Hydrocracking process
    1.
    发明授权
    Hydrocracking process 失效
    加氢裂化过程

    公开(公告)号:US4971680A

    公开(公告)日:1990-11-20

    申请号:US287399

    申请日:1988-12-20

    摘要: A hydrocarbon conversion process is disclosed involving the hydrocracking of a catalytic cycle oil in the presence of a catalyst having a nickel component, a tungsten component, and a support component containing a crystalline molecular sieve material present in an amount ranging from about 25 to about 60 wt. % based on the weight of the support component wherein at least about 1 to about 80 wt. % of the sieve material is a gallosilicate, based on the total weight of the sieve component.

    摘要翻译: 公开了一种烃转化方法,其涉及在具有镍组分,钨组分和含有结晶分子筛材料的载体组分的催化剂存在下催化循环油的加氢裂化,所述结晶分子筛材料的存在量为约25至约60 重量 基于支持组分的重量,其中至少约1至约80重量% 基于筛组分的总重量,筛材料的百分比是硅酸盐。

    Distillate hydrogenation
    2.
    发明授权
    Distillate hydrogenation 失效
    馏分氢化

    公开(公告)号:US5271828A

    公开(公告)日:1993-12-21

    申请号:US851311

    申请日:1992-03-16

    摘要: A process and catalyst is provided for the hydrogenation of a hydrocarbon feedstock comprising a substantial portion of a distillate hydrocarbon feedstock, wherein said distillate hydrocarbon feedstock consists essentially of material boiling between about 150.degree. F. and about 700.degree. F. at atmospheric pressure, which comprises reacting the feedstock with hydrogen at hydrogenation conditions in the presence of a catalyst comprising from about 0.1% to about 2.0% by weight of palladium and from about 0.1% to about 2.0% by weight of platinum and a support comprising borosilicate, for producing a hydrogenated product.

    摘要翻译: 提供了一种方法和催化剂用于包含大部分馏出物烃原料的烃原料的氢化,其中所述馏出物烃原料基本上由在大气压下沸点在约150°F至约700°F之间的材料组成,其中 包括在氢化条件下在催化剂存在下使原料与氢反应,所述催化剂包含约0.1重量%至约2.0重量%的钯和约0.1重量%至约2.0重量%的铂和包含硼硅酸盐的载体,用于生产 氢化产物。

    Distillate hydrogenation
    3.
    发明授权
    Distillate hydrogenation 失效
    馏分氢化

    公开(公告)号:US5151172A

    公开(公告)日:1992-09-29

    申请号:US695426

    申请日:1991-05-03

    IPC分类号: C10G45/54

    CPC分类号: C10G45/54

    摘要: A process and catalyust are provided for hydrogenation of a hydrocarbon feedstock consisting essentially of material boiling between about 150.degree. F. and about 700.degree. F. which comprises reacting the feedstock with hydrogen at hydrogenation conditions in the presence of a catalyst comprising from about 0.1% to about 2.0% by weight each of palladium and platinum and a support comprising mordenite. The process of the present invention provides substantially improved dearomatization performance, increased desulfurization and denitrogenation, increased distillate product cetane number, increased distllate volume expansion, and utilizes a more durable catalyst.

    摘要翻译: 提供了一种方法和催化剂,用于氢化烃原料,其基本上由沸点在约150°F至约700°F之间的材料进行氢化,其包括在氢化条件下使原料与氢气在催化剂存在下反应,所述催化剂包含约0.1% 至约2.0重量%的钯和铂,以及包含丝光沸石的载体。 本发明的方法提供了显着改进的脱芳构化性能,增加的脱硫和脱氮,增加的馏出物产品十六烷值,增加的二馏液体积膨胀,并且使用更耐用的催化剂。

    Distillate hydrogenation catalyst
    4.
    发明授权
    Distillate hydrogenation catalyst 失效
    馏分氢化催化剂

    公开(公告)号:US5308814A

    公开(公告)日:1994-05-03

    申请号:US880492

    申请日:1992-05-08

    IPC分类号: B01J29/12 C10G45/54 B01J29/10

    CPC分类号: B01J29/126 C10G45/54

    摘要: A process and catalyst are provided for hydrogenation of a hydrocarbon feedstock consisting essentially of material boiling between about 150.degree. F. and about 700.degree. F. which comprises reacting the feedstock with hydrogen at hydrogenation conditions in the presence of a catalyst comprising hydrogenation metals and a support comprising zeolite Y. The hydrogenation metals comprise from about 0.1 percent to about 2.0 percent by weight each of palladium and platinum calculated as a percentage of the catalyst. The zeolite Y further comprises sodium in an amount ranging from about 1.5 to about 8.0 percent of the zeolite Y by weight. The process of the present invention provides substantially improved dearomatization performance, increased desulfurization and denitrogenation, increased distillate product cetane number, and increased distillate volume expansion.

