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CONTINUOUS PROCESS FOR THE PREPARATION OF MALEIC ANHYDRIDE FROM AN AQUEOUS SOLUTION OF MALEIC ACID BY DISTILLATION

机译:蒸馏法从马来酸水溶液中制备马来酸酐的连续过程

摘要

Maleic anhydride of at least 99% by weight purity and containing 0-0À1% by weight of fumaric acid is prepared in a continuous process from an aqueous solution of maleic acid by: (a) Heating the maleic acid solution in a concentration zone at a temperature of between 100 and 150 C. and at a pressure of between 400 and 760 mm. Hg until the water content of the maleic acid is reduced to 0-10% by weight (b) Treating the maleic acid obtained in stage (a) in a conversion zone at a temperature of between 150 and 200 C. and at a pressure of between 40 and 300 mm. Hg until from 10 to 97% by weight of the maleic acid is converted into maleic anhydride, to give a liquid phase of impure maleic acid and a purified gaseous phase containing maleic anhydride and water vapour (c) Treating the impure liquid phase produced in stage (b) with an aqueous solution of maleic acid in a dissolution and filtration zone to provide a solid residue containing the impurities and any fumaric acid which may have been formed, which is removed from the system, and a filtrate consisting of an aqueous solution of purified maleic acid, which is either recycled partly to stage (a) and partly to the impure liquid phase produced in stage (b) or is removed from the system (d) Condensing in a condensation zone the gaseous phase consisting of maleic anhydride and water vapour produced in stage (b) at a temperature higher than the dewpoint of the water vapour present in the gaseous phase, thus obtaining maleic anhydride of the desired purity washing the residual vapour with water and returning, if desired, to stage (a) the solution thus obtained containing maleic acid. The temperature employed in step (a) is preferably 135 C. and pressure 500 mm. Hg. The maleic acid solution used as starting material may be obtained by washing the effluent of a catalytic oxidation reactor for hydrocarbons, such as benzene, with or without the previous condensation of part of the maleic anhydride.
机译:由马来酸水溶液通过以下连续方法制备纯度至少为99%(重量),含量为0-0-1%(重量)富马酸的马来酸酐:温度在100至150摄氏度之间,压力在400至760毫米之间。汞直至马来酸的水含量降低到0-10%(重量)为止。(b)在转化区中,在150-200℃的温度和200℃的压力下处理步骤(a)中获得的马来酸。 40至300毫米之间。 Hg直至马来酸的10-97%(重量)转化为马来酸酐,得到不纯的马来酸液相和含有马来酸酐和水蒸气的纯净气相(c)处理阶段中产生的不纯液相(b)在溶解和过滤区中用马来酸水溶液提供固体残留物,该固体残留物含有杂质和可能形成的富马酸,将其从系统中除去,以及由以下物质组成的滤液:纯化的马来酸,可部分循环到阶段(a),部分循环到阶段(b)中产生的不纯液相,或从系统(d)中除去。在冷凝区中冷凝由马来酸酐和水组成的气相步骤(b)中产生的蒸汽的温度高于气相中存在的水蒸汽的露点,因此获得所需纯度的马来酸酐,用水洗涤残留的蒸汽如果需要,将其返回到阶段(a),从而获得的含有马来酸的溶液。步骤(a)中采用的温度优选为135℃,压力为500mm。汞用作原料的马来酸溶液可通过洗涤催化氧化反应器的烃,如苯,在有或没有部分马来酸酐预先缩合的情况下获得。

著录项

  • 公开/公告号ES375942A1

    专利类型

  • 公开/公告日1972-04-16

    原文格式PDF

  • 申请/专利号ES19700375942

  • 发明设计人

    申请日1970-01-27

  • 分类号C07C;

  • 国家 ES

  • 入库时间 2022-08-23 08:47:00

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