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Method of obtaining alkali metal salts of n-phosphonomethylglycine

IPC classes for russian patent Method of obtaining alkali metal salts of n-phosphonomethylglycine (RU 2364601):
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FIELD: chemistry.

SUBSTANCE: claimed invention relates to method of obtaining alkali metal salts of N-phosphomethylglycine and can be applied in agriculture, for fight against weeds. Claimed method lies in the following: reaction of glyphosate and alkaline reagent interaction is carried out in solid phase in highly efficient mixer in conditions of crashing and in close contact of reaction components.

EFFECT: development of new method for obtaining N-phosphomethylglucine salts without solvents.

4 cl, 4 ex

 

This invention relates to the petrochemical industry, and more specifically, to obtain alkali metal salts of organic acids, which are used in pure form or as intermediates in the production of economic goods. So, alkali metal salts of biologically active organic acids are used as herbicide funds in the fight against weeds ("Handbook of pesticides and agrochemicals permitted for use on the territory of the Russian Federation", Moscow, 2007, publishing house "Agrorus", str, 177).

In this invention we are talking about a method of producing alkali metal salts of N-phosphonomethylglycine (glyphosate) as a herbicide funds for destruction of weeds ("Handbook of pesticides and agrochemicals permitted for use on the territory of the Russian Federation", Moscow, 2007, publishing house "Agrorus", str).

Known conventional option of obtaining alkali metal salts of organic acids, when an aqueous solution of the alkaline agent is in contact with an organic acid.

For example, in U.S. Pat. U.S. No. 6096686 potassium salt of N-phosphonomethylglycine (glyphosate) is obtained by neutralization of the glyphosate aqueous solution of KOH to a pH equal to 7.

However, as is common variant of the synthesis of alkaline salts of organic acids, and specifically potassium salt GL is fosatu have fault, associated with significant costs if you need to get dry (anhydrous) salts, namely the introduction of additional process steps, including evaporation, unloading and drying salt.

Getting dry (anhydrous) alkali metal salts of glyphosate opens the prospect of creating a new glyphosate containing products in the form of water-soluble powders or water-soluble granules.

New progressive forms allow you to raise the concentration of biologically active agent (glyphosate) in the product up to 700 g or more per 1 kg and significantly impact on the economy of the production of glyphosate containing products.

The present invention is to develop a method of producing alkali metal salts of glyphosate in a dry (anhydrous) variant that eliminates the shortcomings of traditional methods of obtaining such salts.

This object is achieved in that the formation of alkali metal salts of glyphosate is carried out in a solid phase under conditions of mechano-chemical interaction of glyphosate and an alkaline reagent (NaOH, KOH, N2CO3To2CO3with Tonino grinding no more than 20 microns in effective Z-shaped worm-blade mixer, ensuring close contact of the components of the reaction.

To implement the invention can be used l the all other mechanical devices, providing functions of crushing and contact the solid reactants.

It can be electromagnetic shredders, high-speed multi-blade centrifugal mixers, etc.

Experiments were performed as follows.

In the Z-shaped mixer downloaded the estimated amount of the powder of glyphosate and an alkaline reagent (NaOH, KOH, N2CO3To2CO3with Tonino grinding no more than 20 microns, included mixer (rotation rate of the mixing device 60 rpm) at ambient temperature. The reaction time varied from 60 to 90 minutes Transition of crystalline structures of glyphosate and an alkaline reagent in solid crystalline alkali salt of glyphosate is on the middle of the reaction through a stage of powdery amorphous state.

Upon completion of the reaction from the mixer get dry, loose corresponding salt of an alkali metal glyphosate, in the case of alkali and without the stage of formation of the amorphous state due to the selection process of the reaction of carbon dioxide, in the case of carbonates.

Two of the considered structures of alkaline chemicals (alkalis and carbonates) should be preferred carbonates, because they, unlike pure alkali, leave in the reaction products two times less water of crystallization (4.3% as against 8.6 per cent for alkalis).

Output about what aktov reaction was determined as the ratio of the weight actually unloaded the reaction products together with crystallization water to theoretically calculated.

The above is illustrated by the following examples.

Example 1

In the Z-shaped mixer was downloaded 169 g (1 mol) of powdery glyphosate and 40 g (1 mol) of powdered NaOH. When the ambient temperature was performed solid-phase reaction for 70 min Uploaded 204,9 g dry powdered Na-salt of glyphosate. The estimated weight of Na-salt of glyphosate according to the reaction 209, the Output of the Na-salt of glyphosate 98%.

Example 2

Analogously to example 1 was downloaded 169 g (1 mol) of glyphosate and 56 g (1 mol) of KOH. The reaction time of 60 minutes was Unloaded to 220.3 g (225 g estimated number) dry powder K-salt of glyphosate. Access To the salt of glyphosate is 97.7%.

Example 3

Analogously to example 1 was downloaded 169 g (1 mol) of glyphosate and 53 g (0.5 mol) of Na2CO3. Carried out the reaction for 90 min Uploaded 195,4 g (200 g estimated number) of dry powdered Na-salt of glyphosate. The output of the Na-salt of glyphosate, which is 97.5%.

Example 4

Analogously to example 1 was downloaded 169 g (1 mol) of glyphosate and 69 g (0.5 mol)2CO3. Carried out the reaction within 80 minutes Unloaded 210,5 g (216 g estimated number) dry powder K-salt of glyphosate. The output of the K-salt of glyphosate 97,4%.

1. The method of obtaining alkali metal salts of N-phosphonomethylglycine (glyphosate), characterized in that the reaction of interaction of glyphosate and the alkaline reagent is carried out in the solid phase in high-performance is Musicale in conditions of grinding and closely components of the reaction.

2. The method according to claim 1, characterized in that the crushing of the components of the reaction should be not more than 20 μm.

3. The method according to claim 1, characterized in that the reaction of the interaction is carried out at ambient temperature.

4. The method according to any one of claims 1 to 3, characterized in that the interaction time is 60-90 minutes

 

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