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1.发明申请Alkylation Process Using a Catalyst Comprising a Solid Acid and a Hydrogenation Metal 有权使用包含固体酸和氢化金属的催化剂的烷基化方法公开(公告)号：US20070282149A1
公开(公告)日：2007-12-06
申请号：US10588106
申请日：2005-01-26
CPC分类号： C07C2/58 , B01J29/126 , B01J2229/42 , C10G29/20 , C10G29/205 , C10G2400/02 , Y10S585/906
摘要： The invention relates to a process for alkylating a hydrocarbon feed which comprises contacting the hydrocarbon feed to be alkylated with an alkylation agent in the presence of a catalyst comprising a solid acid, a hydrogenation metal, and 1.5-6 wt % of water, measured as the loss on ignition at 600° C. The presence of 1.5-6 wt % of water results in a higher activity and a higher alkylate quality compared with a comparable but drier catalyst.
摘要翻译： 本发明涉及烃类进料的烷基化方法，该方法包括使待烷基化的烃进料与烷基化试剂在含有固体酸，氢化金属和1.5-6重量％水的催化剂存在下接触，测量为 在600℃下的点火损失。与可比较但干燥的催化剂相比，存在1.5-6重量％的水导致更高的活性和更高的烷基化物质量。
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2.发明授权Alkylation process using a catalyst comprising a solid acid and a hydrogenation metal 有权使用包含固体酸和氢化金属的催化剂的烷基化方法公开(公告)号：US07750197B2
公开(公告)日：2010-07-06
申请号：US10588106
申请日：2005-01-26
CPC分类号： C07C2/58 , B01J29/126 , B01J2229/42 , C10G29/20 , C10G29/205 , C10G2400/02 , Y10S585/906
摘要： The invention relates to a process for alkylating a hydrocarbon feed which comprises contacting the hydrocarbon feed to be alkylated with an alkylation agent in the presence of a catalyst comprising a solid acid, a hydrogenation metal, and 1.5-6 wt % of water, measured as the loss on ignition at 600° C. The presence of 1.5-6 wt % of water results in a higher activity and a higher alkylate quality compared with a comparable but drier catalyst.
摘要翻译： 本发明涉及烃类进料的烷基化方法，该方法包括使待烷基化的烃进料与烷基化试剂在含有固体酸，氢化金属和1.5-6重量％水的催化剂存在下接触，测量为 在600℃下的点火损失。与可比较但干燥的催化剂相比，存在1.5-6重量％的水导致更高的活性和更高的烷基化物质量。
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公开(公告)号：US07176340B2
公开(公告)日：2007-02-13
申请号：US10163108
申请日：2002-06-05
CPC分类号： C07C2/58 , C07C2523/42 , C07C2523/44 , Y02P20/584
摘要： A continuous alkylation process performed in an apparatus comprising a series of at least two zone A reactors and a series of at least two zone B reactors, in which the zone A reactors and the zone B reactors cycle between alkylation mode and mild regeneration mode, and wherein the alkylation mode comprises introducing an alkylation agent into a first reactor of the zone through which the alkylatable compound passes, reacting a portion of the alkylatable compound with a portion of the alkylation agent to produce a product stream, and performing this operation at least once more in a downstream reactor in the same zone employing, instead of alkylatable compound, a stream comprising the product stream.
摘要翻译： 在包括一系列至少两个A区反应器和一系列至少两个B区反应器的装置中进行的连续烷基化方法，其中A区反应器和B区反应器在烷基化模式和温和再生模式之间循环，以及 其中所述烷基化模式包括将烷基化试剂引入所述可烷基化合物通过的区域的第一反应器中，使可烷基化合物的一部分与部分烷基化试剂反应以产生产物流，并进行至少一次 在同一区域的下游反应器中更多地使用代替可烷化化合物的包含产物流的物流。
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