Hydrodesulfurization Catalyst for Petroleum Hydrocarbons and Process for Hydrodesulfurization Using the Same
    13.
    发明申请
    Hydrodesulfurization Catalyst for Petroleum Hydrocarbons and Process for Hydrodesulfurization Using the Same 审中-公开
    石油烃加氢脱硫催化剂及其加氢脱硫方法

    公开(公告)号:US20070175797A1

    公开(公告)日:2007-08-02

    申请号:US11626074

    申请日:2007-01-23

    CPC分类号: C10G45/08 B01J27/19

    摘要: The present invention provides a hydrodesulfurization that can attain an extremely high depth of desulfurization to a sulfur content of 10 ppm by mass and maintain such a high desulfurization activity for a long period of time. The catalyst comprises an inorganic porous support containing alumina and phosphorus, at least one active metal selected from the metals of Group 8 of the periodic table, and at least one metal selected from the metals of Group 6A of the periodic table, the Group 8 metal and the Group 6A metal being contained in a molar ratio defined by (oxide of the Group 8 metal)/(oxide of the Group 6A metal) ranging from 0.055 to 0.150, and the content of the Group 6A metal in terms of oxide being in the range of 30 to 40 percent by mass based on the mass of the catalyst.

    摘要翻译: 本发明提供一种能够达到非常高的脱硫深度至硫酸含量为10质量ppm的加氢脱硫,并且长期保持如此高的脱硫活性。 催化剂包括含有氧化铝和磷的无机多孔载体,选自元素周期表第8族金属的至少一种活性金属和选自元素周期表第6A族金属中的至少一种金属,第8族金属 并且6A族金属以(由第8族金属的氧化物)/(6A族金属的氧化物)定义的摩尔比包含在0.055〜0.150的范围内,6A族金属的含量以氧化物为单位 相对于催化剂的质量为30〜40质量%的范围。

    Method of hydrotreating gas oil fraction
    14.
    发明申请
    Method of hydrotreating gas oil fraction 审中-公开
    加氢处理瓦斯油馏分的方法

    公开(公告)号:US20060260983A1

    公开(公告)日:2006-11-23

    申请号:US10548315

    申请日:2004-03-05

    摘要: The gas oil fraction hydrotreatment process of the invention is characterized by using a hydrorefined petroleum-based hydrocarbon oil with a sulfur content of 5-15 ppm by mass, a total aromatic content of 10-25% by volume and a boiling point range of 150-380° C. as the feed oil and subjecting the feed oil to hydrotreatment in the presence of a hydrogenation catalyst to obtain an ultralow sulfur and low aromatic gas oil fraction having a sulfur content of not greater than 1 ppm by mass and a total aromatic content of not greater than 1% by volume. This hydrotreatment process allows production of a “zero sulfur” and “zero aromatic” gas oil fraction in an efficient and reliable manner without provision of special operating conditions or equipment investment.

    摘要翻译: 本发明的粗柴油馏分加氢处理方法的特征在于使用硫含量为5〜15质量ppm的加氢精制石油基烃油,总芳族化合物含量为10〜25体积%,沸点范围为150 -380℃作为原料油,并在进料油在氢化催化剂存在下进行加氢处理,得到硫含量不大于1质量ppm的超低硫和低芳烃馏分,总芳烃 含量不超过1%(体积)。 该加氢处理方法允许以有效和可靠的方式生产“零硫”和“零芳烃”瓦斯油馏分,而不需要特殊的操作条件或设备投资。

    Process for hydrodesulfurization of diesel gas oil
    15.
    发明授权
    Process for hydrodesulfurization of diesel gas oil 有权
    柴油机加氢脱硫工艺

    公开(公告)号:US06251262B1

    公开(公告)日:2001-06-26

    申请号:US09377087

    申请日:1999-08-19

    IPC分类号: C10G6504

    CPC分类号: C10G65/04 C10G2400/04

    摘要: Diesel gas oil feedstock with 1-3 wt % sulfur can be hydrodesulfurized to a diesel gas oil with 0.05 wt % or less sulfur and a Saybolt color of +20 or higher, by defining a hydrogenation region in a fixed bed reactor with a first hydrogenation zone for dibenzothiophene, 1-, 2- and 3-methyldibenzothiophenes, a second hydrogenation zone for 4-methyldibenzothiophene and 4,6-dimethyldibenzothiophene and a third hydrogenation zone for thiols, sulfides and other sulfur-containing substances.

