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3-溴吡啶连续化合成工艺研究

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采用分段式管式反应器连续化合成3-溴吡啶,当吡啶、氢溴酸和双氧水按摩尔比为1∶3∶1.2,一段管式反应器温度为50℃,停留时间为5min,二段管式反应器温度为90℃,停留时间为20min时,吡啶转化率达到99.2%,反应收率达到80.6%.采用负压精馏提纯,3-溴吡啶含量达到98.5%以上.合成与分离过程节能、高效,适合工业化生产.
Study on the Continuous Synthesis of 3-Bromopyridine
3-Bromopyridine was synthesized continuously in a two-stage tubular reactor. The molar ratio of pyridine,hy-drobromic acid and hydrogen peroxide was 1∶3∶1.2. The temperature of the first-stage tubular reactor was 50℃ and the residence time was 5 min. The temperature of the second-stage tubular reactor was 90℃ and the residence time was 20 min. The conversion rate of pyridine reached 99.2% and the reaction yield was 80.6%. The content of 3-bromopyridine reached 98.5% by negative pressure distillation. The process of synthesis and separation is energy saving and high effi-ciency,which is a suitable route for industrial production.

tubular reactorcontinuous synthesis3-bromopyridinenegative pressure distillation

谷顺明、刘国良、张正涛、金文娟、温兰兰

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安徽国星生物化学有限公司,安徽马鞍山 243100

管式反应器 连续化合成 3-溴吡啶 负压精馏

2024

安徽化工
安徽省化工研究院

安徽化工

影响因子:0.229
ISSN:1008-553X
年,卷(期):2024.50(4)