Process for making an acid-base leached zeolite catalyst
    21.
    发明授权
    Process for making an acid-base leached zeolite catalyst 失效
    制造酸碱浸出沸石催化剂的方法

    公开(公告)号:US5952259A

    公开(公告)日:1999-09-14

    申请号:US104951

    申请日:1998-06-25

    摘要: A catalyst composition and a process for converting a hydrocarbon stream such as, for example, gasoline to olefins and C.sub.6 to C.sub.8 aromatic hydrocarbons such as toluene and xylenes are disclosed. The catalyst composition comprises an alumina and a silica wherein the weight ratio of aluminum to silicon is in the range of from about 0.002:1 to about 0.25:1. The process comprises contacting a hydrocarbon stream with the catalyst composition under a condition sufficient to effect the conversion of a hydrocarbon to an olefin and a C.sub.6 to C.sub.8 aromatic hydrocarbon. Also disclosed is a process for producing the catalyst composition which comprises: (1) contacting a zeolite with an effective amount of a base under a condition sufficient to effect a reduction in silicon content of said zeolite to produce a base-leached zeolite; and (2) contacting said base-leached zeolite with an effective amount of an acid under a condition sufficient to effect a reduction in aluminum content of said base-leached zeolite.

    摘要翻译: 公开了一种催化剂组合物和用于将烃流例如汽油转化为烯烃和C 6至C 8芳族烃如甲苯和二甲苯的方法。 催化剂组合物包含氧化铝和二氧化硅,其中铝与硅的重量比在约0.002:1至约0.25:1的范围内。 该方法包括使烃流与催化剂组合物在足以使烃转化为烯烃和C 6至C 8芳烃的条件下接触。 还公开了一种制备催化剂组合物的方法,其包括:(1)在足以使所述沸石的硅含量降低以产生碱浸出的沸石的条件下使沸石与有效量的碱接触; 和(2)在足以实现所述碱浸出的沸石的铝含量降低的条件下使所述碱浸出的沸石与有效量的酸接触。

    Hydrotreating catalyst composition and processes therefor and therewith
    23.
    发明授权
    Hydrotreating catalyst composition and processes therefor and therewith 失效
    加氢处理催化剂组合物及其工艺及其

    公开(公告)号:US5856608A

    公开(公告)日:1999-01-05

    申请号:US803909

    申请日:1997-02-21

    摘要: A catalyst composition and a process for converting a C.sub.9 + aromatic compound such as, for example, 1,2,4-trimethylbenzene to a C.sub.6 to C.sub.8 aromatic hydrocarbon such as a xylene are disclosed. The composition comprises a zeolite, a metal oxide, and optionally a selectivity modifier selected from the group consisting of silicon, sulfur, phosphorus, boron, magnesium, tin, titanium, zirconium, germanium, indium, lanthanum, cesium, oxides thereof and combinations of any two or more thereof. The process comprises contacting a fluid which comprises a C.sub.9 + aromatic compound with the catalyst composition under a condition sufficient to effect the conversion of a C.sub.9 + aromatic compound to a C.sub.6 to C.sub.8 aromatic hydrocarbon.

    摘要翻译: 公开了一种催化剂组合物和将C 9+芳族化合物例如1,2,4-三甲基苯转化为C 6〜C 8芳烃如二甲苯的方法。 组合物包含沸石,金属氧化物和任选的选自硅,硫,磷,硼,镁,锡,钛,锆,锗,铟,镧,铯,氧化物的选择性改性剂和 其任何两个或多个。 该方法包括在足以使C 9+芳族化合物转化为C 6至C 8芳族烃的条件下使包含C 9+芳族化合物的流体与催化剂组合物接触。

    Catalyst composition and processes therefor and therewith
    25.
    发明授权
    Catalyst composition and processes therefor and therewith 失效
    催化剂组合物及其工艺及其

    公开(公告)号:US5714659A

    公开(公告)日:1998-02-03

    申请号:US705917

    申请日:1996-08-29

    IPC分类号: C07C4/18 C07C4/11

    摘要: A catalyst composition and a process for hydrodealkylating a C.sub.9 + aromatic compound such as, for example, 1,2,4-trimethylbenzene to a C.sub.6 to C.sub.8 aromatic hydrocarbon such as a xylene are disclosed. The composition comprises an alumina, a metal oxide, and a acid site modifier selected from the group consisting of silicon oxides, boron oxides magnesium oxides, tin oxides, titanium oxides, zirconium oxides, molybdenum oxides, germanium oxides, indium oxides, lanthanum oxides, cesium oxides, and combinations of any two or more thereof. The process comprises contacting a fluid which comprises a C.sub.9 + aromatic compound with the catalyst composition under a condition sufficient to effect the conversion of a C.sub.9 + aromatic compound to a C.sub.6 to C.sub.8 aromatic hydrocarbon.

