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Process for preparing acephate from ethenone

A technology of acephate raw powder and ketene, which is applied in the field of pesticide acephate preparation and high-purity acephate preparation from ketene, which can solve the problem of lower product yield and purity, low total separation yield, Separation difficulties and other problems, to reduce decomposition loss, overcome the neutralization process, reduce the effect of side reactions

Inactive Publication Date: 2008-10-22
UNIV OF JINAN
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In above-mentioned these methods, all there is common problem: produce a large amount of acetic acid in the production process; Need to consume a large amount of ammoniacal liquor (or liquid ammonia) and because by-product ammonium acetate is too much in the neutralization process, ammonium acetate and acephate are easy Water-soluble substances have certain similarities in their properties, and it is difficult to completely separate them. Most production methods use ammonia water neutralization, and then use dozens of times the organic solvent to extract, as shown in Figure 1.
[0008] 1. Almost all the acephate obtained by the reaction meets with water (JP-B48-34583 is to use chloroform to extract acephate crude oil and then treat it with brine; JP-A64-75494 is to directly neutralize acephate with aqueous alkali solution Acephate crude oil), and acephate is easily decomposed in aqueous solution (especially in alkaline solution), so the loss of acephate may be larger in the separation process, resulting in a low total yield of separation
[0009] 2. Methamidophos is easily soluble in water, difficult to extract and has high solvent consumption; and when recovering the solvent, acephate is decomposed due to distillation, which reduces the yield and purity of the product
[0010] 3. A large amount of industrial wastewater is generated during the production process. The water cannot be recycled during the separation process and can only be discharged as wastewater in the end. This may cause the discharge loss of organic solvents and acephate, further increasing the separation cost
[0011] 4. Although neutralization with liquid ammonia can partially solve the above problems, such as CN1362415, the by-product ammonium acetate is too much, and it is difficult to separate. A part of acephate is entrained in the ammonium acetate, and solid-liquid separation and desorption are also required in the production process. High-purity acephate raw powder was obtained through complex processes such as dissolution and crystallization separation, coarse crystal purification, resulting in a decrease in yield
Since the emulsifiable concentrate prepared with mother liquor contains more impurities, the stability is generally poor

Method used

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  • Process for preparing acephate from ethenone
  • Process for preparing acephate from ethenone
  • Process for preparing acephate from ethenone

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033] In a 1000mL four-necked flask with a stirrer, condenser, thermometer and vent tube, add 472g of O, O-dimethylphosphorothioate, add 28g of dimethyl sulfate, carry out isomerization reaction to obtain 73.5% O,S-Dimethylphosphorothioate 500g. The reaction temperature is 50-65° C., and the reaction time is 3 hours.

[0034] Add 300mL of dichloroethane and 1.8g of p-toluenesulfonic acid to the above reaction product, under vigorous stirring, control the temperature at 20°C with ice-salt water, and feed the newly produced mixed gas of ketene and nitrogen to control about 40-50g Feed ketene at a rate of / hr, and stop the reaction when the reaction mixture no longer absorbs ketene. The reaction time is 4-6 hours. Cool down to 0-5°C, a large amount of solids are precipitated, filter, the mother liquor can be recycled to the next batch of reaction solution, and the product is washed with 100mL dichloroethane, and vacuum-dried to obtain 430g of acephate. The yield is 90.7% (with...

Embodiment 2

[0036] O, the preparation of S-dimethylphosphorothioate is the same as in Example 1.

[0037] In a 1000mL four-neck flask with a stirrer, condenser, thermometer and vent tube, add 500g of O, S-dimethylphosphorothioate (methamidophos), 300mL of dichloromethane and 1.5g of boron trifluoride - Diethyl ether, under vigorous stirring, control the temperature in a water bath to 20°C, feed the newly produced mixed gas of ketene and nitrogen, control the speed of about 40-50g / hr to feed ketene, when the reaction mixture no longer absorbs ketene stop responding. The reaction time was 6 hours. Cool down to 0-5°C, a large amount of solids are precipitated, filter, the mother liquor can be recycled to the next batch of reaction liquid, wash the product with 100mL dichloroethane, and vacuum dry to obtain 420g of acephate, the yield is 88.7%, and the product is white Solid purity 98.5%.

Embodiment 3

[0039] O, the preparation of S-dimethylphosphorothioate is the same as in Example 1.

[0040] In a 1000mL four-necked flask equipped with a stirrer, condenser, thermometer and vent tube, add 500g of O, S-dimethylphosphorothioate (methamidophos), 50mL of acetonitrile, 250mL of dichloromethane, 1.5g of tris Boron fluoride-ether and 2g dimethyl sulfate, under vigorous stirring, the temperature is controlled by a water bath at 25°C, and the newly produced mixed gas of ketene and nitrogen is introduced, and the rate of about 40-50g / hr is controlled to feed ketene. The reaction was stopped when the reaction mixture no longer took up ketene. The reaction time was 6 hours. Cool down to 0-5°C, a large amount of solids are precipitated, filter, the mother liquor can be recycled to the next batch of reaction liquid, wash the product with 100mL of dichloromethane, and dry in vacuum to obtain 425g of acephate, the yield is 89.7%, and the product is a white solid 98.5% purity.

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Abstract

The invention discloses a new method for using a ketene acetylation method to synthesize high purity acephate raw powder, which includes the following steps: O, O-dimethyl thiophosphoryl is used as raw material; the O, O-dimethyl thiophosphorus is isomerized to prepare O, S-dimethyl thiophosphoryl amine (methamidophos), the ketene and the O, S-dimethyl thiophosphoryl amine is caused to generate acetylation reaction at a proper speed, under the condition of a solvent and a catalyst and the temperature of minus 20 to 50 DEG C, the reaction time is 2 to 8 hours; and acephate raw powder is prepared through the processes of crystallization, solid-liquid separation and drying. The yield rate of the acephate raw powder prepared by the new method is high up to 90 percent (accounted by methamidophos), and the purity is up to 98 percent, without discharging waste liquid and polluting the environment.

Description

1. Technical field [0001] The invention belongs to the field of pesticides and relates to a method for preparing the pesticide acephate, in particular to a new method for preparing high-purity acephate from ketene. 2. Background technology [0002] Acephate is an acetylated derivative of the insecticide methamidophos. It is a good high-efficiency, low-toxicity, and low-residue broad-spectrum insecticide. It is effective against major pests of rice, cotton, vegetables, and fruit trees. It has good control effect and is one of the ideal varieties to replace highly toxic and high residue pesticides. Especially in the current social and economic development, some highly toxic pesticides such as methamidophos, parathion (1605), methyl parathion (methyl 1605), monocrotophos, ammonium phosphate and other five highly toxic pesticides Since January 1, 2007, the use in agriculture has been completely prohibited, and the structural adjustment of the agricultural industry is inevitable...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07F9/24
Inventor 郑庚修王秋芬卢言建
Owner UNIV OF JINAN
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