A kind of preparation method of saflufenacil
A technology of saflufenacil and sulfonyl diamide, which is applied in the field of preparation of saflufenacil, can solve the problems of many impurities in side reactions, difficult separation of condensing agents, high production costs, etc., and achieve high total yield, The effect of reducing industrial salt solid waste and three wastes
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Embodiment 1
[0020] (Embodiment 1) Saflufenacil
[0021] Preparation of the target product in a small test:
[0022] Put 60.5g (0.20mol) of I-methyl intermediate and 100g of benzene into a 500mL glass bottle, heat and stir at 60°C, control the amount of chlorine gas 60g through the mass flow meter, and control the amount of I-methyl intermediate in the total material during the heat preservation The normalized content of liquid chromatography is less than 1%, the solvent is recovered by precipitation and the by-product hydrochloric acid is recovered by negative pressure to obtain the crude product of I-trichlorobenzyl intermediate, the by-product hydrochloric acid is recovered by solvent washing and liquid separation, and the recovery rate of solvent dehydration is 90%. Produce 28% hydrochloric acid 100g.
[0023] Under the protection of nitrogen, 150 g of dichloroethane and 30.5 g of sulfonamide intermediate were successively added to the above-mentioned 500 mL reaction vessel, stirred e...
Embodiment 2
[0025] Preparation of target product in pilot scale:
[0026] Put 605kg of I-methyl intermediate and 1,200kg of benzene into a 5000L enamel kettle, heat and stir at 60°C, control the amount of chlorine gas 590kg through the mass flow meter, and control the liquid chromatography of I-methyl intermediate in the total material in the heat preservation The content is less than 1%. The solvent is recovered by precipitation and the by-product hydrochloric acid is recovered by negative pressure to obtain the crude product of I-trichlorobenzyl intermediate. The by-product hydrochloric acid is recovered by solvent washing and liquid separation. The recovery rate of solvent dehydration is 92%, and the by-product 28% hydrochloric acid is 1050kg .
[0027] Under the protection of nitrogen, 1500 kg of dichloroethane and 310 kg of sulfonamide intermediates were sequentially added to the above-mentioned 5000L reaction kettle, stirred evenly and then raised to a reflux temperature of 90°C; T...
Embodiment 3
[0028] (Example 3) One-pot method does not separate and synthesize saflufenacil
[0029] Preparation of the target product in a small test:
[0030] Put 60.5g (0.20mol) of I-methyl intermediate and 100g of benzene into a 500mL glass bottle, heat and stir at 60°C, control the amount of chlorine gas 60g through the mass flow meter, and control the amount of I-methyl intermediate in the total material during the heat preservation The normalized content of liquid chromatography was less than 1%, and hydrogen chloride was pulled out under negative pressure to recover 90 g of by-product hydrochloric acid to obtain a crude benzene solution of I-trichlorobenzyl intermediate, which was directly used in the next step.
[0031] Under the protection of nitrogen, add 30.5g of sulfonamide intermediate to the above-mentioned 500mL reaction vessel in turn, stir well and then rise to the reflux temperature of 90°C; at this temperature, reflux and keep warm until the liquid phase of the I-trich...
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