    摘要翻译: 公开了一种催化剂组合物和将C 9+芳族化合物例如1,2,4-三甲基苯加氢脱烷基化成C6-C8芳族烃如二甲苯的方法。 该组合物包含氧化铝,金属氧化物和酸性位点改性剂,其选自氧化硅,氧化硼,氧化镁,氧化锡,氧化钛,氧化锆,氧化钼,氧化锗,氧化铟,氧化镧, 氧化铯,以及它们的任何两种或更多种的组合。 该方法包括在足以使C 9+芳族化合物转化为C 6至C 8芳族烃的条件下使包含C 9+芳族化合物的流体与催化剂组合物接触。

    Selective para-xylene production via methylation of toluene with methanol in the presence of modified HZSM-5 catalyst
    27.
    发明授权
    Selective para-xylene production via methylation of toluene with methanol in the presence of modified HZSM-5 catalyst 有权
    在改性HZSM-5催化剂存在下,甲醇与甲醇甲基化反应选择性对二甲苯

    公开(公告)号:US07049260B2

    公开(公告)日:2006-05-23

    申请号:US10453679

    申请日:2003-06-03

    IPC分类号: B01J29/06 B01J29/40

    摘要: We disclose a method for converting toluene to xylenes, comprising contacting toluene with methanol in the presence of a silica-bound HZSM-5 catalyst. As an example, in one embodiment the method can include: (i) first silylating HZSM-5, to form silylated HZSM-5; (ii) first calcining the silylated HZSM-5, to form calcined silylated HZSM-5; (iii) binding the calcined silylated HZSM-5 to silica, to form silica-bound calcined silylated HZSM-5; (iv) extruding the silica-bound calcined silylated HZSM-5, to form extruded silica-bound calcined silylated HZSM-5; (v) second calcining the extruded silica-bound calcined silylated HZSM-5, to form extruded silica-bound twice-calcined silylated HZSM-5; (vi) second silylating the extruded silica-bound twice-calcined silylated HZSM-5, to form extruded silica-bound twice-calcined twice-silylated HZSM-5; and (vii) third calcining the extruded silica-bound twice-calcined twice-silylated HZSM-5, to form the silica-bound HZSM-5 catalyst.

    摘要翻译: 我们公开了将甲苯转化为二甲苯的方法,包括在二氧化硅结合的HZSM-5催化剂存在下使甲苯与甲醇接触。 作为示例,在一个实施方案中,该方法可以包括:(i)首先使甲硅烷基化HZSM-5,以形成甲硅烷基化的HZSM-5; (ii)首先煅烧甲硅烷基化HZSM-5,形成煅烧甲硅烷基化HZSM-5; (iii)将煅烧的甲硅烷基化HZSM-5与二氧化硅结合,形成二氧化硅结合的煅烧甲硅烷基化HZSM-5; (iv)挤出二氧化硅结合的煅烧甲硅烷基化HZSM-5,以形成挤出的二氧化硅结合的煅烧甲硅烷基化HZSM-5; (v)第二次煅烧挤出的二氧化硅结合的煅烧甲硅烷基化HZSM-5,以形成挤出的二氧化硅结合的二次煅烧的甲硅烷基化HZSM-5; (vi)将挤出的二氧化硅结合的二次煅烧的甲硅烷基化HZSM-5二甲硅烷基化,以形成挤出的二氧化硅结合的二次煅烧的二次甲硅烷基化的HZSM-5; 和(vii)第三次煅烧挤出的二氧化硅结合的二次煅烧的二次甲硅烷基化的HZSM-5,以形成二氧化硅结合的HZSM-5催化剂。

    Syngas conversion and catalyst system employed therefor
    28.
    发明授权
    Syngas conversion and catalyst system employed therefor 有权
    合成气转化和催化剂体系

