Flow control in a three-phase monolithic catalyst reactor
    2.
    发明授权
    Flow control in a three-phase monolithic catalyst reactor 失效
    三相整体式催化剂反应器中的流量控制

    公开(公告)号:US06822128B2

    公开(公告)日:2004-11-23

    申请号:US10027645

    申请日:2001-12-20

    IPC分类号: C07C502

    摘要: A method is disclosed for maintaining a volumetric gas to liquid ratio in a segmented gas/liquid flow along a reactor of monolithic catalyst beds in series. The present invention includes the steps of: initiating the segmented gas/liquid flow at a first end of the reactor by introducing feed liquid and feed gas both at a predetermined volume and a predetermined flow rate; injecting an additional amount of gas at least once into any of the spaces between catalyst beds; and combining the segments of the segmented gas/liquid flow at a second end of the reactor. The injection of gas is controlled such that the segmented gas/liquid flow can be maintained near or at the Taylor regime.

    摘要翻译: 公开了一种用于在沿着整体式催化剂床的反应器串联的分段气/液流中维持体积气体与液体比的方法。 本发明包括以下步骤:通过以预定的体积和预定流量引入进料液体和进料气体来在反应器的第一端引发分段的气/液流; 将至少一次额外量的气体注入催化剂床之间的任何空间; 并且在反应器的第二端处组合分段的气体/液体流的段。 控制气体的注入使得分段的气体/液体流可以保持在泰勒状态附近或处于泰勒状态。

    Process for hydrogenating cuts containing hydrocarbons, in particular unsaturated molecules containing at least two double bonds or at least one triple bond
    4.
    发明授权
    Process for hydrogenating cuts containing hydrocarbons, in particular unsaturated molecules containing at least two double bonds or at least one triple bond 有权
    氢化含有烃的切割的方法,特别是含有至少两个双键或至少一个三键的不饱和分子

    公开(公告)号:US06693225B2

    公开(公告)日:2004-02-17

    申请号:US09892764

    申请日:2001-06-28

    IPC分类号: C07C502

    摘要: Hydrogenation of a liquid cut containing hydrocarbons, in particular unsaturated molecules containing at least two double bonds or at least one triple bond, is described wherein the unsaturated molecules are at least partially hydrogenated to less unsaturated molecules containing at least one double bond, in at least one reactor comprising at least two distinct beds of at least one hydrogenation catalyst, and wherein a gas phase containing hydrogen is introduced, a portion thereof being mixed with said cut upstream of the first catalyst bed and a portion thereof being introduced upstream of the subsequent beds contained in said reactor.

    摘要翻译: 描述了含有烃,特别是含有至少两个双键或至少一个三键的不饱和分子的液体切割的氢化,其中不饱和分子至少部分氢化成至少含有至少一个双键的不饱和分子,至少在 一个反应器,其包括至少两个不同的床的至少一个氢化催化剂,并且其中引入含有氢的气相,其一部分与所述第一催化剂床的上游的所述切口混合,并且其一部分被引入后续床的上游 包含在所述反应器中。

    Hydrogenation of polyenes to monoenes
    6.
    发明授权
    Hydrogenation of polyenes to monoenes 失效
    将多烯氢化成单烯

    公开(公告)号:US06194624B1

    公开(公告)日:2001-02-27

    申请号:US09444316

    申请日:1999-11-22

    申请人: Rolf Pinkos

    发明人: Rolf Pinkos

    IPC分类号: C07C502

    CPC分类号: C07C5/05 C07C2523/46

    摘要: A process for hydrogenating polyenes, especially 1,5,9-cyclododecatriene, to the corresponding monoenes, especially cyclododecene, using homogeneous ruthenium catalysts comprises hydrogenating in the presence of a carboxylic acid, advantageously a C1-C20 monocarboxylic acid, a C2-C6 dicarboxylic acid, cyclohexylcarboxylic acid, benzoic acid, terephthalic acid, phthalic acid or phenylacetic acid, especially acetic acid, propionic acid, succinic acid or adipic acid or a C12-C20 fatty acid. The homogeneous ruthenium catalyst is advantageously generated in situ prior to the hydrogenation. The in situ generation is carried out in the additional presence of CO or formaldehyde and the hydrogenation in the additional presence of triphenylphosphine.

