首页> 外国专利> Process for dehydrating unsaturated aldehydes and the resulting unsaturated aldehydes

Process for dehydrating unsaturated aldehydes and the resulting unsaturated aldehydes

机译:脱水不饱和醛及所得不饱和醛的方法

摘要

An a , b unsaturated C3 or C4 aldehyde such as acrolein or 2-methylacrolein, which during manufacture or treatment comes into contact with water, is dehydrated by mixing with a liquid hydrocarbon before, during or after the water-contacting stage, a liquid aqueous phase practically free from unsaturated aldehyde being separated in a further stage from a liquid phase containing the hydrocarbon and substantially all the unsaturated aldehyde and of lower water content than the aldehyde-water azeotrope. If the boiling points are sufficiently apart, the hydrocarbon and aldehyde may be separated by distillation. Water may be removed from the hydrocarbon solution of aldehyde by a dehydrating agent or by distilling to give a bottoms containing hydrocarbon, most of the aldehyde, and practically no water, and a distillate of aldehyde and water which may be returned to a stage prior to separation of the liquid aqueous phase. The hydrocarbon may be aromatic, paraffinic, olefinic, cycloparaffinic or cyclo-olefinic, e.g. xylene, propane or butane. The amount added is preferably 5-10 vols. per vol. of the aldehyde. Saturated aldehydes and ketones are separated in the aqueous phase. Stratification is preferably effected at 0-20 DEG C. Extraction may be effected by flowing water and hydrocarbon in counter-current to each other through a vessel and feeding crude unsaturated aldehyde, e.g. containing saturated carboxylic compounds, at an intermediate point. The water should generally be added in an amount at least twice that of the hydrocarbon. The ratio of water to hydrocarbon may be greater in the upper part of the column, e.g. above 1, and lower in the lower part. e.g. less than 1. This may be effected by taking off a mixture, for example, just above the crude aldehyde inlet, fractionating it, separating into two phases with a hydrocarbon, and returning at suitable places. In examples, xylene and a paraffinic fraction are the hydrocarbon solvents; acrolein-water azeotrope, acrolein and 2-methylacrolein mixtures with propionaldehyde, acetaldehyde, isobutyraldehyde, and acetone the mixtures treated. A preliminary separation by distillation may be used.
机译:在制造或处理过程中与水接触的a,b不饱和C3或C4醛(如丙烯醛或2-甲基丙烯醛)在与水接触之前,之中或之后,通过与液态烃混合来脱水在几乎不包含不饱和醛的另一相中,将其进一步从含有烃和基本上所有不饱和醛且水含量低于醛-水共沸物的液相中分离出来。如果沸点充分分开,则烃和醛可以通过蒸馏分离。可以通过脱水剂或通过蒸馏以得到包含烃,大部分醛且实际上不含水的塔底馏分的醛的水从醛的烃溶液中除去,并且可以将醛和水的馏出物返回至之前的阶段。分离液体水相。烃可以是芳族的,链烷烃的,烯烃的,环烷烃的或环烯烃的,例如烃。二甲苯,丙烷或丁烷。添加的量优选为5-10体积。每卷醛。在水相中分离饱和的醛和酮。分层优选在0-20℃下进行。萃取可以通过使水和烃彼此逆流通过容器并进料粗的不饱和醛,例如丙烯醛来进行。在中间点含有饱和的羧酸化合物。通常应以至少两倍于烃的量添加水。在塔的上部,例如,水与烃的比例可以更大。 1以上,下部较低。例如小于1。这可以通过例如在粗醛入口正上方取出混合物,将其分馏,与烃分离成两相并在合适的位置返回而实现。在实施例中,二甲苯和链烷烃馏分是烃溶剂。丙烯醛-水共沸物,丙烯醛和2-甲基丙烯醛混合物与丙醛,乙醛,异丁醛和丙酮的混合物。可以使用通过蒸馏的初步分离。

著录项

  • 公开/公告号GB675544A

    专利类型

  • 公开/公告日1952-07-09

    原文格式PDF

  • 申请/专利号GB19500007867

  • 发明设计人

    申请日1950-03-29

  • 分类号C07C45/78;C07C45/80;

  • 国家 GB

  • 入库时间 2022-08-24 01:00:53

相似文献

  • 专利
  • 外文文献
  • 中文文献
获取专利

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