首页> 外文期刊>Organic process research & development >Overcoming Problems at Elaboration and Scale-up of Liquid-Phase Pd/C Mediated Catalytic Hydrogenations in Pharmaceutical Production
【24h】

Overcoming Problems at Elaboration and Scale-up of Liquid-Phase Pd/C Mediated Catalytic Hydrogenations in Pharmaceutical Production

机译:克服制药生产中液相Pd / C介导的催化加氢的规模化和规模化问题

获取原文
获取原文并翻译 | 示例
       

摘要

The practical solutions for scale-up and production of intermediates or precursors of pharmaceuticals by liquid phase Pd/C mediated hydrogenation can be of considerable interest and deserve broader attention even if they have not been the focus of previously published research due to regulations of patent law. The practical obstacles are persistent and have been known for a long time, but for the most part remained unpublished. The most important discoveries and solutions that contributed to the successful scale-up of hydrogenations for pharmaceutical production were the following: (i) the poisoning of Pd/C catalyst with Fe2+ ions for the selective hydrogenation of 2,6-dimethyl-1-nitrosopiperidine to the corresponding hydrazo compound; (ii) alloying of the deposited Pd metal with Cu for converting the aromatic acid chlorides into the corresponding aldehydes; (iii) alteration of the pH of the reaction mixture to basic values which enhanced the stereoselectivity of paracetamol hydrogenation; (iv) a useful modification of the catalyst preparation process, i.e, the acidification of the catalyst resulted in the hydrogenolysis of benzylic OH in a molecule containing a basic N atom; (v) use of two liquid phases, altogether a four-phase system, which permitted the hydrogenolysis of the S-S bond in a potential catalyst poisoning molecule; (vi) the preservation of the metallic Pd surface of the catalyst by saturation of the reaction mixture with hydrogen, resulting in a high H-2/substrate ratio, increased the aldehyde yield in the hydrogenation of 4-chloro-butyric-acid-chloride by avoiding the unwanted poisoning effect of the hydrochloric acid. In the present article, these problems and their solutions, as they emerged during the scale-up of the processes, will be discussed in detail.
机译:通过液相Pd / C介导的加氢工艺扩大规模和生产中间体或前体药物的实用解决方案可能引起广泛关注,即使由于专利法的规定它们不是先前发表的研究重点,也应引起广泛关注。实际的障碍是持久存在的,并且已为人所知很长时间,但大部分仍未公布。促成成功扩大药物生产氢化规模的最重要发现和解决方案如下:(i)Pd / C催化剂被Fe2 +离子中毒以选择性氢化2,6-二甲基-1-亚硝基哌啶得到相应的化合物; (ii)将沉积的Pd金属与Cu合金化以将芳族酰氯转化为相应的醛; (iii)将反应混合物的pH值改变为碱性值,以增强对乙酰氨基酚氢化的立体选择性; (iv)对催化剂制备方法的有用修改,即催化剂的酸化导致苄基OH在含碱性N原子的分子中氢解; (v)使用两个液相,一共是四相系统,这允许潜在的催化剂中毒分子中的S-S键发生氢解; (vi)通过使反应混合物用氢饱和来保持催化剂的金属Pd表面,导致高的H-2 /底物比,增加了4-氯丁酸-氯化物加氢中的醛产率。通过避免盐酸的有害中毒作用。在本文中,将详细讨论这些问题及其解决方案,这些问题及其解决方案是在流程规模扩大期间出现的。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号