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    • 2. 发明公开
    • ACETIC ACID PRODUCTION PROCESS
    • VERFAHREN ZUR HERSTELLUNG VONESSIGSÄURE
    • EP3110785A1
    • 2017-01-04
    • EP15755596.2
    • 2015-02-24
    • LyondellBasell Acetyls, LLC
    • HALLINAN, NoelSALISBURY, Brian A.WHITE, Daniel F.RAMAGE, David L.
    • C07C51/15C07C53/08C07C51/573
    • Processes for producing acetic acid and determining corrosion therein are described herein. The processes generally include contacting methanol and carbon monoxide in the presence of a liquid reaction medium under carbonylation conditions sufficient to form acetic acid, wherein the liquid reaction medium includes: a carbonylation catalyst selected from rhodium catalysts, iridium catalysts and palladium catalysts; from 1 wt. % to 14 wt. % water; and one or more, in-situ generated derivatives of the one or more additives and combinations thereof; wherein the one or more additives are independently selected from non-benzoyl containing pentavalent phosphine oxides, compound mixtures of at least four phosphine oxides and pentavalent aryl or alkaryl phosphine oxides including one or more benzoyl groups; and recovering acetic acid from the process.
    • 本文描述了生产乙酸和确定腐蚀的方法。 该方法通常包括在足以形成乙酸的羰基化条件下在液体反应介质存在下使甲醇和一氧化碳接触,其中液体反应介质包括:选自铑催化剂,铱催化剂和钯催化剂的羰基化催化剂; 从1重量% %至14重量% % 水; 和一种或多种原位产生的一种或多种添加剂及其组合的衍生物; 其中所述一种或多种添加剂独立地选自非苯甲酰基的五价氧化膦,至少四种氧化膦的化合物混合物和包括一个或多个苯甲酰基的五价芳基或烷芳基氧化膦; 并从该方法回收乙酸。
    • 4. 发明公开
    • IMPROVED WATER CONTROL IN ACETIC ACID PRODUCTION PROCESSES
    • 改进醋酸生产过程中的水质控制
    • EP3230251A1
    • 2017-10-18
    • EP15820937.9
    • 2015-12-10
    • LyondellBasell Acetyls, LLC
    • HALLINAN, Noel C.HEARN, John D.RAMAGE, David L.SALISBURY, Brian A.WHITE, Daniel F.
    • C07C51/12C07C51/44C07C51/48C07C51/50
    • C07C51/12C07C51/44C07C51/48C07C51/50C07C53/08
    • Processes for producing acetic acid are presented herein. One or more embodiments include processes for controlling downstream water concentration in acetic acid production process including contacting methanol and carbon monoxide in the presence of a reaction medium under carbonylation conditions sufficient to form a carbonylation product including acetic acid, wherein the reaction medium includes a carbonylation catalyst, water in an upstream water concentration of from 1 wt. % to 14 wt. % water, and a tertiary phosphine oxide; recovering acetic acid from the carbonylation product; and controlling a downstream water concentration by determining a target water concentration and introducing the tertiary phosphine oxide to the reaction medium at a rate, basicity, concentration or combination thereof sufficient to provide a downstream water concentration within 1 wt. % of the target water concentration.
    • 本文介绍了生产乙酸的方法。 一个或多个实施方案包括用于控制乙酸生产过程中下游水浓度的过程,包括在足以形成包含乙酸的碳化产物的羰基化条件下,在反应介质存在下使甲醇和一氧化碳接触,其中反应介质包括羰基化催化剂 上游水浓度为1重量%至14重量%水的水和叔膦氧化物; 从羰基化产物中回收乙酸;以及通过确定目标水浓度并以足以提供1wt%下游水浓度的速率,碱度,浓度或其组合来将叔膦氧化物引入反应介质中来控制下游水浓度 。目标水浓度的百分比。