    公开(公告)号:US06638892B1

    公开(公告)日:2003-10-28

    申请号:US10125661

    申请日:2002-04-18

    IPC分类号: B01J2300

    摘要: A process for the conversion of syngas by contact of syngas under conversion conditions with catalyst having as components zinc oxide, copper oxide, aluminum oxide, Y zeolite and clay in which (A) in a one step process for conversion of syngas to dimethyl ether, the catalyst has as components an extruded mixture of zinc oxide, copper oxide, gamma aluminum oxide, Y zeolite and clay; (B) in a two step process for conversion of syngas to light olefins, a catalyst system is employed that has in the first step a catalyst mixture of zinc oxide, copper oxide, aluminum oxide, Y zeolite and clay and the catalyst employed in the second step is SAPO-34; SAPO-34 modified with lanthanum(III) nitrate hexahydrate; SAPO-34 modified with magnesium nitrate hexahydrate; SAPO-34 modified with tributyl borate or SAPO-34 modified with triethyl phosphate or (C) in a two step process for conversion of syngas to light olefins, the pressure on the effluent from the contact of syngas with a mixture of zinc oxide, copper oxide, aluminum oxide, Y zeolite and clay is reduced before contact with a second catalyst of SAPO-34. The catalyst systems employed in the processes herein.

    摘要翻译: 通过合成气在转化条件下与作为组分氧化锌,氧化铜,氧化铝,Y沸石和粘土的组分的催化剂接触合成气的方法,其中(A)在将合成气转化为二甲醚的一步法中, 催化剂具有氧化锌,氧化铜,γ氧化铝,Y沸石和粘土的挤出混合物的组分; (B)在将合成气转化为轻质烯烃的两步法中,采用了催化剂体系,该催化剂体系在第一步中是氧化锌,氧化铜,氧化铝,Y沸石和粘土的催化剂混合物, 第二步是SAPO-34; 用硝酸镧(III)六水合物修饰的SAPO-34; SAPO-34用硝酸镁六水合物改性; 用硼酸三丁酯或用三乙基磷酸酯改性的SAPO-34改性的SAPO-34或(C)在将合成气转化为轻质烯烃的两步法中,合成气与氧化锌,铜的混合物接触的流出物的压力 氧化物,氧化铝,Y沸石和粘土在与SAPO-34的第二催化剂接触之前还原。 本文工艺中使用的催化剂体系。

    Catalyst composition and processes therefor and therewith
    29.
    发明授权
    Catalyst composition and processes therefor and therewith 失效
    催化剂组合物及其工艺及其

    公开(公告)号:US06528450B2

    公开(公告)日:2003-03-04

    申请号:US09255973

    申请日:1999-02-23

    IPC分类号: B01J2108

    摘要: A catalyst composition and a process for hydrodealkylating a C9+ aromatic compound such as, for example, 1,2,4-trimethylbenzene to a C6 to C8 aromatic hydrocarbon such as a xylene are disclosed. The composition comprises an alumina, a metal oxide, and a coke suppressor selected from the group consisting of silicon oxides, phosphorus oxides, boron oxides, magnesium oxides, tin oxides, titanium oxides, zirconium oxides, molybdenum oxides, germanium oxides, indium oxides, lanthanum oxides, cesium oxides, and combinations of any two or more thereof. The process comprises contacting a fluid which comprises a C9+ aromatic compound with the catalyst composition under a condition sufficient to effect the conversion of a C9+ aromatic compound to a C6 to C8 aromatic hydrocarbon.

    摘要翻译: 公开了一种催化剂组合物和将C 9+芳族化合物例如1,2,4-三甲基苯加氢脱烷基化成C6-C8芳族烃如二甲苯的方法。 该组合物包含氧化铝,金属氧化物和选自氧化硅,氧化磷,氧化硼,氧化镁,氧化锡,氧化钛,氧化锆,氧化钼,氧化锗,氧化铟, 氧化镧,氧化铯及其任意两种以上的组合。 该方法包括在足以使C 9+芳族化合物转化为C 6至C 8芳族烃的条件下使包含C 9+芳族化合物的流体与催化剂组合物接触。

    Hydrocarbon hydrogenation catalyst and process

    公开(公告)号:US06436863B1

    公开(公告)日:2002-08-20

    申请号:US09730310

    申请日:2000-12-05

    IPC分类号: B01J2904

    摘要: A catalyst composition and process for preparing such catalyst composition which can be useful in contacting a hydrocarbon-containing fluid which contains a highly unsaturated hydrocarbon such as 1,3-butadiene, in the presence of hydrogen, with such catalyst composition in a hydrogenation zone under a hydrogenation condition effective to hydrogenate such highly unsaturated hydrocarbon to a less unsaturated hydrocarbon such as n-butene is disclosed. Such process for preparing a catalyst composition includes (1) combining a zeolite, a Group VIB metal, and an inorganic support to form a modified zeolite; (2) calcining such modified zeolite under a calcining condition to produce a calcined, modified zeolite; and (3) contacting such calcined, modified zeolite with a carburizing agent under a carburizing condition to provide such catalyst composition.