Ethylene copolymerization catalyst
    73.
    发明授权
    Ethylene copolymerization catalyst 失效
    乙烯共聚催化剂

    公开(公告)号:US4948771A

    公开(公告)日:1990-08-14

    申请号:US280981

    申请日:1988-12-07

    申请人: Francis G. Stakem

    发明人: Francis G. Stakem

    CPC分类号: C08F10/00

    摘要: A catalyst composition comprising:(i) a complex comprised of V.sub.2 X.sub.3 (ED).sub.m and AlCl.sub.2 R.sub.2 whereinX=Cl, Br, or I, or mixtures thereofED=an electron donor, which is an ether, a phosphine, a ketone, an isocyanide, or an ester, said electron donor having 2 to 20 carbon atomsR=an alkyl having up to 14 carbon atomsm=an integer from 3 to 6,said complex impregnated into an inorganic oxide support;(ii) sufficient trialkylaluminum compound adsorbed on the inorganic oxide support to provide a molar ratio of adsorbed trialkylaluminum compound to vanadium of about 2.5:1 to about 10:1;(iii) a halocarbon promoter; and(iv) a hydrocarbyl aluminum cocatalyst.

    Catalyst for synthesis of mixtures of methanol and higher alcohols
    74.
    发明授权
    Catalyst for synthesis of mixtures of methanol and higher alcohols 失效
    用于合成甲醇和高级醇的混合物的催化剂

    公开(公告)号:US4943551A

    公开(公告)日:1990-07-24

    申请号:US796411

    申请日:1985-11-08

    申请人: Bernard D. Dombek

    发明人: Bernard D. Dombek

    摘要: Catalyst composition for the production of methanol and higher saturated aliphatic alcohols from synthesis gas. The catalysts consist essentially of:(i) about 0.18 to about 0.81 mol fraction of copper;(ii) about 0.045 to about 0.54 mol fraction of thorium;(iii) up to about 0.54 mol fraction of zirconium; and(iv) about 0.01 to about 0.2 mol fraction of an alkali metal.

    摘要翻译: 用于从合成气中生产甲醇和较高级饱和脂肪醇的催化剂组合物。 催化剂基本上由以下组成:(i)约0.18至约0.81摩尔份的铜; (ii)约0.045至约0.54摩尔份量的钍; (iii)至多约0.54摩尔份的锆; 和(iv)约0.01至约0.2摩尔碱金属的分数。

    Crystalline orthodontic bracket
    76.
    发明授权
    Crystalline orthodontic bracket 失效
    结晶正畸支架

    公开(公告)号:US4932865A

    公开(公告)日:1990-06-12

    申请号:US220303

    申请日:1988-07-18

    IPC分类号: A61C7/12 A61K6/06

    CPC分类号: A61C7/12

    摘要: A sapphire orthodontic bracket with enhanced tolerance to fabrication, installation and use is fabricated such that the "r" planes of the sapphire are at substantially equal angles to the longitudinal axis of the arch wire groove of the bracket.

    摘要翻译: 制造具有增强的制造,安装和使用耐受性的蓝宝石正畸托架,使得蓝宝石的“r”面与支架的拱形线槽的纵向轴线基本相等。

    Method for on-line decoking of flame cracking reactors
    79.
    发明授权
    Method for on-line decoking of flame cracking reactors 失效
    火焰裂解反应器在线除焦方法

    公开(公告)号:US4917787A

    公开(公告)日:1990-04-17

    申请号:US39756

    申请日:1987-04-16

    IPC分类号: C10G9/38

    CPC分类号: C10G9/38 Y10S585/95

    摘要: This invention relates to a method for on-line decoking of flame-cracking reactors whereby decoking is achieved without interruption of the normal operation of such reactors and without the necessity to change feed equipment and/or disassemble reactor components. While maintaining the temperature of the effluent at 1000.degree. C. to 2000.degree. C., the flow of the hydrocarbon feedstock in the reactor is periodically stopped for a time sufficient to reduce the carbon deposits to an acceptable level.

    摘要翻译: 本发明涉及一种火焰裂解反应器的在线除焦方法,其中除焦是在不中断这种反应器的正常运行的情况下进行的,而不需要改变进料设备和/或拆卸反应器部件。 在将流出物的温度保持在1000℃至2000℃的同时,将反应器中的烃原料的流动周期性地停止足以将碳沉积物降低至可接受水平的时间。

    Process and reaction vessel for production of alkyl nitrite
    80.
    发明授权
    Process and reaction vessel for production of alkyl nitrite 失效
    用于生产亚硝酸烷基酯的方法和反应容器

    公开(公告)号:US4908466A

    公开(公告)日:1990-03-13

    申请号:US102367

    申请日:1987-09-29

    申请人: James R. Nelson

    发明人: James R. Nelson

    摘要: A process and reaction vessel for producing alkyl nitrite is disclosed the process comprising (a) contacting nitric oxide, lower alcohol and oxygen in a reaction zone such that alkyl nitrite is formed, said reaction zone comprising a reactor section and a rectification section, (b) supplying a liquid scrubbing agent to an upper portion of the rectification section, (c) withdrawing a gaseous alkyl nitrite product stream from the upper portion of the rectification section, and (d) withdrawing a liquid stream from a lower portion of the reactor section. The reactor section provides intimate vapor-liquid contact sufficient to enhance the conversion of nitric oxide to alkyl nitrite and the rectification section provides sufficient vapor residence time to enhance conversion of oxygen, as well as sufficient rectification capabilities to reduce the amounts of water and nitric acid in the gaseous alkyl nitrite product stream.