Synthetic method for preparing pyraclostrobin intermediate from o-nitrobenzyl chloride
A technology of pyraclostrobin and o-nitrobenzyl chloride, which is applied in the field of synthesis of organic compounds, can solve the problems of many by-products, low yield, and small yield, and achieve the reduction of environmental protection pressure, simple synthesis process, and low The effect of production costs
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Embodiment 1
[0034] In the present embodiment, the synthetic process of o-nitrobenzyl chloride is as follows:
[0035] Add catalyst (50 mesh activated carbon) into o-nitrotoluene, control the mass ratio of o-nitrotoluene to catalyst at 1:0.01, stir at 200r / min and heat to 100°C, slowly introduce chlorine gas, and track with gas chromatography The reaction by-product o-nitrobenzylidene dichloride reached 4%, the conversion rate of o-nitrotoluene was 39.7%, and the reaction was stopped; after the reaction was completed, under reduced pressure distillation at a vacuum degree of -0.097Mpa and a temperature of 110°C, the o-nitrotoluene was recovered. Toluene is continuously chlorinated and utilized; the residue after recovery of o-nitrotoluene is recrystallized and purified with petroleum ether to obtain white crystal o-nitrobenzyl chloride solid powder.
[0036] In this embodiment, the production effect of o-nitrobenzyl chloride with a purity of 99.3% and a yield of 83.7% (based on the actual ...
Embodiment 2
[0038] In the present embodiment, the synthetic process of o-nitrobenzyl chloride is as follows:
[0039] Add the catalyst (a mixture of activated carbon and DMF at a mass ratio of 2:1200 mesh) to o-nitrotoluene, control the mass ratio of o-nitrotoluene to catalyst at 1:0.2, stir at 400r / min and heat to 180°C , slowly feed chlorine gas, track the reaction by-product o-nitrobenzylidene dichloride with gas chromatography to reach 6%, and the conversion rate of o-nitrotoluene is 41%, stop the reaction; Distill under reduced pressure at ℃ to recover o-nitrotoluene, and continue to recycle chlorination; the residue after recovering o-nitrotoluene is recrystallized and purified with petroleum ether to obtain white crystalline solid powder of o-nitrobenzyl chloride.
[0040] In this embodiment, the production effect of o-nitrobenzyl chloride with a purity of 99.6% and a yield of 80.0% can be achieved (based on the actual consumption of o-nitrotoluene).
Embodiment 3
[0042] In the present embodiment, the synthetic process of o-nitrobenzyl chloride is as follows:
[0043] Add a catalyst (a mixture of bromine, azobisisobutyronitrile and azobisisoheptanonitrile in a mass ratio of 1:1:2) to o-nitrotoluene, and control the mass ratio of o-nitrotoluene to catalyst at 1 : 0.15, stirring at a speed of 300r / min and heating to 130°C, slowly introducing chlorine gas, tracking the reaction by-product o-nitrobenzylidene dichloride with gas chromatography to reach 5%, and the conversion rate of o-nitrotoluene is 40.2%, stop the reaction; After the reaction is over, distill under reduced pressure at a vacuum degree of -0.097Mpa and a temperature of 115°C to recover o-nitrotoluene and continue to circulate chlorination; the residue after recovery of o-nitrotoluene is recrystallized and purified with petroleum ether to obtain a white Crystalline o-nitrobenzyl chloride solid powder.
[0044] In this embodiment, the production effect of o-nitrobenzyl chlori...
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