首页> 外国专利> SEPARATION OF PYRIDINE OR PYRIDINE DERIVATIVES FROM AQUEOUS SOLUTIONS

SEPARATION OF PYRIDINE OR PYRIDINE DERIVATIVES FROM AQUEOUS SOLUTIONS

机译:从水溶液中分离出吡啶或吡啶衍生物

摘要

PCT No. PCT/FI97/00645 Sec. 371 Date Apr. 26, 1999 Sec. 102(e) Date Apr. 26, 1999 PCT Filed Oct. 24, 1997 PCT Pub. No. WO98/18744 PCT Pub. Date May 7, 1998The present invention relates to a method of continuously separating pyridine or pyridine derivatives from aqueous solutions by extraction, wherein supercritical fluid is employed to extract the pyridine material from liquid media. The method of the invention, in particular, extracts pyridine or pyridine derivatives from aqueous solutions with pressurized carbon dioxide, which is used under pressure, or in the liquid state, or in the near critical state or in the supercritical state. The operating system is a continuously operating extraction system, so that a part, or all, of the pyridine and/or pyridine derivatives are transferred from the aqueous phase to the carbon dioxide phase, and thereafter the aqueous phase and carbon dioxide phase are separated from each other; and the pyridine and/or pyridine derivatives are separated from carbon dioxide; and the extract containing pyridine and/or pyridine derivatives is thereby obtained. Preferred temperatures for the pyridine and/or pyridine derivative contacting with carbon dioxide are from 5 to 80 DEG C.; and preferred pressures range from 60 to 300 bar. Specific pyridine derivatives which are usefully separated comprise alkylpyridine, vinylpyridine or halopyridine. In the operating system according to the invention the carbon dioxide is preferentially recycled back to the extraction system in a preferred embodiment.
机译:PCT号PCT / FI97 / 00645第二部分371日期1999年4月26日102(e),1999年4月26日,PCT,1997年10月24日提交,PCT Pub。 WO98 / 18744 PCT公布1998年5月7日,本发明涉及一种通过萃取从水溶液中连续分离吡啶或吡啶衍生物的方法,其中采用超临界流体从液体介质中萃取吡啶材料。本发明的方法特别是用加压的二氧化碳从水溶液中提取吡啶或吡啶衍生物,所述二氧化碳在压力下,或以液态,或以近临界态或以超临界态使用。操作系统是连续操作的萃取系统,因此将部分或全部吡啶和/或吡啶衍生物从水相转移到二氧化碳相,然后将水相和二氧化碳相从彼此;吡啶和/或吡啶衍生物与二氧化碳分离;得到含有吡啶和/或吡啶衍生物的提取物。吡啶和/或吡啶衍生物与二氧化碳接触的优选温度为5至80℃。优选的压力范围为60至300 bar。有效分离的特定吡啶衍生物包括烷基吡啶,乙烯基吡啶或氯吡啶。在一个优选的实施方案中,在根据本发明的操作系统中,优选将二氧化碳再循环回萃取系统。

著录项

  • 公开/公告号EP1019341A1

    专利类型

  • 公开/公告日2000-07-19

    原文格式PDF

  • 申请/专利权人 VALTION TEKNILLINEN TUTKIMUSKESKUS;

    申请/专利号EP19970910469

  • 发明设计人 LAITINEN ANTERO;MAUKONEN MARKO;

    申请日1997-10-24

  • 分类号C07B63/04;C07D213/00;B01D11/04;C02F1/26;

  • 国家 EP

  • 入库时间 2022-08-22 01:47:10

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