    摘要翻译: 通过在具有第一氢化的固定床反应器中限定氢化区域,可以将具有1-3重量%硫的柴油瓦斯油原料加氢脱硫至具有0.05重量%或更少硫并且Saybolt颜色为+ 20以上的柴油瓦斯油 二苯并噻吩,1-,2-和3-甲基二苯并噻吩的区域,4-甲基二苯并噻吩和4,6-二甲基二苯并噻吩的第二氢化区和用于硫醇,硫化物和其它含硫物质的第三氢化区。

    Fuel composition
    16.
    发明授权
    Fuel composition 有权
    燃油组成

    公开(公告)号:US07914593B2

    公开(公告)日:2011-03-29

    申请号:US12294110

    申请日:2007-02-22

    IPC分类号: C10L1/10

    摘要: The present invention provides a fuel composition capable of suppressing reduction of fuel consumption, maintaining the excellent exhaust gas properties of a Fischer-Tropsch synthetic oil. The fuel composition comprises a Fischer-Tropsch synthetic oil and a petroleum-based hydrocarbon mixture A having the following properties (1) to (5) in an amount of 10 to 30 percent by volume on the basis of the total mass of the composition: (1) 15° C. density: 800 Kg/cm3 or greater and 900 Kg/m3 or less; (2) 10 volume % distillation temperature (T10): 150° C. or higher and 200° C. or lower; (3) 97 volume % distillation temperature (T97): 270° C. or lower; (4) aromatic content: 40 percent by volume or more and 70 percent by volume or less; and (5) sulfur content: 30 ppm by mass or less.

    摘要翻译: 本发明提供能够抑制燃料消耗的降低,维持费 - 托合成油优异的废气性能的燃料组合物。 燃料组合物包含基于组合物的总质量的10至30体积%的具有以下性质(1)至(5)的费 - 托合成油和石油基烃混合物A: (1)15℃密度:800Kg / cm 3以上900kg / m 3以下; (2)10体积%蒸馏温度(T10):150℃以上且200℃以下; (3)97体积%蒸馏温度(T97):270℃以下; (4)芳香族含量:40体积%以上且70体积%以下; 和(5)硫含量:30质量ppm以下。

    PROCESS FOR PRODUCING GASOLINE BASE AND GASOLINE
    17.
    发明申请
    PROCESS FOR PRODUCING GASOLINE BASE AND GASOLINE 有权
    生产汽油基和汽油的方法

    公开(公告)号:US20100219102A1

    公开(公告)日:2010-09-02

    申请号:US12681787

    申请日:2008-10-06

    IPC分类号: C10G69/02

    摘要: The production process of the invention comprises a first step of hydrodesulfurizing of catalytically-cracked gasoline so as to result in an olefin hydrogenation rate of no greater than 25 mol % in the catalytically-cracked gasoline, a total sulfur content of no greater than 20 ppm by weight based on the product oil weight, a sulfur content derived from thiophenes and benzothiophenes of no greater than 5 ppm by weight and a sulfur content derived from thiacyclopentanes of no greater than 0.1 ppm by weight, and a second step of further hydrodesulfurizing of the product oil obtained by the first step so as to result in a total of no greater than 30 mol % for the olefin hydrogenation rate in the first step and the olefin hydrogenation rate in the second step, a total sulfur content of no greater than 10 ppm by weight based on the product oil weight, and a sulfur content derived from thiols of no greater than 5 ppm by weight.

