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    • 4. 发明授权
    • Process for initiating a highly selective ethylene oxide catalyst
    • 引发高选择性环氧乙烷催化剂的方法
    • US08487123B2
    • 2013-07-16
    • US12977549
    • 2010-12-23
    • Nabil RizkallaNorma B. CastagnolaGirish Desai
    • Nabil RizkallaNorma B. CastagnolaGirish Desai
    • C07D301/03
    • C07D301/10
    • A start-up process for epoxidation of ethylene is provided. The process includes initiating an epoxidation reaction by reacting a feed gas composition in the presence of an epoxidation catalyst at a first temperature of about 180° C. to about 210° C. The first temperature is increased to a second temperature of about 230° C. to about 290° C., over a time period of about 6 hours to about 50 hours, while simultaneously adding a sufficient concentration of moderator so that the amount of moderator adsorbed on the catalyst after achieving the second temperature is from about 10 to about 50 g/m3 of catalyst. The second temperature is maintained for about 50 hours to about 350 hours, while regulating the feed gas composition to contain about 0.5% to about 25% CO2. The second temperature is decreased to a third temperature, while simultaneously increasing moderator concentration to a level greater than the sufficient concentration.
    • 提供了乙烯环氧化的启动方法。 该方法包括通过在约180℃至约210℃的第一温度下在环氧化催化剂存在下使进料气体组合物反应来引发环氧化反应。将第一温度升至约230℃的第二温度 至约290℃,同时加入约6小时至约50小时的时间,同时加入足够浓度的缓和剂,使得达到第二温度后吸附在催化剂上的缓和剂的量为约10至约 50 g / m3催化剂。 第二温度保持约50小时至约350小时,同时调节进料气体组成以含有约0.5%至约25%的CO 2。 第二温度降低到第三温度,同时将增效剂浓度同时提高至高于足够浓度的水平。
    • 5. 发明授权
    • Process for preparation of a catalyst carrier
    • 催化剂载体的制备方法
    • US08318627B2
    • 2012-11-27
    • US11201253
    • 2005-08-10
    • Nabil Rizkalla
    • Nabil Rizkalla
    • B01J21/00B01J23/00B01J25/00B01J29/00B01J31/00B01J23/08B01J20/00
    • B01J21/04B01J23/50B01J37/0018C07D301/08C07D301/10
    • This invention relates to catalyst carriers to be used as supports for metal and metal oxide catalyst components of use in a variety of chemical reactions. More specifically, the invention provides a process of formulating a low surface area alpha alumina carrier that is suitable as a support for silver and the use of such catalyst in chemical reactions, especially the epoxidation of ethylene to ethylene oxide. A precursor for a catalyst support comprises an admixture of an alpha alumina and/or a transition alumina; a binder; and either a solid blowing agent which expands, or propels a gas upon the application of sufficient heat, and optionally contains talc and/or water soluble titanium compound.
    • 本发明涉及用作用于各种化学反应的金属和金属氧化物催化剂组分的载体的催化剂载体。 更具体地说,本发明提供了一种配制低表面积α氧化铝载体的方法,其适合作为银的载体,以及在化学反应中使用这种催化剂,特别是将乙烯环氧化成环氧乙烷。 催化剂载体的前体包含α氧化铝和/或过渡氧化铝的混合物; 粘合剂 以及在施加足够的热量时膨胀或推动气体的固体发泡剂,并且任选地含有滑石和/或水溶性钛化合物。