首页> 外国专利> USE OF CHEMICAL REACTION TO SEPARATE ETHYLENE FROM ETHANE IN ETHANE-BASED PROCESSES TO PRODUCE ACETIC ACID

USE OF CHEMICAL REACTION TO SEPARATE ETHYLENE FROM ETHANE IN ETHANE-BASED PROCESSES TO PRODUCE ACETIC ACID

机译:在基于乙烷的过程中使用化学反应从乙烷中分离出乙烯来生产乙酸

摘要

Described herein is a process in which acetic acid is produced by ethaneoxidation. One byproduct of the ethane oxidation is ethylene. High ethylenecontent in the recycle gas stream will lead to poor efficiencies and higherlosses to the COx byproduct in the acetic acid reactor. In fact, ethylene inthe recycle feed competes with the ethane for the limited amount of oxygenfeed, resulting in higher inefficiencies to carbon oxides than straight ethaneoxidation. Ethylene is removed in this process by a further oxidation reactionat a temperature low enough such that ethane is not reactive, but the ethyleneis converted to acetic acid. Either the ethane oxidation reactor effluent or aportion or all of the recycle stream to the ethane oxidation reactor, or anycombination of the same, can be processed in this manner to reduce theethylene content of those streams.
机译:本文描述的是其中通过乙烷生产乙酸的方法氧化。乙烷氧化的一种副产物是乙烯。高乙烯循环气流中的杂质含量会导致效率低下和更高乙酸反应器中COx副产物的损失。实际上,乙烯在循环进料与乙烷竞争有限的氧气量进料,导致碳氧化物的效率比纯乙烷高氧化。在此过程中,乙烯通过进一步的氧化反应被去除在足够低的温度下使乙烷不发生反应,但乙烯转化为乙酸。乙烷氧化反应器的流出物或进入乙烷氧化反应器的部分或全部循环物流,或任何相同的组合,可以这种方式进行处理以减少这些物流中的乙烯含量。

著录项

  • 公开/公告号CA2640631C

    专利类型

  • 公开/公告日2014-11-18

    原文格式PDF

  • 申请/专利权人 CELANESE INTERNATIONAL CORPORATION;

    申请/专利号CA20072640631

  • 发明设计人 RYAN DEBRA ANN;FOSTER JAMES A.;

    申请日2007-01-30

  • 分类号C07C51/16;C07C51/25;B01J27/198;C07C53/08;

  • 国家 CA

  • 入库时间 2022-08-21 15:11:40

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