PROCESS AND SYSTEM FOR THE RECOVERY OF GLYOXYLIC ACID

    公开(公告)号:WO2022258732A1

    公开(公告)日:2022-12-15

    申请号:PCT/EP2022/065630

    申请日:2022-06-09

    Abstract: The present invention concerns a process for the recovery and purification of glyoxylic acid from a process stream comprising glyoxylic acid and oxalic acid, wherein the process stream comprising glyoxylic acid and oxalic acid is subjected to a number of alternating separation and dehydration steps. The process comprising the steps of: (i) providing an aqueous solution comprising glyoxylic acid and oxalic acid; (ii) precipitating at least a portion of the oxalic acid using low-temperature crystallization at a temperature of at most 18 °C; (iii) separating the precipitated oxalic acid from the solution to obtain a solution depleted in oxalic acid; (iv) concentrating the solution depleted in oxalic obtained in step (iii) using reverse osmosis; and repeating steps (ii)- (iv) with the concentrated solution obtained in step (iv) until a purified glyoxylic acid stream with a predetermined degree of purity is obtained. The invention also relates to a system for carrying out the process.

    PROCESS OF PREPARATION OF GLYOXYLIC ACID AQUEOUS SOLUTION
    4.
    发明申请
    PROCESS OF PREPARATION OF GLYOXYLIC ACID AQUEOUS SOLUTION 审中-公开
    葡萄糖酸水溶液的制备方法

    公开(公告)号:WO2009092734A1

    公开(公告)日:2009-07-30

    申请号:PCT/EP2009/050661

    申请日:2009-01-21

    CPC classification number: C07C51/27 C07C59/153

    Abstract: The invention relates to a method for preparing an aqueous solution of glyoxylic acid by oxidation of an aqueous solution of glyoxal with oxygen or a gas containing oxygen, in the presence of a catalytic quantity of nitric acid and/or at least one nitrogen oxide, a strong acid not oxidizing glyoxal, and by maintaining conditions satisfying the equation K L a/Q > 10, where K L a is the total volumetric mass transfer coefficient and Q is the heat load liberated by the reaction per mole of glyoxal.

    Abstract translation: 本发明涉及一种在催化量的硝酸和/或至少一种氮氧化物存在下,用氧气或含氧气体氧化乙二醛水溶液来制备乙醛酸水溶液的方法, 强酸不氧化乙二醛,并且通过维持满足方程式KLa / Q> 10的条件,其中KLa是总体积传质系数,Q是通过每摩尔乙二醛反应释放的热负荷。

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