Process for the preparation of oligomers
    31.
    发明申请
    Process for the preparation of oligomers 审中-公开
    制备低聚物的方法

    公开(公告)号:US20030045752A1

    公开(公告)日:2003-03-06

    申请号:US10176301

    申请日:2002-06-20

    IPC分类号: C07C051/16 C07C002/02

    摘要: Process for the oligomerization of one or more olefinically unsaturated monomers comprising three or more carbon atoms, at least one of these monomers consisting of a C3 to C30 aliphatic mono-olefin, which process comprises reacting the olefinically unsaturated monomer(s) under oligomerization conditions in the presence of an effective amount of a catalyst system based on (a) a specific titanium bisamide compound or its dimer; (b) one or more activating cocatalysts comprising at least one boron atom; and optionally, but in any event if the titanium bisamide compound or its dimer comprise halogen: (c) one or more aluminium alkyls or alumoxanes. A mixture of homo-oligomers of propylene is provided by the above process, which mixture comprises oligomers of propylene based on up to 20 propylene molecules, wherein at least 50 mole % of the oligomer chains have a terminal vinyl group.

    摘要翻译: 包含三个或更多个碳原子的一种或多种烯属不饱和单体低聚的方法,这些单体中的至少一种由C 3至C 30脂族单烯烃组成,该方法包括在低聚条件下使烯属不饱和单体反应 存在有效量的基于(a)特定的钛双酰胺化合物或其二聚体的催化剂体系; (b)一种或多种包含至少一个硼原子的活化助催化剂; 并且任选地,但无论如何,如果钛二酰胺化合物或其二聚体包含卤素:(c)一种或多种烷基铝或铝氧烷。 通过上述方法提供丙烯均聚物的混合物,该混合物包含基于至多20个丙烯分子的丙烯低聚物,其中至少50摩尔%的低聚物链具有末端乙烯基。

    Selective ring-opening cross-metathesis of cycloolefins
    32.
    发明申请
    Selective ring-opening cross-metathesis of cycloolefins 有权
    环烯烃的选择性开环交叉复分解

    公开(公告)号:US20020198426A1

    公开(公告)日:2002-12-26

    申请号:US10114674

    申请日:2002-04-01

    IPC分类号: C07C002/02 C07C006/00

    摘要: A catalytic method is provided for a ring-opening cross-metathesis reaction between a cycloolefinic substrate and a second olefinic reactant, wherein the catalyst used is a transition metal alkylidene complex substituted with an N-heterocyclic carbene ligand. The substrates are selected so that the rate of the cross-metathesis reaction of the second olefinic reactant, kCM, is greater than or equal to the rate of the ring-opening metathesis reaction, kRO. In this way, the predominant ROCM product is a monomer, dimer, and/or oligomer, but not a polymer. The invention additionally provides for selective production of an end-differentiated olefinic product, using trisubstituted cycloolefins as substrates and/or a subsequent cross-metathesis reaction following an initial ROCM step. The cycloolefinic substrates include low-strain olefins such as cyclohexene as well as higher strain olefins such as cyclooctene.

    摘要翻译: 提供了用于环烯基底物和第二烯属反应物之间的开环交叉复分解反应的催化方法,其中使用的催化剂是被N-杂环卡宾配体取代的过渡金属亚烷基络合物。 选择底物使得第二烯属反应物的交叉复分解反应速率kCM大于或等于开环复分解反应速率(kRO)。 以这种方式,主要的ROCM产物是单体,二聚体和/或低聚物,但不是聚合物。 本发明另外提供了在初始ROCM步骤之后使用三取代的环烯烃作为底物和/或随后的交叉复分解反应来选择性生产末端分解的烯烃产物。 环烯烃底物包括低应变烯烃如环己烯以及较高级烯烃如环辛烯。

    Sequence of processes for olefin oligomerisation
    33.
    发明申请
    Sequence of processes for olefin oligomerisation 有权
    烯烃低聚方法的顺序

