Process for producing hydrogenated aromatic polycarboxylic acid
    2.
    发明授权
    Process for producing hydrogenated aromatic polycarboxylic acid 有权
    氢化芳族聚羧酸的制备方法

    公开(公告)号:US08846973B2

    公开(公告)日:2014-09-30

    申请号:US13055247

    申请日:2009-07-21

    申请人: Tomohiro Sugawara

    发明人: Tomohiro Sugawara

    IPC分类号: C07C51/36 C07C61/09 C07C61/08

    摘要: A production method of a hydrogenated product of aromatic polycarboxylic acid by the hydrogenation of aromatic ring of the aromatic polycarboxylic acid in the presence of a catalyst composed of rhodium in combination with palladium and/or platinum supported on a carbon support. By using the catalyst, the hydrogenated product of aromatic polycarboxylic acid is produced industrially advantageously in high purity and high yield. By activating the catalyst composed of rhodium in combination with palladium and/or platinum supported on the carbon support after the hydrogenation, the conversion to the hydrogenated product of aromatic polycarboxylic acid is maintained at nearly 100% even after repeatedly using the catalyst many times. Also, a hydrogenated product of aromatic polycarboxylic acid substantially free from the starting aromatic polycarboxylic acid is obtained.

    摘要翻译: 芳族多元羧酸的氢化产物的制备方法,其通过在由铑组成的催化剂与负载在碳载体上的钯和/或铂组合的催化剂存在下芳香族多元羧酸的芳香环进行氢化。 通过使用催化剂,芳族多元羧酸的氢化产物在工业上以高纯度和高收率有利地产生。 通过在氢化后将由铑组成的催化剂与负载在碳载体上的钯和/或铂一起活化,即使在多次反复使用催化剂之后,芳族多元羧酸的氢化产物的转化也保持接近100%。 另外,得到基本上不含起始芳香族多元羧酸的芳香族多元羧酸的氢化物。

    PROCESS FOR PREPARING CYCLOHEXANEPOLYCARBOXYLIC ACID DERIVATIVES HAVING A LOW PROPORTION OF BY-PRODUCTS
    3.
    发明申请
    PROCESS FOR PREPARING CYCLOHEXANEPOLYCARBOXYLIC ACID DERIVATIVES HAVING A LOW PROPORTION OF BY-PRODUCTS 有权
    制备具有较低比例的副产物的环己烷羧酸羧酸衍生物的方法

    公开(公告)号:US20140100387A1

    公开(公告)日:2014-04-10

    申请号:US14045178

    申请日:2013-10-03

    申请人: BASF SE

    IPC分类号: C07C51/36 C07C61/09

    摘要: 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.

    摘要翻译: 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。

    Method for hydrogenating benzene polycarboxylic acids or derivatives thereof by using a catalyst containing macropores

    公开(公告)号:US06284917B1

    公开(公告)日:2001-09-04

    申请号:US09581843

    申请日:2000-06-19

    IPC分类号: C07C6974

    摘要: A process for hydrogenating a benzenepolycarboxylic acid or a derivative thereof or a mixture of two or more thereof by bringing the benzenepolycarboxylic acid or the derivative thereof or the mixture of two or more thereof into contact with a hydrogen-containing gas is carried out in the presence of a catalyst which comprises as active metal at least one metal of transition group VIII of the Periodic Table alone or together with at least one metal of transition group I or VII of the periodic table applied to a support which contains macropores with the proviso that if dimethyl terephthalate is hydrogenated, the hydrogenation using a catalyst which comprises as active metal ruthenium either alone or together with at least one metal of transition group I, VII or VIII of the Periodic Table applied to a support, where the support has a mean pore diameter of at least 50 nm and a BET surface area of at most 30 m2/g and the amount of the active metal is from 0.01 to 30% by weight, based on the total weight of the catalyst, and the ratio of the surface areas of the active metal and the catalyst support is less than 0.05, and/or a catalyst which comprises as active metal ruthenium either alone or together with at least one metal of transition group I, VII or VIII of the Periodic Table in an amount of from 0.01 to 30% by weight, based on the total weight of the catalyst, applied to a support, where from 10 to 50% of the pore volume of the support is formed by macropores having a pore diameter in the range from 50 nm to 10,000 nm and from 50 to 90% of the pore volume of the support is formed by mesopores having a pore diameter in the range from 2 to 50 nm, where the sum of the pore volumes adds up to 100%, is excluded, and novel hydrogenation products, obtainable by hydrogenating benzenepolycarboxylic acid (derivatives) as well as their use as plasticizers in plastics.