Aerobic oxidation of alkanes
    1.
    发明授权
    Aerobic oxidation of alkanes 有权
    烷烃的有氧氧化

    公开(公告)号:US09150971B2

    公开(公告)日:2015-10-06

    申请号:US13597071

    申请日:2012-08-28

    CPC classification number: C25B3/02 C25B3/00 C25B9/08

    Abstract: An aerobic method for oxidizing an alkane is disclosed herein. At least a portion of a surface of a platinum working electrode is activated at an interface between the platinum working electrode and an ionic liquid electrolyte (i.e., 1-ethyl-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)imide, 1-propyl-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)imide, 1-butyl-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)imide, 1-pentyl-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)imide, 1-hexyl-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)imide, 1-heptyl-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)imide, 1-octyl-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)imide, 1-nonyl-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)imide, and 1-decyl-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)imidem, and combinations thereof). An interface complex is formed at the interface. An alkane gas is supplied to the interface. The alkane adsorbs at or near the interface complex. The alkane gas in the presence of oxygen is supplied to the interface. While the alkane gas in the presence of oxygen is supplied to the interface, a positive electrode potential is applied to the platinum working electrode, which causes a reactive oxygen species formed at the interface to catalyze oxidation of the adsorbed alkane to form a reaction product.

    Abstract translation: 本文公开了一种用于氧化烷烃的好氧方法。 铂工作电极的至少一部分表面在铂工作电极和离子液体电解质(即,1-乙基-1-甲基吡咯烷鎓双(三氟甲基磺酰基)酰亚胺,1-丙基-1-甲基吡咯烷鎓 (三氟甲基磺酰基)酰亚胺,双(三氟甲基磺酰基)酰亚胺,1-戊基-1-甲基吡咯烷鎓双(三氟甲基磺酰基)酰亚胺,1-己基-1-甲基吡咯烷鎓双(三氟甲基磺酰基)酰亚胺,1-庚基-1 (三氟甲基磺酰基)酰亚胺,1-辛基-1-甲基吡咯烷鎓双(三氟甲基磺酰基)酰亚胺,1-壬基-1-甲基吡咯烷鎓双(三氟甲基磺酰基)酰亚胺和1-癸基-1-甲基吡咯烷鎓双(三氟甲磺酰基)亚胺,以及组合 )。 在接口上形成接口复合体。 烷烃气体被供应到界面。 烷烃在界面络合物处或附近吸附。 在存在氧气的情况下将烷烃气体供应给界面。 当在存在氧气的情况下将烷烃气体供应到界面时,将正极电位施加到铂工作电极,这导致在界面处形成的活性氧物质催化吸附的烷烃的氧化以形成反应产物。

    Method for producing aldehyde functional compounds
    3.
    发明授权
    Method for producing aldehyde functional compounds 失效
    醛官能化合物的制备方法

    公开(公告)号:US08394996B2

    公开(公告)日:2013-03-12

    申请号:US13142505

    申请日:2010-01-12

    CPC classification number: C07C29/32 C07C67/333 Y02P20/55 C07C33/03 C07C69/732

    Abstract: The invention relates to a method for producing aldehyde functional compounds by a cross-metathesis reaction of an olefinic compound having at least one hydroxy group and at least one C—C double bond with at least one at least monounsaturated fatty acid or at least one at least monounsaturated fatty acid derivative, in the presence of a metathesis catalyst at a maximum temperature of 180° C. and in the presence of at least one reagent that acts as a protective group-forming compound in relation to the aldehyde group of the aldehyde functional compounds.

