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Improved technology for condensation reaction in propiconazole synthesis

A technology of condensation reaction and propiconazole is applied in the field of improved technology of condensation reaction in the synthesis of propiconazole, can solve the problems of long condensation reaction time, difficult solvent treatment, dehydration difficulty and the like, avoids difficulty in solvent recovery, shortens dehydration and the like. time, and the effect of reducing energy consumption

Inactive Publication Date: 2019-09-13
浙江禾本科技股份有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The purpose of the present invention is to invent an improved process for the condensation reaction in the synthesis of propiconazole, which can solve the problem of adding a solvent during the condensation reaction of propiconazole to carry out precipitation reaction, resulting in longer condensation reaction time, difficult dehydration, and more energy consumption. And the problem of difficult solvent handling

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  • Improved technology for condensation reaction in propiconazole synthesis

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Embodiment 1

[0028] A kind of improved technology of condensation reaction in the synthesis of propiconazole

[0029] Including the following steps:

[0030] S1. Add 239㎏ triazole and 201㎏ potassium hydroxide into the 3000L reactor, then cover the manhole cover, raise the temperature at a rate of 1.5°C / min while stirring at a rate of 350 rpm, when the temperature rises to 58°C Finally, turn on the vacuum, the vacuum degree is -0.098MPa, and dehydrate under reduced pressure. When the temperature rises to 138°C, continue to dehydrate for 2 hours, then cool down to 70°C, add 990㎏ bromide, 1450㎏DMF, and then open the steam to raise the temperature to 140 ℃, heat preservation reaction for 5.5 hours, control in the sampling, control the bromide content to 0.08%, and the reaction is over;

[0031] Among the above, the bromide is trans-2-bromomethyl-2-(2,4-dichlorophenyl)-4-propyl-1,3-dioxolane.

[0032] S2. After the reaction is over, after recovering DMF under reduced pressure at a temperature...

Embodiment 2

[0034] A kind of improved technology of condensation reaction in the synthesis of propiconazole

[0035] Including the following steps:

[0036] S1. Add 259kg of triazole and 221kg of potassium hydroxide into a 3000L reactor, then cover the manhole cover, raise the temperature at a rate of 3.5°C / min while stirring at a rate of 650 rpm, when the temperature rises to 62°C Finally, turn on the vacuum, the vacuum degree is -0.092MPa, and dehydrate under reduced pressure. When the temperature rises to 142°C, continue to dehydrate for 3 hours, then cool down to 80°C, add 1010㎏ bromide, 1550㎏DMF, and then open the steam to raise the temperature to 145 ℃, heat preservation reaction for 6 hours, control in the sampling, control the bromide content to 0.12%, and the reaction is over;

[0037] Among the above, the bromide is trans-2-bromomethyl-2-(2,4-dichlorophenyl)-4-propyl-1,3-dioxolane.

[0038] S2. After the reaction is over, after recovering DMF under reduced pressure at a temper...

Embodiment 3

[0040] A kind of improved technology of condensation reaction in the synthesis of propiconazole

[0041] Including the following steps:

[0042] S1. Add 245kg of triazole and 206kg of potassium hydroxide into a 3000L reactor, then cover the manhole cover, raise the temperature at a rate of 2.0°C / min while stirring at a rate of 450 rpm, when the temperature rises to 59°C Finally, turn on the vacuum, the vacuum degree is -0.093MPa, and dehydrate under reduced pressure. When the temperature rises to 139°C, continue to dehydrate for 2.2 hours, then cool down to 72°C, add 995㎏ bromide, 1470㎏DMF, and then open the steam to raise the temperature to 141 ℃, heat preservation reaction for 5.6 hours, control in the sampling, control the bromide content to 0.20%, and the reaction is over;

[0043] Among the above, the bromide is trans-2-bromomethyl-2-(2,4-dichlorophenyl)-4-propyl-1,3-dioxolane.

[0044]S2. After the reaction is over, after recovering DMF under reduced pressure at a temp...

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Abstract

The invention discloses an improved technology for a condensation reaction in propiconazole synthesis. The improved technology comprises the following steps: mixing triazole with potassium hydroxide,carrying out reduced pressure dehydration, adding a bromide, performing condensation to form propiconazole, and adding water and toluene for layering and desolvation in order to obtain crude propiconazole. The improved technology for the condensation reaction in propiconazole synthesis is obtained by improving the conventional condensation technology, reduced pressure dehydration is directly carried out after mixing the triazole with the potassium hydroxide without adding a solvent, so the desolvation time is shortened in order to shorten the dehydration time from the original 19 h or above to4 h, thereby the improved technology significantly saves time, overcomes the difficulty of dehydration, reduces the energy consumption, and has progressive significance.

Description

technical field [0001] The invention relates to the technical field of propiconazole synthesis, in particular to an improved process for condensation reaction in the synthesis of propiconazole. Background technique [0002] Propiconazole is 1-[2-(2,4-dichlorophenyl)-4-propyl-1,3-dioxolane-2-methyl]-1-hydrogen-1,2,4- The general name of triazole is a broad-spectrum, systemic triazole fungicide with protective and therapeutic effects, which can be absorbed by roots, stems, and leaves, and can quickly conduct upwards in plants. Prevention and treatment of diseases caused by Ascomycetes, Basidiomycetes and Deuteromycetes, especially for banana leaf spot, wheat powdery mildew, leaf blight, grape powdery mildew, rice bakanae, etc. Up to 3-5 weeks. [0003] At present, in the condensation process of propiconazole, solvents such as toluene are generally added, solvent removal reaction, the mixed solvent produced after the reaction is difficult to handle, waste pollutes the environ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07D405/06
CPCC07D405/06
Inventor 王进陈共华曾挺潘光飞
Owner 浙江禾本科技股份有限公司