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    • 21. 发明授权
    • Monoalkylated aromatic compound production
    • 单烷基化芳香族化合物生产
    • US08247629B2
    • 2012-08-21
    • US12299508
    • 2007-04-17
    • Michael C. ClarkChristine N. EliaFrederick Y. LoYun-Feng Chang
    • Michael C. ClarkChristine N. EliaFrederick Y. LoYun-Feng Chang
    • C07C2/66C07C6/12
    • C07C2/66B01J29/06B01J29/70B01J29/7007B01J29/7038B01J35/002B01J35/026B01J37/0009B01J37/0045B01J2229/42C10G29/205C10G2300/1092C10G2300/1096C10G2300/4018C10G2300/4056C10G2400/30C07C15/02
    • A process for producing a monoalkylated aromatic compound in an alkylation reaction zone, said process comprising the steps of: (a) providing a first catalytic particulate material having a ratio of surface area over volume ratio greater than about 79 cm−1, (b) providing said alkylation reaction zone with an alkylatable aromatic compound, an alkylating agent, and said first catalytic particulate material; and (c) contacting said alkylatable aromatic compound and said alkylating agent with said catalytic particulate material in said alkylation reaction zone maintained under alkylation conditions, to form a product comprised of said monoalkylated aromatic compound and polyalkylated aromatic compound(s). The molar ratio of said polyalkylated aromatic compound(s) over said monoalkylated aromatic compound produced by said first catalytic particulate material is less than the molar ratio of polyalkylated aromatic compound(s) over monoalkylated aromatic compound produced by a second catalytic particulate material and said alkylation reaction zone is operated under the same alkylation conditions, wherein at least 51 wt. % of said second catalytic particulate material having a ratio of surface area over volume between 78 and 79 cm−1.
    • 一种在烷基化反应区中制备单烷基化芳族化合物的方法,所述方法包括以下步骤:(a)提供具有大于约79cm -1的体积比的表面积比率的第一催化颗粒材料,(b) 向所述烷基化反应区提供可烷基化芳族化合物,烷基化剂和所述第一催化颗粒材料; 和(c)使所述烷基化芳族化合物和所述烷基化剂与所述烷基化反应区中的所述催化颗粒材料接触,所述烷基化反应区保持在烷基化条件下,以形成由所述单烷基化芳族化合物和多烷基化芳族化合物组成的产物。 所述多烷基化芳族化合物与所述第一催化颗粒材料制备的所述单烷基化芳族化合物的摩尔比小于由第二催化颗粒材料制备的多烷基化芳族化合物与单烷基化芳族化合物的摩尔比,并且所述烷基化 反应区在相同的烷基化条件下操作,其中至少51wt。 所述第二催化颗粒材料的%具有在78和79cm -1之间的体积上的表面积比。
    • 23. 发明申请
    • Monoalkylated Aromatic Compound Production
    • 单烷基化芳香族化合物生产
    • US20090306446A1
    • 2009-12-10
    • US12299508
    • 2007-04-17
    • Michael C. ClarkChristine N. EliaFrederick Y. LoYun-Feng Chang
    • Michael C. ClarkChristine N. EliaFrederick Y. LoYun-Feng Chang
    • C07C2/66
    • C07C2/66B01J29/06B01J29/70B01J29/7007B01J29/7038B01J35/002B01J35/026B01J37/0009B01J37/0045B01J2229/42C10G29/205C10G2300/1092C10G2300/1096C10G2300/4018C10G2300/4056C10G2400/30C07C15/02
    • A process for producing a monoalkylated aromatic compound in an alkylation reaction zone, said process comprising the steps of: (a) providing a first catalytic particulate material having a ratio of surface area over surface volume ratio greater than about 79 cm−1, (b) providing said alkylation reaction zone with an alkylatable aromatic compound, an alkylating agent, and said first catalytic particulate material; and (c) contacting said alkylatable aromatic compound and said alkylating agent with said catalytic particulate material in said alkylation reaction zone maintained under alkylation conditions, to form a product comprised of said monoalkylated aromatic compound and polyalkylated aromatic compound(s). The molar ratio of said polyalkylated aromatic compound(s) over said monoalkylated aromatic compound produced by said first catalytic particulate material is less than the molar ratio of polyalkylated aromatic compound(s) over monoalkylated aromatic compound produced by a second catalytic particulate material and said alkylation reaction zone is operated under the same alkylation conditions, wherein at least 51 wt. % of said second catalytic particulate material having a ratio of surface area over surface volume between 78 and 79 cm−1.
    • 一种在烷基化反应区中制备单烷基化芳族化合物的方法,所述方法包括以下步骤:(a)提供具有大于约79cm -1的表面体积比的表面积比例的第一催化颗粒材料,(b )向所述烷基化反应区提供可烷基化芳族化合物,烷基化剂和所述第一催化颗粒材料; 和(c)使所述烷基化芳族化合物和所述烷基化剂与所述烷基化反应区中的所述催化颗粒材料接触,所述烷基化反应区保持在烷基化条件下,以形成由所述单烷基化芳族化合物和多烷基化芳族化合物组成的产物。 所述多烷基化芳族化合物与所述第一催化颗粒材料制备的所述单烷基化芳族化合物的摩尔比小于由第二催化颗粒材料制备的多烷基化芳族化合物与单烷基化芳族化合物的摩尔比和所述烷基化 反应区在相同的烷基化条件下操作,其中至少51wt。 所述第二催化颗粒材料的百分比具有在78和79cm -1之间的表面积之比。
    • 28. 发明授权
    • Vapor phase aromatics alkylation process
    • 气相芳烃烷基化方法
    • US07498474B2
    • 2009-03-03
    • US11362255
    • 2006-02-27
    • Benjamin S. UmanskyMichael C. ClarkAjit B. DandekarChristine N. Elia
    • Benjamin S. UmanskyMichael C. ClarkAjit B. DandekarChristine N. Elia
    • C07C2/66
    • C10G29/205
    • A process for the production of high octane number gasoline from light refinery olefins and benzene-containing aromatic streams such as reformate. The process achieves good utilization of both the ethylene and the propylene present in the mixed olefin feed from the unsaturated gas plant while reducing gasoline benzene levels. The light olefins including ethylene and propylene are reacted with the light aromatic stream containing benzene and other single ring aromatic compounds to form a gasoline boiling range product containing akylaromatics. The reaction is carried out with a two-catalyst system which comprises a member of the MWW family of zeolites and an intermediate pore size zeolite such as ZSM-5 using a fixed catalyst bed in both stages. Use of the two catalyst system enables the conversion of the ethylene and propylene components of the olefin feed to be converted to alkylaromatics under favorable conditions.
    • 一种从轻质炼油烯烃和含苯芳族物流如重整油生产高辛烷值汽油的方法。 该方法可以很好地利用来自不饱和气体装置的混合烯烃进料中存在的乙烯和丙烯,同时降低汽油苯的含量。 包括乙烯和丙烯的轻质烯烃与含有苯和其它单环芳族化合物的轻芳烃物流反应,形成含烷基芳族化合物的汽油沸程产品。 该反应用两催化剂体系进行,该双催化剂体系包括MWW沸石族的成员和中等孔径的沸石如ZSM-5,其使用两个阶段的固定催化剂床。 使用这两种催化剂体系可使烯烃进料的乙烯和丙烯成分转化成有利条件下的烷基芳族化合物。