    摘要翻译: 本发明的制造方法包括催化裂化汽油的加氢脱硫的第一步骤,使催化裂化汽油中的烯烃氢化率不大于25mol%,总硫含量不大于20ppm 基于产品油重量,来自噻吩和苯并噻吩的硫含量不大于5ppm重量,硫代环戊烷的硫含量不大于0.1ppm重量,第二步是进一步加氢脱硫 通过第一步获得的产物油,以使第一步中的烯烃氢化速率和第二步中的烯烃氢化速率总共不大于30mol%,总硫含量不大于10ppm 基于产品油重量,和硫醇的硫含量不大于5重量ppm。

    Fuel Composition
    18.
    发明申请
    Fuel Composition 有权
    燃料组成

    公开(公告)号:US20090126264A1

    公开(公告)日:2009-05-21

    申请号:US12294110

    申请日:2007-02-22

    IPC分类号: C10L1/18

    摘要: The present invention provides a fuel composition capable of suppressing reduction of fuel consumption, maintaining the excellent exhaust gas properties of a Fischer-Tropsch synthetic oil. The fuel composition comprises a Fischer-Tropsch synthetic oil and a petroleum-based hydrocarbon mixture A having the following properties (1) to (5) in an amount of 10 to 30 percent by volume on the basis of the total mass of the composition: (1) 15° C. density: 800 Kg/cm3 or greater and 900 Kg/m3 or less; (2) 10 volume % distillation temperature (T10): 150° C. or higher and 200° C. or lower; (3) 97 volume % distillation temperature (T97): 270° C. or lower; (4) aromatic content: 40 percent by volume or more and 70 percent by volume or less; and (5) sulfur content: 30 ppm by mass or less.

    摘要翻译: 本发明提供能够抑制燃料消耗的降低,维持费 - 托合成油优异的废气性能的燃料组合物。 燃料组合物包含基于组合物的总质量的10至30体积%的具有以下性质(1)至(5)的费 - 托合成油和石油基烃混合物A: (1)15℃密度:800Kg / cm 3以上900kg / m 3以下; (2)10体积%蒸馏温度(T10):150℃以上且200℃以下; (3)97体积%蒸馏温度(T97):270℃以下; (4)芳香族含量:40体积%以上且70体积%以下; 和(5)硫含量:30质量ppm以下。

    Hydrodesulfurization catalyst and hydrodesulfurization process for gasoline fractions
    20.
    发明授权
    Hydrodesulfurization catalyst and hydrodesulfurization process for gasoline fractions 有权
    汽油馏分的加氢脱硫催化剂和加氢脱硫工艺

    公开(公告)号:US07776784B2

    公开(公告)日:2010-08-17

    申请号:US10888972

    申请日:2004-07-13

    摘要: A hydrodesulfurization catalyst used for hydrodesulfurization of catalytically cracked gasoline comprises a support composed mainly of alumina modified with an oxide of at least one metal selected from the group consisting of iron, chromium, cobalt, nickel, copper, zinc, yttrium, scandium and lanthanoid-based metals, with at least one metal selected from the group consisting of Group 6A and Group 8 metals loaded as an active metal on the support. Hydrogenation of olefins generated as by-products during hydrodesulfurization of the catalytically cracked gasoline fraction, as an important constituent base of gasoline, can be adequately inhibited to maintain the octane number, while sufficiently reducing the sulfur content of the hydrodesulfurized catalytically cracked gasoline fraction.

    摘要翻译: 用于催化裂化汽油加氢脱硫的加氢脱硫催化剂包括主要由氧化物组成的载体,该氧化铝用选自铁,铬,钴,镍,铜,锌,钇,钪和镧系元素中的至少一种金属的氧化物, 具有至少一种选自负载作为活性金属的6A族和第8族金属的金属在载体上。 作为汽油的重要成分基的催化裂化汽油馏分的加氢脱硫期间作为副产物生成的烯烃的氢化可以充分地抑制维持辛烷值,同时充分降低加氢脱硫催化裂化汽油馏分的硫含量。