    Abstract translation: 本发明涉及通过具有至少一个羟基和至少一个C-C双键的至少一个至少一个不饱和脂肪酸或至少一个不饱和脂肪酸的烯属化合物的交叉复分解反应来生产醛官能化合物的方法, 在复分解催化剂存在下,在最高温度为180℃,并且在至少一种作为形成保护基团的化合物作为保护基形成化合物相对于醛官能团的醛基的试剂存在下,最少单不饱和脂肪酸衍生物 化合物。

    Industrial Process For Production Of High-Purity Diphenyl Carbonate
    4.
    发明申请
    Industrial Process For Production Of High-Purity Diphenyl Carbonate 有权
    高纯度碳酸二苯酯生产工艺

    公开(公告)号:US20080041712A1

    公开(公告)日:2008-02-21

    申请号:US11660362

    申请日:2005-08-24

    Abstract: It is an object of the present invention to provide a specific process that enables a high-purity diphenyl carbonate that can be used as a raw material of a high-quality and high-performance polycarbonate to be produced stably for a prolonged period of time on an industrial scale of not less than 1 ton/hr from a reaction mixture containing a catalyst and reaction by-products that has been obtained through transesterification reaction and the like using a dialkyl carbonate and a phenol as a starting material. Although there have been various proposals regarding processes for the production of reaction mixtures containing aromatic carbonates by means of a reactive distillation method, these have all been on a small scale and short operating time laboratory level, and there have been no disclosures on a specific process or apparatus enabling mass production on an industrial scale from such a reaction mixture to a high-purity diphenyl carbonate that can be used as a raw material of a high-quality and high-performance polycarbonate. According to the present invention, there are provided a high boiling point material separating column A and a diphenyl carbonate purifying column B each comprising a continuous multi-stage distillation column having specified structures, and there is provided a specific process that enables a high-purity diphenyl carbonate which is important as a raw material of a high-quality and high-performance polycarbonate to be produced stably for a prolonged period of time on an industrial scale of not less than 1 ton/hr from a reaction mixture containing the diphenyl carbonate using an apparatus in which these two continuous multi-stage distillation columns are connected together.

    Abstract translation: 本发明的目的是提供一种具体方法,其能够将高纯度碳酸二苯酯用作高质量和高性能聚碳酸酯的原料,以在较长时间内稳定地制备, 从含有催化剂的反应混合物和通过酯交换反应等获得的反应副产物使用碳酸二烷基酯和苯酚作为起始原料的工业规模不低于1吨/小时。 虽然已经有关于通过反应蒸馏法生产含有芳族碳酸酯的反应混合物的方法的各种建议,但是这些方法都已经在小规模和操作时间短的实验室水平上,并且没有公开具体方法 或能够从这种反应混合物到能够用作高质量和高性能聚碳酸酯的原料的高纯度碳酸二苯酯在工业规模上批量生产的装置。 根据本发明,提供了一种分离塔A和碳酸二苯酯精制塔B的高沸点物质,它们均包含具有特定结构的连续多级蒸馏塔,并且提供了能够获得高纯度 碳酸二苯酯作为高质量,高性能的聚碳酸酯的原料,以不低于1吨/小时的工业规模从含有碳酸二苯酯的反应混合物中长时间稳定地制备而成,其使用 这两个连续多级蒸馏塔连接在一起的装置。

    Continuous production of axerophthol
    7.
    发明授权
    Continuous production of axerophthol 失效
    连续生产AXEROPHTHOL

    公开(公告)号:US3681466A

    公开(公告)日:1972-08-01

    申请号:US3681466D

    申请日:1969-09-23

    Applicant: BASF AG

    CPC classification number: C07C403/08 C07C2601/16

    Abstract: Continuous production of axerophthol by reaction of axerophthyl acetate with a lower alcohol using guanidine as transesterification catalyst in two stages, alkyl acetate and some of the excess alcohol being distilled off in the first stage and the remainder of the alcohol being removed in the second stage by distillation with a hydrocarbon as entrainer.

    Abstract translation: 通过使用胍作为酯交换催化剂在两个阶段中通过乙酸半酯与低级醇反应连续生产萜烯酚,在第一阶段中将乙酸烷基酯和一些过量的醇在第二阶段被蒸馏除去,其余的醇在第二阶段被除去 用烃作为夹带剂进行蒸馏。

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