PRODUCTION OF PHTHALIC ANHYDRIDE BY GAS PHASE OXIDATION OF o-XYLOL IN A PRIMARY AND A SECONDARY REACTOR
    3.
    发明申请
    PRODUCTION OF PHTHALIC ANHYDRIDE BY GAS PHASE OXIDATION OF o-XYLOL IN A PRIMARY AND A SECONDARY REACTOR 审中-公开
    制备通过邻二甲苯的气相氧化邻苯二甲酸酐IN头部和Nachreaktor

    公开(公告)号:WO2007135102A2

    公开(公告)日:2007-11-29

    申请号:PCT/EP2007054839

    申请日:2007-05-18

    CPC classification number: C07D307/89 C07C51/265 C07C63/16

    Abstract: The invention relates to a method for producing phthalic anhydride by catalytic gas phase oxidation of o-xylol. According to said method, a gaseous mixture of o-xylol and an oxygen-containing gas is reacted in a primary reactor to give a gaseous intermediate reaction product which contains unreacted o-xylol, phthalic anhydride reaction products with a lower oxidation state and phthalic anhydride, the reaction heat produced in the primary reactor being at least partially carried off by indirect cooling with a heat exchange medium, and introducing the intermediate reaction product to a secondary reactor. The concentration of the unreacted o-xylol in the intermediate reaction product is at least 1% by weight, and the sum of the concentrations of phthalic anhydride of the lower oxidation state in the intermediate reaction product is at least 0.5% by weight. The method according to the invention allows an increase in total yield of phthalic anhydride without any or without substantial decrease in product quality.

    Abstract translation: 公开了一种用于由邻二甲苯,其包含邻二甲苯的含氧气体中的主反应器中的气体混合物,并以气态中间反应产物,其包含未转化的邻二甲苯,邻苯二甲酸酐欠氧化产物反应的催化气相氧化制备邻苯二甲酸酐的方法 和邻苯二甲酸酐,所述一个至少部分地耗散由间接冷却用载热介质,并导入中间反应产物分离成二级反应器在主反应器的反应热产生的热。 未反应的邻二甲苯中的中间反应产物中的浓度为至少1重量%,邻苯二甲酸酐产品欠氧化浓度的在中间反应产物中的总和为至少0.5重量%。 该方法允许增加邻苯二甲酸酐的总产没有或没有在产品质量上显著恶化。

    8.
    发明专利
    未知

    公开(公告)号:DE50008266D1

    公开(公告)日:2004-11-18

    申请号:DE50008266

    申请日:2000-10-31

    Applicant: BASF AG

    Abstract: In a process for the two-stage catalytic gas-phase oxidation of propene to acrylic acid, the reaction gas starting mixture is passed, in a tube-bundle reactor, with a propene loading of >=160 l (S.T.P.) of propene/l.h, first over a fixed catalyst bed 1 present in two successive temperature zones A, B and then over a fixed catalyst bed 2 which is housed either in one further temperature zone C or in two further temperature zones D, E, the temperature of the zone A being kept at a lower temperature than the zone B and the temperature of the zone D at a lower temperature than the zone E.

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