PROCESS FOR CONTINUOUSLY PREPARING DI-C1-3-ALKYL SUCCINATES
    3.
    发明公开
    PROCESS FOR CONTINUOUSLY PREPARING DI-C1-3-ALKYL SUCCINATES 有权
    VERFAHREN ZUR KONTINUIERLICHEN HERSTELLUNG VON DI-C1-3-ALKYLSUCCINATEN

    公开(公告)号:EP3001835A1

    公开(公告)日:2016-04-06

    申请号:EP14722653.4

    申请日:2014-05-07

    Applicant: BASF SE

    CPC classification number: C07C67/08 B01D3/141 C07C67/54 C07C69/40

    Abstract: The invention relates to a process for continuously preparing di-C1-3-alkyl succinates by reacting succinic acid with an C1-3-alkanol in the presence of a fixed-bed heterogeneous acidic esterification catalyst in a tubular reactor at a temperature in the range of from 60 to 100° C., wherein a mixture, comprising succinic acid, C1-3-alkanol, mono-C1-3-alkyl succinate, di-C1-3-alkyl succinate and water, is formed in a mixing stage and fed to the entrance of the tubular reactor, and wherein 5 to 75% of the outlet flow rate of the tubular reactor are recycled directly to the mixing stage as a recycle stream, and the molar ratio of C1-3-alkanol to succinic acid added to the mixing zone, and not including the C1-3-alkanol and succinic acid at the recycle stream, being in the range of from 2.0 to 9.5. The invention furthermore relates to a process for separating the reactor effluent of an esterification of succinic acid with an C1-3-alkanol to give di-C1-3-alkyl succinates by distillation, wherein the separation is performed in a divided wall column in which C1-3-alkanol and water are removed in a top draw of the column, di-C1-3-alkyl succinate is removed in a side draw of the column, and wherein mono-C1-3-alkyl succinate and succinic acid are removed in a bottom draw of the column.

    Abstract translation: 本发明涉及一种在固定床非均相酸性酯化催化剂存在下,在管式反应器中在一定范围内的温度下使琥珀酸与C 1-3烷醇反应连续制备二-C 1-3烷基琥珀酸盐的方法 为60〜100℃,其中在混合阶段形成包含琥珀酸,C 1-3 - 链烷醇,琥珀酸单-C1-烷基酯,琥珀酸二-C1-烷基酯和水的混合物, 进料到管状反应器的入口,其中管式反应器的出口流量的5%至75%作为循环物流直接循环到混合阶段,并且加入了C 3-链烷醇与琥珀酸的摩尔比 到混合区,并且不包括在再循环流中的C 1-3链烷醇和琥珀酸,其范围为2.0-9.5。 本发明还涉及一种将琥珀酸酯化为C 3-链烷醇的反应器流出物分离以通过蒸馏得到二-C1-烷基琥珀酸盐的方法,其中分离是在分隔壁塔中进行的,其中在 在柱的顶部抽出物中除去C 3-链烷醇和水,在柱的侧馏分中除去琥珀酸二-C1--烷基酯,并且其中除去琥珀酸单C 1-3 - 烷基酯和琥珀酸 在列的底部绘制。

    VERFAHREN ZUR GEWINNUNG AROMATISCHER WERTPRODUKTE AUS LIGNINHALTIGEN ZUSAMMENSETZUNGEN

    公开(公告)号:EP3215247A1

    公开(公告)日:2017-09-13

    申请号:EP15790940.9

    申请日:2015-11-06

    Applicant: BASF SE

    CPC classification number: C07C45/79 B01D15/00 C07C47/58

    Abstract: The invention relates to a method for extracting aromatic compounds from aqueous, alkaline compositions containing lignin, which have a pH value of at least pH 10, in particular of at least pH 11, especially of at least pH 12, characterized in that the aqueous, alkaline composition containing lignin is treated with active carbon, the active carbon separates from the aqueous, alkaline composition containing lignin and the active carbon then undergoes a desorption step in order to extract the aromatic compounds, wherein the desorption step comprises the treatment of the active carbon (i) by means of an organic solvent, which essentially consists of one or more aromatic hydrocarbons or a mixture of at least one aromatic hydrocarbon together with at least one C
    1 -C
    4 alkanol, or (ii) by means of water vapor, wherein an eluate is obtained which contains the aromatic compounds.

    Abstract translation: 本发明涉及从含有木质素的含水碱性组合物中提取芳族化合物的方法,所述组合物具有至少pH 10,特别是至少pH 11,特别是至少pH 12的pH值,其特征在于所述含水, 将含有木质素的碱性组合物用活性炭处理,将活性炭与含木质素的含水碱性组合物分离,然后进行解吸步骤以提取芳族化合物,其中解吸步骤包括处理活性炭 (i)借助于基本上由一种或多种芳族烃或至少一种芳族烃与至少一种C 1 -C 4链烷醇的混合物组成的有机溶剂,或(ii)借助水蒸气,其中 得到含有芳族化合物的洗出液。

    SYNTHESIS OF ZEOLITIC MATERIALS USING N,N-DIMETHYL ORGANOTEMPLATES
    10.
    发明公开
    SYNTHESIS OF ZEOLITIC MATERIALS USING N,N-DIMETHYL ORGANOTEMPLATES 审中-公开
    沸石材料的合成使用N,N-二甲基有机模板

    公开(公告)号:EP2753579A1

    公开(公告)日:2014-07-16

    申请号:EP12830164.5

    申请日:2012-09-06

    Applicant: BASF SE

    CPC classification number: C01B39/48 B01J29/7015

    Abstract: A process for the preparation of a zeolitic material having a structure comprising YO
    2 and X
    2 O
    3 is provided, wherein said process comprises the steps of ( 1 ) providing a mixture comprising one or more ammonium compounds of which the ammonium cation has the formula (I): [R
    1 R
    2 NR
    3 R
    4+ (I) and further comprising one or more sources for Y0
    2 and one or more sources for X
    2 O
    3 ; (2) crystallizing the mixture provided in step ( 1 ); wherein Y is a tetravalent element, and X is a trivalent element, and wherein the ammonium compounds are preferably derivatized or underivatized N,N-dimethylpyrrolidinium compounds, Ν,Ν-dimethylpiperidinium compounds, Ν,Ν-dimethylhexahydroazepinium compounds, and mixtures thereof, and wherein the molar ratio of ammonium cation having the formula (I) to Y in the mixture provided in step (1) and crystallized in step (2) is equal to or greater than 0.25.

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