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ACETIC ACID PRODUCTION PROCESS VIA IRIDIUM-CATALYZED CARBONYLATION

机译:通过铱催化的羰基化生产乙酸

摘要

FIELD: industrial inorganic synthesis.;SUBSTANCE: process is accomplished by continuously feeding methanol and/or reactive derivative thereof and carbon monoxide into carbonylation reactor filled with reaction mixture containing iridium carbonylation catalyst, methyl iodide cocatalyst, water in limited concentration, acetic acid, and methyl acetate, liquid reaction mixture further including at least one promoter selected from ruthenium, osmium, rhenium, and tungsten. Carbonylation of methanol to produce acetic acid involves reaction with carbon monoxide in liquid reaction mixture. When recovering acetic acid from liquid reaction mixture, concentration of water is maintained therein not exceeding 4.5%. During reaction, partial pressure of carbon monoxide in reactor is maintained within a range between 0 and 6 bar.;EFFECT: accelerated carbonylation reaction, diminished by-product formation, and simplified acetic acid recovery operation.;6 dwg, 3 tbl
机译:领域:工业无机合成。物质:通过将甲醇和/或其反应性衍生物和一氧化碳连续进料到羰基化反应器中而完成,所述羰基化反应器填充有包含铱羰基化催化剂,甲基碘助催化剂,有限浓度的水,乙酸和乙酸甲酯,液体反应混合物,其还包含至少一种选自钌,,rh和钨的促进剂。甲醇羰基化生产乙酸涉及在液体反应混合物中与一氧化碳反应。当从液体反应混合物中回收乙酸时,其中水的浓度保持不超过4.5%。反应期间,反应器中的一氧化碳分压保持在0至6 bar之间。效果:加速羰基化反应,减少副产物形成,简化了乙酸回收操作; 6 dwg,3 tbl

著录项

  • 公开/公告号RU2245870C2

    专利类型

  • 公开/公告日2005-02-10

    原文格式PDF

  • 申请/专利权人

    申请/专利号RU19970121233

  • 申请日1997-12-19

  • 分类号C07C53/08;C07C51/12;

  • 国家 RU

  • 入库时间 2022-08-21 22:02:10

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