    公开(公告)号:US20020052537A1

    公开(公告)日:2002-05-02

    申请号:US09984053

    申请日:2001-10-26

    IPC分类号: C07C002/02

    摘要: A process is described for carrying out olefin oligomerisation in two catalysis steps of different types, using an organic feed containing at least one olefin. The cut to be treated, containing at least one olefin (Cn), is introduced into a first reaction zone where, in a first step, it undergoes catalytic oligomerisation either of the homogeneous liquid phase type, or of the heterogeneous type with a solid support. The effluent produced is generally sent to a heat exchanger traversed by a cold liquid, the effluent thus being cooled before being sent to a second reaction zone where it undergoes catalytic oligomerisation in a liquid-liquid two-phase medium, the invention being characterized in that at least an ethylenic hydrocarbon containing 3 to 5 carbon atoms per molecule is added to the inlet to the second reaction zone.

    摘要翻译: 描述了一种使用含有至少一种烯烃的有机进料在不同类型的两个催化步骤中进行烯烃低聚的方法。 将要处理的含有至少一种烯烃(Cn)的切割物引入第一反应区域,其中在第一步骤中,其经历均相液相型或异相型催化低聚,具有固体支持物 。 所产生的流出物通常被送到由冷液体穿过的热交换器中,因此流出物在被送到第二反应区之前被冷却,在第二反应区中,其在液 - 液两相介质中经历催化低聚,本发明的特征在于 每个分子至少含有3至5个碳原子的烯烃加入第二反应区的入口。

    Acetaldehyde dehydration to produce ethyne
    34.
    发明申请
    Acetaldehyde dehydration to produce ethyne 审中-公开
    乙醛脱水生成乙炔

    公开(公告)号:US20020026088A1

    公开(公告)日:2002-02-28

    申请号:US09910248

    申请日:2001-07-20

    发明人: Christian Everett

    CPC分类号: C07C1/24 C07C11/24

    摘要: A process of dehydrating acetaldehyde to produce ethyne comprising passing acetaldehyde in the gas phase over a dehydration catalyst such as aluminum oxide which may be promoted with mercuric sulfate at a temperature of approximately 600 degrees Centigrade to produce ethyne and water and a cooling zone following the reaction zone. This method having the advantage of ease of separation of ethyne from the unreacted acetaldehyde and co-product water by simple condensation whereby the ethyne remains gaseous while the other compounds liquify and is thereby separated in essentially pure form.

    摘要翻译: 一种使乙醛脱水以产生乙炔的方法,包括使气相中的乙醛在脱氧催化剂如氧化铝上通入,该催化剂可以在约600摄氏度的温度下用硫酸汞硫酸盐促进,以产生乙炔和水,以及反应后的冷却区 区。 该方法具有易于通过简单冷凝将乙炔与未反应的乙醛和共产物水分离的优点,由此乙炔保持气态,而其它化合物液化,从而以基本上纯的形式分离。

    Process for preparing substituted benzyl compounds and toluene derivatives
    36.
    发明申请
    Process for preparing substituted benzyl compounds and toluene derivatives 审中-公开
    取代苄基化合物和甲苯衍生物的制备方法

    公开(公告)号:US20010020104A1

    公开(公告)日:2001-09-06

    申请号:US09790757

    申请日:2001-02-22

    申请人: Clariant GmbH

    IPC分类号: C07C002/02 C07C006/12

    摘要: The novel two-stage process described here makes it possible to obtain substituted benzyl compounds and toluene derivatives in a simple manner and in high yields by means of Suzuki-type coupling reactions of an aromatic with an organoboron compound, followed by a reduction. The process is particularly useful for preparing ortho-substituted benzyl compounds and toluene derivatives. The process can be applied to both intermolecular and intramolecular coupling reactions. Catalysts used for the coupling reaction are palladium compounds and/or nickel compounds. An advantageous aspect is that only very small amounts of catalyst are required.

