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    Process for preparing ketones, in particular macrocyclic ketones
    3.
    发明授权
    Process for preparing ketones, in particular macrocyclic ketones 有权
    制备酮的方法，特别是大环酮

    公开(公告)号：US08563781B2

    公开(公告)日：2013-10-22

    申请号：US13269016

    申请日：2011-10-07

    申请人： Michael Schelper ,  Christoph Stock ,  Klaus Ebel ,  Joaquim Henrique Teles ,  Ralf Pelzer

    发明人： Michael Schelper ,  Christoph Stock ,  Klaus Ebel ,  Joaquim Henrique Teles ,  Ralf Pelzer

    IPC分类号： C07C45/27

    CPC分类号： C07C45/28 ,  C07C45/62 ,  C07C2601/18 ,  C07C49/587 ,  C07C49/385

    摘要： Ketones of the formula II where A is optionally alkyl-substituted C2-C12-alkanediyl, R1 and R2 are each, independently of one another, C1-C6-alkyl, or R1 and R2 together form optionally alkyl-substituted C3-C10-alkanediyl, and R3 is hydrogen or C1-C6-alkyl, are prepared by reacting a cyclic olefin of the formula I with dinitrogen monoxide to form the ketone of the formula II. The ketone of the formula II can be further hydrogenated to form the saturated ketone of the formula III. Macrocyclic ketones of the formula III, e.g. muscone, are sought after as fragrances.

    摘要翻译： 式II的酮，其中A任选为烷基取代的C 2 -C 12 - 烷二基，R 1和R 2各自彼此独立地为C 1 -C 6 - 烷基，或者R 1和R 2一起形成烷基取代的C 3 -C 10 - 烷二基 R 3是氢或C 1 -C 6烷基，是通过使式I的环状烯与一氧化二氮反应形成式II的酮制备的。 式II的酮可以进一步氢化以形成式III的饱和酮。 式III的大环酮，例如 肌肉，被追捧为香水。

    TUBE BUNDLE REACTOR FOR UNCATALYZED OR HOMOGENEOUSLY CATALYZED REACTIONS
    5.
    发明申请
    TUBE BUNDLE REACTOR FOR UNCATALYZED OR HOMOGENEOUSLY CATALYZED REACTIONS 有权
    用于未加氢化或均相催化反应的管组反应器

    公开(公告)号：US20120157719A1

    公开(公告)日：2012-06-21

    申请号：US13380207

    申请日：2010-01-19

    申请人： Joaquim Henrique Teles ,  Peter Resch ,  Wilhelm Ruppel ,  Ulrike Wegerle ,  Wolfgang Gerliing ,  Beatrice Rössler-Feigel ,  Anton Meier ,  Christian Müller

    发明人： Joaquim Henrique Teles ,  Peter Resch ,  Wilhelm Ruppel ,  Ulrike Wegerle ,  Wolfgang Gerliing ,  Beatrice Rössler-Feigel ,  Anton Meier ,  Christian Müller

    IPC分类号： C07C45/00 ,  B01J19/00

    CPC分类号： B01J19/2425 ,  B01J4/001 ,  B01J19/006 ,  B01J2219/00085 ,  B01J2219/00166 ,  F28D7/16 ,  F28F9/0265 ,  F28F9/0275 ,  F28F9/0278 ,  Y02P20/582

    摘要： The invention relates to a tube bundle reactor with a flat feed hood. Alternatively, the release hood may also have a flat design. The flat design reduces the heat of reaction which arises in the hood in the case of reaction types which take place not only in the tube bundle (uncatalyzed reactions and reactions with homogeneously distributed catalyst). This greatly suppresses undesired reactions which already take place in the hood owing to accumulated heat, which achieves a higher selectivity in the case of thermally sensitive reactions. In addition, the thermal distribution within the hoods can be controlled precisely.The tube bundle reactor comprises a tube bundle which has a feed end which is connected to a feed hood of the tube bundle reactor, wherein the feed hood is configured in a flat design with a cross-sectional area at the feed end and an internal volume, and the ratio of internal volume to cross-sectional area is less than 0.35 m. The invention is further implemented by means of a process for operating a tube bundle reactor, comprising: introducing a reactant mixture into a tube bundle and converting at least a proportion of the reactant mixture within the tube bundle to a product. The introducing comprises: feeding the reactant mixture into an interior of a feed hood of the tube bundle reactor and passing the reactant mixture on into a feed end of the tube bundle in the form of a fluid stream. The fluid stream has a cross-sectional area on entry into the feed end, and the interior of the feed hood through which the fluid stream flows has an internal volume; where the ratio of internal volume to cross-sectional area is less than 0.35 m.

