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    • 3. 发明授权
    • Coproduction of vinylidene alcohols and vinylidene hydrocarbons
    • 亚乙烯基醇和亚乙烯基烃的共同生产
    • US5731480A
    • 1998-03-24
    • US552638
    • 1995-11-03
    • Kaung-Far Lin
    • Kaung-Far Lin
    • B01J31/14C07B61/00C07C2/30C07C2/88C07C11/02C07C29/10C07C29/54C07C31/02C07C29/04
    • C07C2/30C07C2/88C07C29/54C07C2531/14
    • A process is described for coproducing vinylidene alcohol and vinylidene olefin. The process involves dimerizing one or more vinylolefins with an alkyl aluminum catalyst to form a first product mixture comprising at least vinylidene olefin and alkyl aluminum compound. The vinylidene olefin is then reacted with the alkyl aluminum compound under displacement conditions to form 1-olefin while concurrently removing the 1-olefin from the displacement reaction mixture to form a second product mixture comprising at least beta-branched alkyl aluminum compound. The second product mixture is treated with air or oxygen under mild oxidation conditions to form a third product mixture comprising at least beta-branched aluminum alkoxide. The beta-branched aluminum alkoxide is then hydrolyzed to form vinylidene alcohol. The process makes effective use of the alkyl aluminum catalyst both as a catalyst and as a reactant, and requires only a relatively small amount of reaction equipment.
    • 描述了用于共聚亚乙烯醇和亚乙烯基烯烃的方法。 该方法包括使一种或多种烯烃与烷基铝催化剂二聚,以形成至少包含亚乙烯基烯烃和烷基铝化合物的第一产物混合物。 然后将亚乙烯基烯烃与置换条件下的烷基铝化合物反应以形成1-烯烃,同时从置换反应混合物中除去1-烯烃以形成至少包含β-支链烷基铝化合物的第二产物混合物。 第二产物混合物在温和氧化条件下用空气或氧气处理以形成至少包含β-支链烷醇铝的第三产物混合物。 然后将β-支链的烷氧基铝水解形成亚乙烯基醇。 该方法有效地利用烷基铝催化剂作为催化剂和作为反应物,并且仅需要相对少量的反应设备。
    • 6. 发明授权
    • Production of vinylidene olefins
    • 生产亚乙烯基烯烃
    • US5663469A
    • 1997-09-02
    • US596812
    • 1996-02-05
    • Douglas H. KrzystowczykKaung-Far Lin
    • Douglas H. KrzystowczykKaung-Far Lin
    • C07C2/30C07C2/26
    • C07C2/30C07C2531/14
    • Vinylidene olefin can be formed in good yield and high selectivity in much shorter reaction periods than found critical heretofore. The process involves dimerizing vinyl olefin with at least one trialkylaluminum compound as the catalyst component charged to the reaction vessel. These materials are charged to the reactor so that it contains in the range of 0.001 to 0.5 mol of trialkylaluminum per mol of the initial vinyl olefin. The reaction is performed at a temperature in the range of 100.degree. to 200.degree. C. for a period of time sufficient to convert 10 to 99% by weight of the initial vinyl olefin to a different product with at least 80 wt % vinylidene dimer selectivity. In conducting the process the liquid reaction mixture is in direct contact with a nickel-containing metal alloy surface for at least one hour at a temperature above about 50.degree. C., and (ii) at least one acetylenic hydrocarbon is added to the mixture prior to such contact in an mount at least sufficient to inhibit double bond isomerization in the reaction mixture but insufficient to inhibit formation of the vinylidene dimer. The acetylenic hydrocarbon also overcomes the devastating effect nickel impurities in the feed or in residues in the reactor have on dimer selectivity.
    • 亚乙烯基烯烃可以以比现在关键的短得多的反应时间段以良好的产率和高选择性形成。 该方法包括使乙烯基烯烃与至少一种三烷基铝化合物二聚作为装入反应容器的催化剂组分。 将这些材料装入反应器,使其每摩尔初始乙烯基烯烃含有0.001至0.5摩尔三烷基铝的范围。 该反应在100℃至200℃的温度下进行足以将10至99重量%的初始乙烯基烯烃转化成不同的产物,至少80重量%的亚乙烯基二聚体选择性 。 在进行该过程中,液体反应混合物与含镍金属合金表面在高于约50℃的温度下直接接触至少1小时,和(ii)将至少一种炔属烃加入到混合物中 至少足以抑制反应混合物中的双键异构化但不足以抑制亚乙烯基二聚体形成的这种接触。 炔烃还克服了进料中的镍杂质或反应器中的残留物对二聚体选择性的破坏性影响。
    • 7. 发明授权
    • Production of vinylidene olefins
    • 生产亚乙烯基烯烃
    • US5625105A
    • 1997-04-29
    • US596848
    • 1996-02-05
    • Kaung-Far LinCarroll W. Lanier
    • Kaung-Far LinCarroll W. Lanier
    • B01J31/14C07B61/00C07C2/30C07C11/09C07C11/10C07C11/107C07C2/26
    • C07C2/30C07C2531/14
    • Vinylidene olefin can be formed in good yield in much shorter reaction periods than found critical heretofore. The process involves dimerizing vinyl olefin with at least one trialkylaluminum compound as the sole catalyst component charged to the reaction vessel. These materials are charged to the reactor so that it contains in the range of 0.001 to 0.05 mol of trialkylaluminum per mol of the initial vinyl olefin. The reaction is performed at a temperature in the range of over 140.degree. C. and below 172.degree. C. for a period of time in the range of 1 to 24 hours sufficient to convert at least 10% by weight of the initial vinyl olefin to a different product with at least 80 wt % vinylidene dimer selectivity.
