaldehyde in the system is 8% (W/W), the content of water is 3.0 mol and accounts for about 6.9% (W/W) of the total amount of the system, 1.3 mol of dimethyl phosphite and 300ml of 36% hydrochloric acid, and the product yield is 74-76%.

The process sequence of the embodiment 5 is the same as that of the embodiment 1, the solvent is changed into ethanol, the other conditions are the same as that of the embodiment 1, and the product yield reaches 77-78%.

The process sequence of example 6 is the same as that of example 1, the catalyst triethylamine is changed into tributylamine, the other conditions are the same as those of example 4, and the product yield reaches 75-77%.

The process sequence of example 7 is the same as that of example 1, the solvent is changed into propanol, the catalyst is changed into tributylamine, the other conditions are the same as those of example 1, and the product yield reaches 75-76%.

Claims

1. The preparation method of glyphosate is characterized by that the formaldehyde obtained by oxidizing methylal as by-product of glyphosate production is dissolved in alcohol solvent, after the glycine addition reaction is added into the obtained solution, dimethyl phosphite is added for condensation reaction, the reaction product is undergone the process of acidic hydrolysis, and after the hydrolysis the solvent and acid are removed so as to obtain the invented glyphosate.

2. The process for producing glyphosate according to claim 1, wherein the water content of the reaction system is controlled to be 0.5 to 10% by weight before the addition of glycine.

3. The process for producing glyphosate according to claim 1, wherein the formaldehyde content in the reaction system is controlled to be 5 to 25% by weight before the addition of glycine.

4. A process for the preparation of glyphosate as claimed in claim 1, 2 or 3, characterized in that the reaction is carried out in the presence of an organic base catalyst.

5. The process of claim 4 wherein the organic base is a tertiary amine.

6. The process of claim 4, wherein the organic base is triethylamine.

7. The process of claim 6 wherein the alcohol is methanol, ethanol or propanol.