    摘要翻译: 这里描述的新颖的两阶段方法可以通过芳香族与有机硼化合物的铃木型偶联反应,然后进行还原,以简单的方式和高收率得到取代的苄基化合物和甲苯衍生物。 该方法对于制备邻位取代的苄基化合物和甲苯衍生物特别有用。 该方法可以应用于分子间和分子内的偶联反应。 用于偶联反应的催化剂是钯化合物和/或镍化合物。 有利的方面是仅需要非常少量的催化剂。

    Process for dimerizing light olefins
    37.
    发明申请
    Process for dimerizing light olefins 有权
    二烯化轻质烯烃的方法

    公开(公告)号:US20040181106A1

    公开(公告)日:2004-09-16

    申请号:US10383763

    申请日:2003-03-10

    IPC分类号: C07C002/02

    摘要: The invention relates to a process for dimerizing lower, olefinic hydrocarbons. In particular, the present invention concerns a process for dimerizing C3-, C4 and C5-olefins with a medium pore zeolite under process conditions allowing selective dimerization According to the invention, fresh olefinic hydrocarbon feedstock is fed to a reaction system including at least one reaction zone and at least one separation zone. The olefinic hydrocarbon feedstock is contacted with an acid catalyst at conditions in which at least a part of the olefins dimerizes. The effluent from the reaction zone is conducted to the separation zone where dimerized reaction product is separated from said effluent.

    摘要翻译: 本发明涉及二烯化低级烯烃的方法。 特别地,本发明涉及在允许选择性二聚化的工艺条件下用中孔沸石二聚C3-,C4和C5-烯烃的方法。根据本发明,将新鲜的烯烃原料进料到包括至少一个反应 区域和至少一个分离区域。 烯烃原料在至少一部分烯烃二聚的条件下与酸催化剂接触。 将来自反应区的流出物进入分离区,其中二聚反应产物与所述流出物分离。

    Process for producing alpha-olefins
    38.
    发明申请
    Process for producing alpha-olefins 审中-公开
    生产α-烯烃的方法

    公开(公告)号:US20040143147A1

    公开(公告)日:2004-07-22

    申请号:US10702685

    申请日:2003-11-06

    IPC分类号: C07C002/02

    摘要: Active catalyst components, in a process stream from the formation of null-olefins by the catalyzed oligomerization of ethylene using complexes of late transition metals with tridentate ligands as catalyst components, can be accomplished by contacting the process stream with a protic organic compound having a specified pKa.

    摘要翻译: 通过使用具有三齿配体作为催化剂组分的后过渡金属的络合物通过乙烯的催化低聚形成α-烯烃的方法流中的活性催化剂组分可以通过使工艺流与具有规定的质子有机化合物 pKa。

    Method for producing polyisobutenes
    40.
    发明申请
    Method for producing polyisobutenes 失效
    生产聚异丁烯的方法

    公开(公告)号:US20040015029A1

    公开(公告)日:2004-01-22

    申请号:US10433439

    申请日:2003-06-04

    IPC分类号: C07C002/02

    摘要: Polyisobutenes in which at least 60 mol % of the polymer chains have at least one olefinically unsaturated terminal group are prepared by cationic polymerization of isobutene or isobutene-containing monomer mixtures in the condensed phase by a process in which the polymerization is carried out in the presence of an initiator system comprising i) a Lewis acid selected from covalent metal chlorides and semimetal chlorides and ii) at least one organic compound I having at least one functional group FG which forms a carbocation or a cationic complex with the Lewis acid under the polymerization conditions, where FG is selected from acyloxy, alkoxy and halogen, which are bonded to a secondary or tertiary carbon atom or to an allylic or a benzylic carbon atom, in a solvent inert toward the Lewis acid, the Lewis acid being used in less than the stoichiometric amount, based on the functional groups FG.

    摘要翻译: 其中至少60mol%的聚合物链具有至少一个烯属不饱和端基的聚异丁烯是通过在冷凝相中通过异丁烯或含异丁烯的单体混合物的阳离子聚合制备的,其中聚合在存在下进行 的引发剂体系,其包含i)选自共价金属氯化物和半金属氯化物的路易斯酸,和ii)至少一种在聚合条件下与路易斯酸形成碳阳离子或阳离子络合物的官能团FG的有机化合物I 其中FG选自酰基氧基,烷氧基和卤素,其在与路易斯酸呈惰性的溶剂中结合到仲或叔碳原子或烯丙基或苄基碳原子上,路易斯酸的用量小于 基于官能团FG的化学计量量。