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74 条记录 (耗时 0.022 秒)

    Hydrotreating olefin stream with complete destruction of oxygenates
    11.
    发明授权
    Hydrotreating olefin stream with complete destruction of oxygenates 有权
    加氢处理烯烃流完全破坏含氧化合物

    公开(公告)号：US06548721B1

    公开(公告)日：2003-04-15

    申请号：US09862897

    申请日：2001-05-22

    申请人： Beth Mc Culloch ,  Jennifer L. Gordon ,  Peter Kokayeff ,  Suheil F. Abdo ,  Daniel H. Wei

    发明人： Beth Mc Culloch ,  Jennifer L. Gordon ,  Peter Kokayeff ,  Suheil F. Abdo ,  Daniel H. Wei

    IPC分类号： C07C502

    CPC分类号： C07C7/163 ,  C07C2523/85 ,  C07C2523/883 ,  C07C2527/02 ,  C07C11/02

    摘要： Disclosed is a process for completely destroying oxygenates in a feed stream. The feed stream of oxygenates typically includes olefins and it is reacted with hydrogen over a catalyst comprising a top row of Group VIII metal and a Group VI-B metal. Olefins are essentially completely saturated and any sulfur compounds present in the feed are completely converted to hydrogen sulfide. A preferred catalyst includes 2 to 5 wt-% nickel, 5 to 15 wt-% molybdenum, at least 5.5 wt-% sulfur, less than 0.05 wt-% phosphorus and no more than 0.3 wt-% silicon. The catalyst has low acidity and therefore does not promote the cracking of desired oligomeric products. The deoxygenation process is preferably a saturation process that follows an oligomerization process in which light olefins are oligomerized to heavy olefins. The saturation catalyst preferably has lower acidity which causes minimal cracking of desired oligomeric products. However, by optimally raising the temperature of the outlet of the saturation reaction zone, excessively heavy oligomers can be cracked down to desirable heavy oligomers.

    摘要翻译： 公开了一种在进料流中完全破坏含氧化合物的方法。 含氧化合物的进料流通常包括烯烃，并且其与氢气在包含第一排VIII族金属和VI-B族金属的催化剂上反应。 烯烃基本上完全饱和，并且进料中存在的任何硫化合物完全转化成硫化氢。 优选的催化剂包括2至5重量％的镍，5至15重量％的钼，至少5.5重量％的硫，小于0.05重量％的磷和不超过0.3重量％的硅。 催化剂具有低酸度，因此不促进所需低聚产物的裂化。 脱氧方法优选是在轻烯烃低聚至重质烯烃的低聚方法之后的饱和方法。 饱和催化剂优选具有较低的酸度，这导致所需低聚产物的最小裂化。 然而，通过最佳地提高饱和反应区的出口的温度，过量的低聚物可以被裂化成所需的重低聚物。

    Hydrotreating with silicon removal
    12.
    发明授权
    Hydrotreating with silicon removal 失效
    加氢处理除硅

    公开(公告)号：US5118406A

    公开(公告)日：1992-06-02

    申请号：US693369

    申请日：1991-04-30

    申请人： Peter Kokayeff ,  Danford E. Clark ,  Howard D. Simpson

    发明人： Peter Kokayeff ,  Danford E. Clark ,  Howard D. Simpson

    IPC分类号： C10G45/08

    CPC分类号： C10G45/08

    摘要： A catalytic hydrotreating process wherein silicon-containing contaminants contained in a hydrocarbon feedstream are deposited onto a hydrotreating catalyst bed during hydrotreating in a manner providing improved catalyst stability. Hydrotreating catalysts having relatively high activities and low surface areas are located downstream of upstream hydrotreating catalysts having relatively low activities and high surface areas.

    摘要翻译： 催化加氢处理方法，其中包含在烃进料流中的含硅污染物以提供改进的催化剂稳定性的方式在加氢处理期间沉积在加氢处理催化剂床上。 具有较高活性和低表面积的加氢处理催化剂位于具有较低活性和高表面积的上游加氢处理催化剂的下游。

    Process and apparatus for producing diesel from a hydrocarbon stream
    13.
    发明授权
    Process and apparatus for producing diesel from a hydrocarbon stream 有权
    从烃流中生产柴油的方法和装置

    公开(公告)号：US08940253B2

    公开(公告)日：2015-01-27

    申请号：US13433701

    申请日：2012-03-29

    申请人： Paul R. Zimmerman ,  Peter Kokayeff

    发明人： Paul R. Zimmerman ,  Peter Kokayeff

    IPC分类号： C10G65/12

    CPC分类号： C10G65/12 ,  B01J19/24 ,  B01J2219/24 ,  C10G45/02 ,  C10G45/08 ,  C10G47/16 ,  C10G67/02 ,  C10G2300/1055 ,  C10G2300/4056 ,  C10G2400/04

    摘要： A process and apparatus are disclosed for hydrotreating a hydrocarbon feed in a hydrotreating unit and hydrocracking a second hydrocarbon stream in a hydrocracking unit. The hydrocracking unit and the hydrotreating unit may share the same recycle gas compressor. A make-up hydrogen stream may also be compressed in the recycle gas compressor. The second hydrocarbon stream may be a diesel stream from the hydrotreating unit. The diesel stream may be a diesel and heavier stream from a bottom of a hydrotreating fractionation column.