    摘要翻译： 本发明涉及具有扁平进料罩的管束反应器。 或者，释放罩也可以具有平坦的设计。 在反应类型不仅在管束（未催化的反应和具有均匀分布的催化剂的反应）的情况下，扁平设计减少了发动机罩中产生的反应热。 这大大地抑制了由于积热而在罩中发生的不期望的反应，这在热敏反应的情况下实现了更高的选择性。 此外，可以精确地控制罩内的热分布。 管束反应器包括管束，其具有连接到管束反应器的进料罩的进料端，其中进料罩构造成平坦设计，在进料端具有横截面积，内部体积 ，内部体积与横截面积的比值小于0.35μm。 通过用于操作管束反应器的方法进一步实现本发明，其包括：将反应物混合物引入管束并将至少一部分管束内的反应物混合物转化成产物。 引入包括：将反应物混合物进料到管束反应器的进料罩的内部，并将反应物混合物以流体流的形式送入管束的进料端。 流体流在进入进料端时具有横截面面积，流体流流过的进料罩的内部具有内部容积; 其中内部体积与横截面积的比值小于0.35μm。

    PROCESS FOR PREPARING GLYCIDYL ESTERS
    8.
    发明申请
    PROCESS FOR PREPARING GLYCIDYL ESTERS 失效
    制备甘油酯的方法

    公开(公告)号：US20110046401A1

    公开(公告)日：2011-02-24

    申请号：US12990756

    申请日：2009-06-10

    申请人： Kai Gumlich ,  Joaquim Henrique Teles ,  Roland Merten

    发明人： Kai Gumlich ,  Joaquim Henrique Teles ,  Roland Merten

    IPC分类号： C07D301/02

    CPC分类号： C07D303/16

    摘要： Process for preparing glycidyl esters, wherein carbonate esters of the formula I are reacted in the presence of a homogeneous catalyst with elimination of carbon dioxide to form glycidyl esters of the formula II where R in the above formulae is an organic radical having from 1 to 20 carbon atoms.

    摘要翻译： 制备缩水甘油酯的方法，其中式I的碳酸酯在均相催化剂的存在下反应，除去二氧化碳以形成式II的缩水甘油酯，其中上式中的R是具有1至20个的有机基团 碳原子。

    PROCESS FOR THE PREPARATION OF CYCLOPENTANONE
    10.
    发明申请
    PROCESS FOR THE PREPARATION OF CYCLOPENTANONE 审中-公开
    制备环丙烷酮的方法

    公开(公告)号：US20100179352A1

    公开(公告)日：2010-07-15

    申请号：US12602836

    申请日：2008-05-27

    申请人： Joaquim Henrique Teles ,  Mathieu Chabanas ,  Thomas Genger ,  Beatrice Rossler

    发明人： Joaquim Henrique Teles ,  Mathieu Chabanas ,  Thomas Genger ,  Beatrice Rossler

    IPC分类号： C07C45/28

    CPC分类号： C07C45/28 ,  C07C49/395

    摘要： The invention relates to a method for producing cyclopentanone. Said method comprises the step of reacting a mixture (G1), which contains at least cyclopentene, with a mixture (G2), which contains at least dinitrogen monoxide. The reaction is carried out in at least one reactor (R1) having channels with a diameter in the range of 0.1 mm to 50 mm, the reactor comprising at least two zones (Z1) and (Z2) having channels with different diameters and the diameters of the channels of zone (Z1) being smaller than the diameter of the channels of zone (Z2).

    摘要翻译： 本发明涉及一种生产环戊酮的方法。 所述方法包括使含有至少环戊烯的混合物（G1）与至少含有一氧化二氮的混合物（G2）反应的步骤。 反应在具有直径在0.1mm至50mm范围内的通道的至少一个反应器（R1）中进行，反应器包括至少两个具有不同直径的通道的区域（Z1）和（Z2），并且直径 的区域（Z1）的通道小于区域（Z2）的通道的直径。