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    • 10. 发明公开
    • CYCLOHEXANONE PRODUCTION PROCESS WITH MODIFIED POST-DISTILLATION
    • Herstellungsverfahren von Cyclohexanon mit modifizierter Post-Destillation
    • EP2234952A1
    • 2010-10-06
    • EP08864701.1
    • 2008-12-16
    • DSM IP Assets B.V.
    • HORSELS, MarleenPARTON, Rudy Francois Maria JozefTINGE, Johan Thomas
    • C07C45/82C07C49/403B01J10/00C07C29/48C07C45/00C07C45/29C07C51/00C07C55/14C07C35/08C08F232/00
    • C07C29/50C07C45/006C07C45/82C07C51/00C07C2601/14C07C49/403C07C55/14C07C35/08
    • The present invention relates to a method for continuously preparing cyclohexanone from phenol making use of a catalyst comprising at least one catalytically active metal selected from platinum and palladium comprising a) hydrogenating phenol to form a product stream comprising cyclohexanone and unreacted phenol; b) separating at least part of the product stream, or at least part of the product stream from which one or more components having a lower boiling point than cyclohexanone have been removed, into a first fraction comprising cyclohexanone and a second fraction comprising phenol and cyclohexanol, using distillation; c) separating the second fraction into a third fraction, rich in cyclohexanol, and a fourth fraction, rich in phenol and, using distillation; d) subjecting at least part of the fourth fraction to a further distillation step, thereby forming a fifth fraction and a sixth fraction, wherein the fifth fraction is enriched in phenol compared to the sixth fraction, and wherein the sixth fraction comprises side-products having a higher boiling point than phenol, and phenol, wherein step d) is carried out in a vacuum distillation column equipped with trays in the lower part of the column, and wherein in the upper part of the column, i.e. in the part above the feed inlet, packing material is present instead of trays in at least part of said upper part, which packing material has a comparable or improved separating efficiency, and provides a reduction of the pressure drop by at least 30%, preferably more than 50%, as compared to the case with trays in the upper part, under otherwise similar distillation conditions.
    • 从苯酚连续制备环己酮的方法使用具有至少一种选自铂和钯的催化活性金属的催化剂。 该方法包括与后续馏分相比富集蒸馏馏分中的苯酚,其中后续馏分包括苯酚和沸点高于苯酚的副产物。 蒸馏在塔底部装有塔板的真空蒸馏塔中进行。 在塔的上部,即在进料入口上方的部分,在其至少一部分中存在填料材料代替塔盘。 包装材料具有相当或改进的分离效率,并且与其他类似的蒸馏条件下的上部塔板的情况相比,压降降低至少30%,优选大于50%。