世界农药2024,Vol.46Issue(9) :23-27.DOI:10.16201/j.cnki.cn10-1660/tq.2024.09.04

吡唑醚菌酯羟胺关键中间体的催化加氢新工艺

New catalytic hydrogenation process for the key intermediate of pyraclostrobin hydroxylamine

李志恺 吴佳祥 陈雄杰 闫琦
世界农药2024,Vol.46Issue(9) :23-27.DOI:10.16201/j.cnki.cn10-1660/tq.2024.09.04

吡唑醚菌酯羟胺关键中间体的催化加氢新工艺

New catalytic hydrogenation process for the key intermediate of pyraclostrobin hydroxylamine

李志恺 1吴佳祥 1陈雄杰 1闫琦1
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作者信息

  • 1. 厦门嘉氢科技有限公司,福建 厦门 316000
  • 折叠

摘要

2-[(N-对氯苯基)-3-吡唑氧基甲基]硝基苯(简称吡唑醚)还原制备吡唑醚菌酯羟胺关键中间体的工业化常规工艺是使用雷尼镍为催化剂,水合肼做氢源,该方法羟胺选择性高,但过程中使用的雷尼镍、水合肼均为易爆品,存在较大安全隐患,且反应过程难控制.催化加氢原子利用率高,但催化加氢工业化制备羟胺仍是难点.采用铂碳催化加氢工艺,可实现吡唑醚原料转化率>99%,吡唑醚菌酯羟胺关键中间体选择性>99%,且工艺条件温和,化学工艺本质更安全.

Abstract

The industrial conventional process for the reduction of 2-[(N-p-chlorophenyl)-3-pyrazoloxy methyl]nitrobenzene(referred to as pyrazole ether)to prepare the key intermediate of hydroxylamine of pyraclostrobin is to use Raney nickel as catalyst and hydrazine hydrate as hydrogen source.This method has high selectivity for hydroxyamide,but the Raney nickel and hydrazine hydrate used in the process are both highly explosive,posing significant safety hazards,and the reaction process is difficult to control.Catalytic hydrogenation has a high atom utilization rate,but it is still difficult to prepare hydroxylamine industrially.By adopting the platinum-carbon catalytic hydrogenation process,the conversion rate of the raw material of pyrazole ether can be>99%,the selectivity of the key intermediate of hydroxylamine of pyraclostrobin can be>99%,with mild process conditions and inherently safer chemical engineering.

关键词

吡唑醚菌酯羟胺关键中间体/催化加氢/化工本质安全

Key words

key intermediate of pyraclostrobin hydroxylamine/catalytic hydrogenation/chemical intrinsic safety

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出版年

2024
世界农药
上海市农药研究所

世界农药

影响因子:0.494
ISSN:1009-6485
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