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Process for the production of acrylic acid or an acrylate

机译:丙烯酸或丙烯酸酯的生产方法

摘要

A process for the production of an acrylate comprising; providing a feed stream comprising acetic acid; providing a second feed stream comprising formaldehyde; contacting the feed streams in the presence of a catalyst and added water at conditions such that reaction occurs; recovering the reaction product; wherein the catalyst is a vanadium-titanium-phosphorous catalyst having a ratio of 1:2:5 respectively; the molar ratio of acetic acid to formaldehyde is from about 1.9:1; and wherein the water concentration is from about 10 to 40 wt% of acetic acid and/or the minimum ratio of water to alkanoic acid is about 0.14:1 on a weight basis. The weight ratio of water to formaldehyde is preferably 1.08:1. The process is preferably carried out at a temperature of from about 300 to 350°C. The vanadium in the catalyst preferably has an average oxidation state of 3.5. The catalyst preferably has an amorphous, mesoporous structure. The added water may be added as part of the acetic acid stream, formaldehyde stream or as a separate feed stream. The process is disclosed to reduce carbon laydown on the catalyst.
机译:一种丙烯酸酯的生产方法,包括:提供包含乙酸的进料流;提供包含甲醛的第二进料流;在催化剂和加水存在的条件下使进料流接触,以使反应发生;回收反应产物;其中催化剂是钒钛磷催化剂,比例分别为1:2:5。乙酸与甲醛的摩尔比为约1.9∶1。且其中水的浓度为乙酸的约10至40wt%和/或水与链烷酸的最小比率为约0.14∶1(以重量计)。水与甲醛的重量比优选为1.08∶1。该方法优选在约300至350℃的温度下进行。催化剂中的钒优选具有3.5的平均氧化态。催化剂优选具有无定形的中孔结构。添加的水可以作为乙酸物流,甲醛物流的一部分或作为单独的进料物流添加。公开了减少碳沉积在催化剂上的方法。

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