    摘要翻译： 公开了用于加氢处理加氢处理装置中的烃进料并加氢裂化加氢裂化装置中的第二烃流的方法和装置。 加氢裂化装置和加氢处理装置可以共用相同的循环气体压缩机。 补充氢气流也可以在循环气体压缩机中被压缩。 第二烃流可以是来自加氢处理单元的柴油流。 柴油流可以是来自加氢处理分馏塔的底部的柴油和较重物流。

    Production of diesel fuel from biorenewable feedstocks
    17.
    发明授权
    Production of diesel fuel from biorenewable feedstocks 有权
    生物可再生原料生产柴油

    公开(公告)号：US07999142B2

    公开(公告)日：2011-08-16

    申请号：US12193156

    申请日：2008-08-18

    申请人： Tom N. Kalnes ,  Terry L. Marker ,  John P. Brady ,  Peter Kokayeff

    发明人： Tom N. Kalnes ,  Terry L. Marker ,  John P. Brady ,  Peter Kokayeff

    IPC分类号： C07C4/00

    CPC分类号： C10L1/08 ,  C10G3/46 ,  C10G3/50 ,  C10G45/58 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/1022 ,  C10G2300/1037 ,  C10G2300/4081 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/28 ,  Y02E50/13 ,  Y02P30/20

    摘要： A process has been developed for producing diesel boiling range fuel from renewable feedstocks such as plant oils and animal oils, fats, and greases. The process involves treating a renewable feedstock by hydrogenating and deoxygenating i.e. decarboxylating, decarbonylating, and/or hydrodeoxygenating to provide a hydrocarbon fraction useful as a diesel boiling range fuel or diesel boiling range fuel blending component. If desired, the hydrocarbon fraction can be isomerized to improve cold flow properties. A portion of the hydrogenated and deoxygenated feedstock is selectively separated and then recycled to the treatment zone to increase the hydrogen solubility of the reaction mixture.

    摘要翻译： 已经开发了用于从可再生原料如植物油和动物油，脂肪和油脂生产柴油沸点燃料的方法。 该方法包括通过氢化和脱氧处理可再生原料，即脱羧，脱羰和/或加氢脱氧，以提供可用作柴油沸程燃料或柴油沸程燃料调配组分的烃馏分。 如果需要，烃馏分可以被异构化以改善冷流动性能。 氢化和脱氧原料的一部分被选择性分离，然后再循环到处理区以提高反应混合物的氢溶解度。

    HYDROCARBON CONVERSION PROCESS
    19.
    发明申请
    HYDROCARBON CONVERSION PROCESS 审中-公开
    石油转化过程

    公开(公告)号：US20110123406A1

    公开(公告)日：2011-05-26

    申请号：US13021214

    申请日：2011-02-04

    申请人： Peter Kokayeff ,  Laura E. Leonard ,  Michael R. Smith

    发明人： Peter Kokayeff ,  Laura E. Leonard ,  Michael R. Smith

    IPC分类号： B01J8/00

    CPC分类号： C10G65/04 ,  C10G65/12 ,  C10G2400/04

    摘要： A process is provided to produce an ultra low sulfur diesel with less than about 10 ppm sulfur using a two-phase or liquid-phase continuous reaction zone to convert a diesel boiling range distillate preferably obtained from a mild hydrocracking unit. In one aspect, the diesel boiling range distillate is introduced once-through to the liquid-phase continuous reaction zone over-saturated with hydrogen in an amount effective so that the liquid phase remains substantially saturated with hydrogen throughout the reaction zone as the reactions proceed.

    摘要翻译： 提供了一种使用两相或液相连续反应区产生具有小于约10ppm硫的超低硫柴油以转化优选从温和加氢裂化装置获得的柴油沸程馏出物的方法。 在一个方面，将柴油沸程馏出物一次性引入到用氢过饱和的液相连续反应区，其量是有效的，使得当反应进行时液相在整个反应区中基本上被氢饱和。

    Hydrocarbon conversion process
    20.
    发明授权
    Hydrocarbon conversion process 有权
    烃转化过程

    公开(公告)号：US07906013B2

    公开(公告)日：2011-03-15

    申请号：US12704780

    申请日：2010-02-12

    申请人： Peter Kokayeff ,  Laura E. Leonard ,  Michael R. Smith

    发明人： Peter Kokayeff ,  Laura E. Leonard ,  Michael R. Smith

    IPC分类号： C10G65/10

    CPC分类号： C10G65/04 ,  C10G65/12 ,  C10G2400/04

    摘要： A process is provided to produce an ultra low sulfur diesel with less than about 10 ppm sulfur using a two-phase or liquid-phase continuous reaction zone to convert a diesel boiling range distillate preferably obtained from a mild hydrocracking unit. In one aspect, the diesel boiling range distillate is introduced once-through to the liquid-phase continuous reaction zone over-saturated with hydrogen in an amount effective so that the liquid phase remains substantially saturated with hydrogen throughout the reaction zone as the reactions proceed.

    摘要翻译： 提供了一种使用两相或液相连续反应区产生具有小于约10ppm硫的超低硫柴油以转化优选从温和加氢裂化装置获得的柴油沸程馏出物的方法。 在一个方面，将柴油沸程馏出物一次性引入到用氢过饱和的液相连续反应区，其量是有效的，使得当反应进行时液相在整个反应区中基本上被氢饱和。