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    • 5. 发明授权
    • Process for dehydrogenation of alkyl aromatic compounds
    • 烷基芳族化合物脱氢方法
    • US5679878A
    • 1997-10-21
    • US967517
    • 1992-10-28
    • Shiou-Shan ChenJoseph C. PetersLionel C. Allmand
    • Shiou-Shan ChenJoseph C. PetersLionel C. Allmand
    • C07C5/333C07C2/64C07C15/46
    • C07C5/3332C07C2523/745
    • This invention relates to a vapor phase process for the production of an alkyl styrene by the catalytic dehydrogenation of tertiary butylethylbenzene in the presence of catalysts containing iron oxides under conditions which minimize the undesirable thermal degradation of the raw material and the product while maintaining good yield and selectivity with low production of by-products. Specifically, it has been discovered that these desired results may be obtained by conducting the subject reaction at relatively low temperatures of between about 1000.degree. F. and about 1100.degree. F. and by maintaining a low partial pressure (i.e., not greater than about 0.5 psi) of the alkyl ethylbenzene in the reaction mixture. The desired partial pressure of the alkyl ethylbenzene is obtained by carrying out the catalytic reaction at a pressure of between about 1 psia and about 30 psia with steam as a diluent, the weight ratio of steam to alkyl ethylbenzene being between about 3 and about 30.
    • 本发明涉及在含有氧化铁的催化剂的存在下,通过叔丁基乙苯的催化脱氢来制备烷基苯乙烯的气相方法,该条件使原料和产物的不期望的热降解最小化,同时保持良好的产率, 低生产副产品的选择性。 具体地,已经发现,通过在约1000°F至约1100°F的相对低的温度下进行目标反应并且通过保持低的分压(即不大于约0.5 psi)的反应混合物中的烷基乙苯。 烷基乙苯的所需分压通过在蒸汽作为稀释剂的约1psia至约30psia的压力下进行催化反应,蒸汽与烷基乙苯的重量比在约3至约30之间获得。
    • 6. 发明授权
    • Process for the production of tertiary butylethylbenzene
    • 生产叔丁基乙基苯的方法
    • US5434325A
    • 1995-07-18
    • US277787
    • 1994-07-20
    • Shiou-Shan ChenJoseph C. Peters
    • Shiou-Shan ChenJoseph C. Peters
    • C07C2/66
    • C07C2/66C07C2529/70Y02P20/582
    • The present invention provides an alkylation process which is highly selective towards the production of para-tertiarybutylethylbenzene in high yield and in high para isomer content, while minimizing the development of unwanted by-products and impurities during the alkylation reaction. In accordance with the process, a feed stream mixture comprising the olefin alkylating agent and a molar excess of an aromatic hydrocarbon substrate is introduced into the inlet of a reactor zone and through a bed of active zeolite alkylation catalyst under alkylation conditions such that substantially all of the olefin reacts with the aromatic substrate to produce a mixture comprising the alkylated product and unreacted aromatic compound. This mixture is continuously withdrawn from the reactor zone as reactor effluent, after which the effluent is split into a product stream and recycle stream. The recycle stream is continuously recirculated back into the inlet of said reactor zone, preferably after being first combined with fresh feed stream mixture, in an amount such that the quantity of said aromatic compound and said olefin present in said reaction zone prior to contact with said catalyst is maintained at a preferred mole ratio greater than 10 to 1.
    • 本发明提供了一种烷基化方法,其以高产率和高对位异构体含量生产对 - 叔丁基苯是高选择性的,同时最小化烷基化反应期间不期望的副产物和杂质的发展。 根据该方法,将包含烯烃烷基化剂和摩尔过量的芳烃底物的进料流混合物在烷基化条件下引入反应器区的入口并通过活性沸石烷基化催化剂床,使得基本上全部 烯烃与芳族底物反应产生包含烷基化产物和未反应的芳族化合物的混合物。 将该混合物作为反应器流出物从反应器区域连续取出,然后将流出物分成产物流和再循环流。 再循环流连续再循环回所述反应器区的入口,优选在与新鲜进料流混合物首次混合之后,其量使得所述芳族化合物和所述烯烃在与所述反应区接触之前存在于所述反应区中的量 催化剂保持在大于10比1的优选摩尔比。