    摘要翻译: 提供了一种方法和催化剂,用于氢化烃原料,其基本上由沸点在约150°F至约700°F之间的材料进行氢化,其包括在氢化条件下,在包含氢化金属和 包含沸石Y的载体。氢化金属包含按催化剂的百分比计算的钯和铂的约0.1重量%至约2.0重量%。 沸石Y还包含按重量计约沸石Y的约1.5至约8.0%的量的钠。 本发明的方法提供了显着改善的脱芳构化性能,增加的脱硫和脱氮,增加的馏出物产品十六烷值和增加的馏出物体积膨胀。

    Selective hydrotreating
    5.
    发明授权
    Selective hydrotreating 失效
    选择性加氢处理

    公开(公告)号:US5266188A

    公开(公告)日:1993-11-30

    申请号:US803131

    申请日:1991-12-05

    IPC分类号: B01J23/85 C10G45/08 C10G23/02

    CPC分类号: B01J23/85 C10G45/08

    摘要: A process, catalyst, and method of making a catalyst are provided for the selective hydrotreating of a selective hydrotreating feedstock comprising reacting the feedstock with hydrogen at hydrotreating conditions in the presence of a catalyst comprising a hydrogenation component and a support component. The hydrogenation component comprises a Group VIB metal component and a Group VIII metal component wherein the Group VIB metal component is present in an amount ranging from about 4 wt % to about 20 wt % and the Group VIII metal component is present in an amount ranging from about 0.5 wt % to about 10 wt %, both calculated as oxides and based on the total catalyst weight. The support component comprises from about 0.5 wt % to about 50 wt % of a magnesium component and from about 0.02 wt % to about 10 wt % of an alkali metal component, both calculated as oxides and based on the total catalyst weight. The present invention provides a process, catalyst, and method of making a catalyst resulting in higher selective hydrotreating feedstock octane at high levels of desulfurization, among numerous other benefits.

    摘要翻译: 提供了一种制备催化剂的方法,催化剂和方法,用于选择性加氢处理选择性加氢处理原料,包括在加氢处理条件下使原料与氢气在含氢化组分和载体组分的催化剂存在下反应。 氢化组分包括VIB族金属组分和VIII族金属组分,其中VIB族金属组分的存在量为约4重量%至约20重量%,第VIII族金属组分的存在量范围为 约0.5重量%至约10重量%,均以氧化物计,基于总催化剂重量计算。 载体组分包含约0.5重量%至约50重量%的镁组分和约0.02重量%至约10重量%的碱金属组分,两者以氧化物计,基于总催化剂重量计。 本发明提供一种制备催化剂的方法,催化剂和方法,其产生较高选择性加氢处理高脱硫水平的原料辛烷等许多益处。

    Distillate hydrogenation catalyst
    6.
    发明授权
    Distillate hydrogenation catalyst 失效
    馏分氢化催化剂

    公开(公告)号:US5494870A

    公开(公告)日:1996-02-27

    申请号:US232731

    申请日:1994-04-25

    IPC分类号: B01J29/74 C10G45/54 B01J29/06

    CPC分类号: C10G45/54 B01J29/7415

    摘要: A process and catalyst are provided for the hydrogenation of a hydrocarbon feedstock consisting essentially of hydrocarbon boiling between about 150.degree. F. and 700.degree. F. at atmospheric pressure. The process comprises reacting the feedstock with hydrogen at hydrogenation conditions in the presence of a catalyst comprising hydrogenation metals and a support comprising beta zeolite. The hydrogenation metals comprise from about 0.1 percent by weight to about 2.0 percent by weight each of palladium and platinum measured as a percentage of the catalyst. The beta zeolite comprises from about 1 ppm by weight to about 3.0 percent by weight sodium calculated as a percentage of said beta zeolite.

    摘要翻译: 提供了一种方法和催化剂,用于氢化烃原料,其基本上由在大气压下在约150°F和700°F之间沸腾的烃组成。 该方法包括在氢化条件下,在包含氢化金属的催化剂和包含β沸石的载体存在下使原料与氢反应。 氢化金属包含以催化剂的百分比测量的钯和铂的约0.1重量%至约2.0重量%。 β-沸石包含以所述β沸石的百分数计算的约1ppm至约3.0重量%的钠。

    Distillate hydrogenation
    7.
    发明授权
    Distillate hydrogenation 失效
    馏分氢化

    公开(公告)号:US5346874A

    公开(公告)日:1994-09-13

    申请号:US104780

    申请日:1993-08-10

    摘要: A process and catalyst is provided for the hydrogenation of a hydrocarbon feedstock comprising a substantial portion of a distillate hydrocarbon feedstock, wherein said distillate hydrocarbon feedstock consists essentially of material boiling between about 150.degree. F. and about 700.degree. F. at atmospheric pressure, which comprises reacting the feedstock with hydrogen at hydrogenation conditions in the presence of a catalyst comprising from about 0.1% to about 2.0% by weight of palladium and from about 0.1% to about 2.0% by weight of platinum and a support comprising borosilicate, for producing a hydrogenated product.

