首页> 外国专利> CATALYST SYSTEM AND PROCESS FOR THE PRODUCTION OF ACETIC ACID BY CATALYTIC REARRANGEMENT OF FORMIC ACID METHYL ESTER

CATALYST SYSTEM AND PROCESS FOR THE PRODUCTION OF ACETIC ACID BY CATALYTIC REARRANGEMENT OF FORMIC ACID METHYL ESTER

机译:甲酸甲酯催化重整制取乙酸的催化剂体系及工艺

摘要

1. A process for the production of acetic acid by catalytic rearrangement of methyl formate at elevated temperature and elevated pressure in the presence of a metal catalyst, a halogen promoter and carbon monoxide, characterised in that the reaction is carried out in the liquid phase at a temperature of 140 to 300 degrees C and a CO partial pressure of 2 to 250 bar at the reaction temperature by means of a metal catalyst system comprising rhodium, a rhodium salt or a rhodium complex and at least one metal compound of Group VI B in the presence of a halogen promoter but in the absence of ligands of Group V A, the rhodium compound being supplied in an amount of 0.05 to 5 mg atom of rhodium per mole of methyl formate supplied and at an atomic ratio of rhodium : Group VI B metal of 1 : 100 to 10 : 1 and an atomic ratio of rhodium : halogen of 1 : 1000 to 1 : 1.
机译:1.一种通过在金属催化剂,卤素促进剂和一氧化碳的存在下在高温和高压下将甲酸甲酯催化重排而制备乙酸的方法,其特征在于,所述反应在液相中于200℃进行。借助于包括铑,铑盐或铑配合物和至少一种VI B族金属化合物的金属催化剂体系,在反应温度下在140至300℃的温度和2至250巴的CO分压下进行反应。存在卤素促进剂但不存在第VA组配体的情况下,所提供的铑化合物的量为每摩尔所提供的甲酸甲酯0.05至5毫克原子的铑,且铑的原子比为:VI B族金属原子比为1:100至10:1,铑:卤素的原子比为1:1000至1:1。

著录项

  • 公开/公告号PH19591A

    专利类型

  • 公开/公告日1986-05-26

    原文格式PDF

  • 申请/专利权人 BUB GUENTHER;HOG HANS ULRICH;

    申请/专利号PH19830029510

  • 发明设计人 DR.HANS-ULRICH HOG;DR.GUNTHER BUB;

    申请日1983-09-08

  • 分类号C07C51/00;C07C51/10;

  • 国家 PH

  • 入库时间 2022-08-22 07:40:02

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