Process for preparing cyclohexanepolycarboxylic acid derivatives having a low proportion of by-products
    14.
    发明授权
    Process for preparing cyclohexanepolycarboxylic acid derivatives having a low proportion of by-products 有权
    具有低比例副产物的环己烷多羧酸衍生物的方法

    公开(公告)号:US09090553B2

    公开(公告)日:2015-07-28

    申请号:US14045178

    申请日:2013-10-03

    Applicant: BASF SE

    CPC classification number: C07C51/36 C07C61/09 C07C67/303 C07C2601/14 C07C69/75

    Abstract: The present invention relates to a process for preparing at least one cyclohexanepolycarboxylic acid or a derivative thereof by bringing at least one corresponding benzenepolycarboxylic acid or a derivative thereof into contact with a hydrogen-comprising gas in the presence of at least one coated catalyst comprising an active metal selected from the group consisting of ruthenium, rhodium, palladium, platinum and mixes thereof, applied to a support material comprising silicon dioxide, where the pore volume of the support material is from 0.6 to 1.0 ml/g, determined by Hg porosimetry, the BET surface area is from 280 to 500 m2/g, at least 90% of the pores present have a diameter of from 6 to 12 nm, and from 40 to 70% by weight of the active metal, based on the total amount of the active metal, are present in the catalyst coating up to a penetration depth of 200 μm, wherein the contacting is carried out at a superficial velocity of not more than 50 m/h.

    Abstract translation: 本发明涉及一种制备至少一种环己烷多羧酸或其衍生物的方法,该方法是使至少一种相应的苯多元羧酸或其衍生物与含氢气体在至少一种包含活性物质的涂层催化剂存在下接触 选自钌,铑,钯,铂及其混合物的金属,施加到包含二氧化硅的载体材料上,其中载体材料的孔体积为0.6至1.0ml / g,通过Hg孔隙率法测定, BET表面积为280〜500m2 / g,至少90%的孔具有6〜12nm的直径和40〜70重量%的活性金属,基于 活性金属存在于催化剂涂层中,直到穿透深度为200μm,其中接触以不大于50m / h的表观速度进行。

    HYDROCARBON CONVERSION PROCESS IN THE PRESENCE OF AN ACIDIC IONIC LIQUID WITH UPSTREAM HYDROGENATION
    16.
    发明申请
    HYDROCARBON CONVERSION PROCESS IN THE PRESENCE OF AN ACIDIC IONIC LIQUID WITH UPSTREAM HYDROGENATION 审中-公开
    酸性离子液体与上海氢化氢存在时的碳氢转化过程

    公开(公告)号:US20140128648A1

    公开(公告)日:2014-05-08

    申请号:US14053672

    申请日:2013-10-15

    Applicant: BASF SE

    CPC classification number: C07C5/13 C07C5/10 C07C5/29 C07C2527/125 C07C13/18

    Abstract: The present invention relates to a process for hydrocarbon conversion in the presence of an acidic ionic liquid. The hydrocarbon conversion is preferably an isomerization, especially an isomerization of methylcyclopentane (MOP) to cyclohexane. Prior to the hydrocarbon conversion, a hydrogenation is performed, preference being given to hydrogenating benzene to cyclohexane. The cyclohexane obtained in the hydrogenation and/or isomerization is preferably isolated from the process. In a preferred embodiment of the present invention, the hydrogenation is followed and the hydrocarbon conversion, especially the isomerization, is preceded by distillative removal of low boilers, especially C5-C6-alkanes such as cyclopentane or isohexanes, from the hydrocarbon mixture used for hydrocarbon conversion.

    Abstract translation: 本发明涉及在酸性离子液体存在下烃转化的方法。 烃转化率优选为异构化,特别是甲基环戊烷(MOP)异构化为环己烷。 在烃转化之前,进行氢化,优选将苯氢化成环己烷。 在氢化和/或异构化中获得的环己烷优选与该方法分离。 在本发明的一个优选实施方案中,遵循氢化并且烃转化,特别是异构化之前是从用于烃的烃混合物中蒸馏除去低锅炉,特别是C 5 -C 6烷烃如环戊烷或异己烷 转换。

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