    摘要翻译: 使用均匀的钌催化剂将多烯,特别是1,5,9-环十二碳三烯氢化成相应的单烯,特别是环十二碳烯的方法包括在羧酸存在下,有利的是C 1 -C 20一元羧酸,C 2 -C 6二羧酸 酸,环己基羧酸,苯甲酸,对苯二甲酸,邻苯二甲酸或苯乙酸,特别是乙酸,丙酸,琥珀酸或己二酸或C 12 -C 20脂肪酸。均匀的钌催化剂有利地在氢化之前原位产生 。 原位产生在CO或甲醛的另外存在下进行,并且在另外存在三苯基膦的情况下进行氢化。

    Transition metal aerogel-supported catalyst
    9.
    发明授权
    Transition metal aerogel-supported catalyst 失效
    过渡金属气凝胶负载催化剂

    公开(公告)号:US06307116B1

    公开(公告)日:2001-10-23

    申请号:US08490573

    申请日:1995-06-15

    IPC分类号: C07C502

    摘要: A process for preparing a supported catalyst comprising a transition metal selected from palladium, platinum, nickel, cobalt or copper on an aerogel support, which includes the steps of providing a mixture containing an alkoxide precursor of the aerogel, a chelate complex of the transition metal with a chelating agent having Si(OR)3 anchor groups, and an organic solvent in which the chelate complex is soluble; hydrolyzing the mixture by admixing it with water to form a gel; and converting the gel under supercritical conditions into the transition metal aerogel-supported catalyst. The supported catalyst has an especially homogeneous distribution of the metal component and is suitable, for example, for use as a hydrogenation catalyst.

    摘要翻译: 一种制备负载型催化剂的方法,该催化剂包含在气凝胶载体上选自钯,铂,镍,钴或铜的过渡金属,其包括以下步骤:提供含有气凝胶的醇盐前体的混合物,过渡金属的螯合络合物 与具有Si(OR)3锚定基团的螯合剂和螯合络合物可溶的有机溶剂; 通过将混合物与水混合以形成凝胶来水解混合物; 并在超临界条件下将凝胶转化为过渡金属气凝胶负载的催化剂。 负载型催化剂具有金属组分特别均匀的分布,并且适用于例如用作氢化催化剂。

    Catalytic hydrogenation to remove gas from x-ray tube cooling oil

    公开(公告)号:US06632970B1

    公开(公告)日:2003-10-14

    申请号:US09474454

    申请日:1999-12-29

    申请人: Robert J. Lyons

    发明人: Robert J. Lyons

    IPC分类号: C07C502

    CPC分类号: H05G1/04 H05G1/025

    摘要: The present invention deals with the catalytic hydrogenation of fluid used to cool and dielectrically insulate an x-ray generating device within an x-ray system. According to the present invention, a method and apparatus are provided for hydrogenating fluid that has been exposed to x-rays to reduce the amount of H2 gas, free hydrogen atoms and unsaturated molecules in the fluid. The method comprises exposing the fluid within the x-ray system to a catalytically effective amount of catalyst. The catalyst operates in temperatures in the range of about 10-300° C. and pressures in the range of about 0.1-30 atmospheres. The catalyst may comprise a solid, non-soluble catalyst, a soluble catalyst, or a combination of both. A suitable solid, non-soluble catalyst comprises Group VIII elements and their compounds. Group VIII elements comprise iron, cobalt, nickel, ruthenium, rhodium, palladium, osmium, iridium and platinum. The catalytically effective amount of solid catalyst ranges from about 1-100 cm2 of surface area of solid catalyst per liter of fluid. Additionally, a suitable soluble catalyst may be added to the fluid and may comprise tris(triphenylphosphine) rhodium (I) chloride, precious metals in solution such as HRu(C2H4)(C6H4PPh2)(PPh3)2), Wilkinson's catalyst which comprises a rhodium, chromium, phosphorus triphenyl chloride compound, and other similar compounds. A catalytically effective amount of soluble catalyst may comprise from about 0.01-1 gram per liter of fluid. The fluid may comprise about 99.7% hydrocarbon, about 0.1% soluble catalyst, and the remainder comprising conditioning additives. The hydrocarbon preferably comprises about 99.7% hydrogenated light naphthenic petroleum distillates.