首页> 外国专利> Catalyst activity control in process for converting an alkene to a carbonyl derivative in the presence of a noble metal and redox agent

Catalyst activity control in process for converting an alkene to a carbonyl derivative in the presence of a noble metal and redox agent

机译:在贵金属和氧化还原剂存在下将烯烃转化为羰基衍生物的方法中的催化剂活性控制

摘要

In converting an alkene such as ethylene to a carbonyl derivative such as acetaldehyde by a process which comprises passing the alkene through a tubular reactor along with an aqueous acidic catalyst solution comprising a noble metal such as palladium together with a cupric chloride redox agent, followed by separating the carbonyl product from the depleted catalyst solution which is then reoxidized with a source of molecular oxygen such as air prior to being returned to the reactor, continuous depletion of the chloride content of the catalyst solution takes place as a result of the formation of chlorinated reaction by-products. This necessitates replenishment of the chloride content of the catalyst solution by adding hydrochloric acid into a catalyst regeneration zone preceding the catalyst reoxidation step of the process. Over-treating or under-treating with the hydrochloric acid results, however, in occasional process upsets and failure to maintain optimal activity of the catalyst solution and maximum reactor output. The present invention comprises maintaining optimal catalyst activity by adding hydrochloric acid in response to the hydraulic pressure gradient obtaining within the alkene- oxidation reactor, within which a deficiency of acid causes an increasing hydraulic pressure gradient due to fouling of the tubular reactor with precipitated solids. Optimal catalyst activity obtains when the acid addition rate is just sufficient to prevent the inception of a pressure gradient rise due to precipitation of solids within the reactor.
机译:在通过如下方法将烯烃如乙烯转化为羰基衍生物如乙醛的过程中,该方法包括使烯烃与包含贵金属如钯和氯化铜氧化还原剂的酸性催化剂水溶液一起通过管式反应器,然后从贫化的催化剂溶液中分离出羰基产物,然后在返回到反应器之前用分子氧源(例如空气)再氧​​化,然后由于形成氯化物而持续耗尽催化剂溶液中的氯化物反应副产物。这需要通过在该方法的催化剂再氧化步骤之前将盐酸添加到催化剂再生区中来补充催化剂溶液中的氯化物含量。但是,用盐酸进行过分处理或过分处理会导致过程偶尔发生故障,并且无法保持催化剂溶液的最佳活性和最大反应器产量。本发明包括响应于在烯烃氧化反应器内获得的水压梯度,通过添加盐酸来维持最佳的催化剂活性,其中由于管式反应器结垢的固体结垢,酸的缺乏导致水压梯度的增加。当酸的添加速率刚好足以防止由于反应器内的固体沉淀而导致压力梯度升高开始时,可​​获得最佳的催化剂活性。

著录项

  • 公开/公告号US3972946A

    专利类型

  • 公开/公告日1976-08-03

    原文格式PDF

  • 申请/专利权人 CELANESE CORPORATION;

    申请/专利号US19710182774

  • 发明设计人 SHINYA OCHIAI;LEONARD GRIFFITH;

    申请日1971-09-22

  • 分类号C07C45/02;

  • 国家 US

  • 入库时间 2022-08-23 01:30:24

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