Plasticizer composition comprising di(2-ethylhexyl) terephthalate

    公开(公告)号:US09670128B2

    公开(公告)日:2017-06-06

    申请号:US15041863

    申请日:2016-02-11

    Applicant: BASF SE

    CPC classification number: C07C67/08 C08K5/12 C07C69/82

    Abstract: A method for preparing an aromatic di-ester includes combining an aromatic di-acid and a linear or branched C4-C13 alcohol to form a mixture. The method also includes heating the mixture from a first temperature (T1) to a second temperature (T2) without a catalyst present in the mixture. The method further includes combining a titanium catalyst with the mixture after the mixture is at the second temperature (T2). The method further includes increasing pressure from a first pressure (P1) to a second pressure (P2) after the mixture is at the second temperature (T2). The method further includes increasing the temperature of the mixture from the second temperature (T2) to a third temperature (T3) while maintaining the second pressure (P2).

    Process for preparing cyclohexanepolycarboxylic acid derivatives having a low proportion of by-products
    6.
    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。

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