    摘要翻译: 提供了一种方法和催化剂用于包含大部分馏出物烃原料的烃原料的氢化,其中所述馏出物烃原料基本上由在大气压下沸点在约150°F至约700°F之间的材料组成,其中 包括在氢化条件下在催化剂存在下使原料与氢反应,所述催化剂包含约0.1重量%至约2.0重量%的钯和约0.1重量%至约2.0重量%的铂和包含硼硅酸盐的载体,用于生产 氢化产物。

    Distillate hydrogenation utilizing a catalyst comprising platinum,
palladium, and a beta zeolite support
    8.
    发明授权
    Distillate hydrogenation utilizing a catalyst comprising platinum, palladium, and a beta zeolite support 失效
    使用包含铂,钯和β沸石载体的催化剂进行馏出氢化

    公开(公告)号:US5346612A

    公开(公告)日:1994-09-13

    申请号:US21530

    申请日:1993-02-19

    CPC分类号: C10G45/54 B01J29/7415

    摘要: A process and catalyst are provided for the hydrogenation of a hydrocarbon feedstock consisting essentially of hydrocarbon boiling between about 150.degree. F. and 700.degree. F. at atmospheric pressure. The process comprises reacting the feedstock with hydrogen at hydrogenation conditions in the presence of a catalyst comprising hydrogenation metals and a support comprising beta zeolite. The hydrogenation metals comprise from about 0.1 percent by weight to about 2.0 percent by weight each of palladium and platinum measured as a percentage of the catalyst. The beta zeolite comprises from about 1 ppm by weight to about 3.0 percent by weight sodium calculated as a percentage of said beta zeolite.

    摘要翻译: 提供了一种方法和催化剂,用于氢化烃原料,其基本上由在大气压下在约150°F和700°F之间沸腾的烃组成。 该方法包括在氢化条件下,在包含氢化金属的催化剂和包含β沸石的载体存在下使原料与氢反应。 氢化金属包含以催化剂的百分比测量的钯和铂的约0.1重量%至约2.0重量%。 β-沸石包含以所述β沸石的百分数计算的约1ppm至约3.0重量%的钠。

    Distillate hydrogenation catalyst
    9.
    发明授权
    Distillate hydrogenation catalyst 失效
    馏分氢化催化剂

    公开(公告)号:US5225383A

    公开(公告)日:1993-07-06

    申请号:US876852

    申请日:1992-04-30

    IPC分类号: C10G45/54

    CPC分类号: C10G45/54

    摘要: A process and catalyst are provided for hydrogenation of a hydrocarbon feedstock consisting essentially of material boiling between about 150.degree. F. and about 700.degree. F. which comprises reacting the feedstock with hydrogen at hydrogenation conditions in the presence of a catalyst comprising from about 0.1% to about 2.0% by weight each of palladium and platinum and a support comprising mordenite. The process of the present invention provides substantially improved dearomatization performance, increased desulfurization and denitrogenation, increased distillate product cetane number, increased distillate volume expansion, and utilizes a more durable catalyst.

    摘要翻译: 提供了一种方法和催化剂,用于氢化烃原料,其基本上由沸点在约150°F至约700°F之间的材料进行氢化,其包括在氢化条件下使原料与氢气在催化剂存在下反应,所述催化剂包含约0.1% 至约2.0重量%的钯和铂,以及包含丝光沸石的载体。 本发明的方法提供了显着改进的脱芳构化性能,增加的脱硫和脱氮,增加的馏出物产品十六烷值,增加的馏出物体积膨胀,并且使用更耐用的催化剂。

    Distillate hydrogenation
    10.
    发明授权
    Distillate hydrogenation 失效
    馏分氢化

    公开(公告)号:US5147526A

    公开(公告)日:1992-09-15

    申请号:US769533

    申请日:1991-10-01

    IPC分类号: B01J29/12 C10G45/54

    CPC分类号: B01J29/126 C10G45/54

    摘要: A process and catalyst are provided for hydrogenation of a hydrocarbon feedstock consisting essentially of material boiling between about 150.degree. F. and about 700.degree. F. which comprises reacting the feedstock with hydrogen at hydrogenation conditions in the presence of a catalyst comprising hydrogenation metals and a support comprising zeolite Y. The hydrogenation metals comprise from about 0.1 percent to about 2.0 percent by weight each of palladium and platinum calculated as a percnetage of the catalyst. The zeolite Y further comprises sodium in an amount ranging from about 1.5 to about 8.0 percent of the zeolite Y by weight. The process of the present invention provides substantially improved dearomatization performance, increased desulfurization and denitrogenation, increased distillate product cetane number, and increased distillate volume expansion.

    摘要翻译: 提供了一种方法和催化剂,用于氢化烃原料,其基本上由沸点在约150°F至约700°F之间的材料进行氢化,其包括在氢化条件下,在包含氢化金属和 包含沸石Y的载体。氢化金属包含按催化剂的百分数计算的钯和铂的约0.1重量%至约2.0重量%。 沸石Y还包含按重量计约沸石Y的约1.5至约8.0%的量的钠。 本发明的方法提供了显着改进的脱芳构化性能,增加的脱硫和脱氮,增加的馏出物产品十六烷值和增加的馏出物体积膨胀。