    • 亚乙烯基烯烃可以在比目前关键的短得多的反应时间内以良好的产率形成。 该方法包括将乙烯基烯烃与至少一种三烷基铝化合物二烯化,作为装入反应容器的唯一催化剂组分。 将这些材料装入反应器,使其每摩尔初始乙烯基烯烃含有0.001至0.05摩尔三烷基铝。 反应在超过140℃和低于172℃的温度下进行,持续1至24小时的时间足以将至少10重量%的初始乙烯基烯烃转化为 具有至少80重量%亚乙烯基二聚体选择性的不同产品。
    • 8. 发明授权
    • Dimerization catalyst and process using alkyl aluminum alkoxide
    • 二甲基化催化剂和使用烷基铝醇盐的方法
    • US5824833A
    • 1998-10-20
    • US345964
    • 1994-11-28
    • Kaung-Far Lin
    • Kaung-Far Lin
    • B01J31/14C07C2/24C07C2/30C07C11/02C07C2/26
    • C07C2/30B01J31/143C07C2531/14
    • A process for producing an vinylidene olefin of the formula ##STR1## where R.sup.1 and R.sup.2 are the same or different and are hydrogen or alkyl and m is an integer of from 0 to 18, with a catalytically effective amount of a mixture of i) an aluminum compound of the formula R.sup.4.sub.n Al(OR.sup.5).sub.p where R.sup.4 and R.sup.5 are the same or different and are alkyl, n is an integer from 0.75 to 2.75, and p is an integer from 0.25 to 2.25, the sum of n and p being 3, at a temperature of from about 120.degree. C. to about 200.degree. C. whereby a major amount of said vinylidene and deep internal olefin dimer is produced and only a minor amount of a beta internal olefin isomer.
    • 一种制备式“IMAGE”的亚乙烯基烯烃的方法,其中R 1和R 2相同或不同,为氢或烷基,m为0至18的整数,其催化有效量的混合物为i) 式R 4 n Al(OR 5)p的铝化合物,其中R 4和R 5相同或不同,为烷基,n为0.75至2.75的整数,p为0.25至2.25的整数,n和p的和为3 在约120℃至约200℃的温度下,由此产生主要量的所述亚乙烯基和深内烯烃二聚体,并且仅产生少量的β内烯烃异构体。
    • 9. 发明授权
    • Production and utilization of tri-(beta-branched alkyl) aluminum
compounds
    • 三(β-支链烷基)铝化合物的生产和利用
    • US5686640A
    • 1997-11-11
    • US708019
    • 1996-08-30
    • Kaung-Far Lin
    • Kaung-Far Lin
    • C07F5/06
    • C07F5/063Y02P20/127
    • Processes are described for the production and use of tri-(beta-branched alkyl)aluminum compounds. In a preferred embodiment, a process of this invention involves dimerizing one or more vinylolefin monomers with an alkyl aluminum catalyst to form a first product mixture comprising at least vinylolefin monomer, trialkylaluminum in which each alkyl group has the same number of carbon atoms and skeletal structure as said vinylolefin monomer, and vinylidene olefin. The vinylolefin monomer is then removed while concurrently the trialkylaluminum and vinylidene olefin are converted to tri-(beta-branched alkyl)aluminum by reactive distillation. Reactive distillation effects a shift of the chemical equilibrium away from the trialkylaluminum compound and toward the production of tri-(beta-branched alkyl)aluminum. compound. The tri-(beta-branched alkyl)aluminum compound may then be purified by a subsequent distillation, or similarly purified and recycled back into the process as the alkyl aluminum catalyst used in forming the first product mixture. The described processes constitute highly efficient economical processes which may be carried out in a single reactor, if desired, for the high-yield production and use of such compounds.
    • 描述了制备和使用三 - (β-支链烷基)铝化合物的方法。 在一个优选的实施方案中,本发明的方法涉及使一种或多种乙烯基烯烃单体与烷基铝催化剂进行二聚,以形成第一产物混合物,其至少包含单烯属单体,三烷基铝,其中每个烷基具有相同数目的碳原子和骨架结构 如所述的乙烯基烯烃单体和亚乙烯基烯烃。 然后除去乙烯基烯烃单体,同时通过反应蒸馏将三烷基铝和亚乙烯基烯烃转化成三(β-支链烷基)铝。 反应蒸馏影响化学平衡偏离三烷基铝化合物和三(β-支链烷基)铝的生产。 复合。 然后可以通过随后的蒸馏纯化三 - (β-支链烷基)铝化合物,或者类似地纯化并再循环回到作为形成第一产物混合物中的烷基铝催化剂的工艺中。 所描述的方法构成了高效的经济方法,如果需要,可以在单个反应器中进行,用于高产量生产和使用这些化合物。