Hydrodesulfurization Catalyst for Petroleum Hydrocarbons and Process for Hydrodesulfurization Using the Same
    1.
    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 FOR PRODUCING AVIATION FUEL OIL BASE AND AVIATION FUEL OIL COMPOSITION
    3.
    发明申请
    METHOD FOR PRODUCING AVIATION FUEL OIL BASE AND AVIATION FUEL OIL COMPOSITION 有权
    制造航空燃油油基和航空燃料油组合物的方法

    公开(公告)号:US20120216449A1

    公开(公告)日:2012-08-30

    申请号:US13391727

    申请日:2010-08-30

    IPC分类号: C10L1/188

    摘要: A method for producing an aviation fuel oil base includes obtaining a first generated oil by hydrotreating a feedstock by bringing a feedstock which includes an oxygen-containing hydrocarbon compound derived from an animal or vegetable oils and fat into contact with a first dual functional catalyst which has dehydrogenation and hydrogenation functions and which includes a metal of group 6A of the periodic table, a metal of group 8, and an amorphous solid acidic substance, in the presence of hydrogen; and obtaining a second generated oil including an aviation fuel oil base by hydroisomerizing the first generated oil by bringing the first generated oil into contact with a second dual functional catalyst which has dehydrogenation and hydrogenation functions and which includes a metal of the group 8 of the periodic table and a crystalline solid acidic substance, in the presence of hydrogen.

    摘要翻译: 一种航空燃料油基料的制造方法,其特征在于,通过使来自动物或植物油脂的含氧烃化合物的原料与第一双官能催化剂接触而进行加氢处理,得到第一产生油, 脱氢和氢化功能,其包括周期表第6A族金属,第8族金属和无定形固体酸性物质,在氢的存在下; 以及通过使第一产生的油与具有脱氢和氢化功能的第二双功能催化剂接触来获得包含航空燃料油基的第二产生的油,该第二双功能催化剂包括周期性的第8族金属 表和结晶固体酸性物质,在氢的存在下。

    Method for producing aviation fuel oil base and aviation fuel oil composition
    5.
    发明授权
    Method for producing aviation fuel oil base and aviation fuel oil composition 有权
    制造航空燃油基地和航空燃油组合物的方法

    公开(公告)号:US09283552B2

    公开(公告)日:2016-03-15

    申请号:US13391727

    申请日:2010-08-30

    摘要: A method for producing an aviation fuel oil base, including: a first step of obtaining a first generated oil by hydrotreating a feedstock by bringing a feedstock which includes an oxygen-containing hydrocarbon compound derived from an animal or vegetable oils and fat into contact with a first dual functional catalyst which has dehydrogenation and hydrogenation functions and which includes a metal of group 6B of the periodic table, a metal of group 8, and an amorphous solid acidic substance, in the presence of hydrogen; and a second step of obtaining a second generated oil including an aviation fuel oil base by hydroisomerizing the first generated oil by bringing the first generated oil into contact with a second dual functional catalyst which has dehydrogenation and hydrogenation functions and which includes a metal of the group 8 of the periodic table and a crystalline solid acidic substance, in the presence of hydrogen.

    摘要翻译: 一种生产航空燃料油基料的方法,包括:第一步骤,通过将包含来源于动物或植物油脂的含氧烃化合物的原料与一种原料接触而将原料加氢处理获得第一产生的油 具有脱氢和氢化功能的第一双官能催化剂,其包含周期表第6B族金属,第8族金属和无定形固体酸性物质,在氢的存在下; 以及第二步骤,通过使第一产生的油与具有脱氢和氢化功能的第二双功能催化剂接触,并且包括该组的金属,获得包含航空燃料油基的第二产生的油, 8和结晶固体酸性物质,在氢的存在下。

    Method of hydrotreating gas oil fraction
    7.
    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:US20060211900A1

    公开(公告)日:2006-09-21

    申请号:US10548313

    申请日:2004-03-05

    IPC分类号: C07C1/00

    摘要: The gas oil fraction hydrotreatment process of the invention is characterized by using a gas oil fraction with a sulfur content of 0.8-2% by mass and a total aromatic content of 20-35% by volume as the feed oil and subjecting the feed oil to hydrotreatment in the presence of a hydrogenation catalyst comprising at least one metal from among Group 6A metals and at least one metal from among Group 8 metals as active metals, and under reaction conditions with a reaction temperature of 330-390° C., a hydrogen partial pressure of 12-20 MPa and a liquid hourly space velocity of 0.1-1 h−1, 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0.8〜2质量%,总芳烃含量为20〜35体积%的粗柴油馏分作为原料油, 在包含至少一种金属的6A族金属和至少一种金属作为活性金属的第8族金属中进行加氢处理,在反应温度为330-390℃的反应条件下,加氢处理 12-20MPa的分压和0.1-1小时-1的液时空速,得到硫含量不大于1ppm的超低硫和低芳烃瓦斯油馏分 并且总芳族含量不大于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。

    Hydrodesulfurization catalyst and hydrodesulfurization process for gasoline fractions
    8.
    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。

    Method of hydrotreating gas oil fraction
    10.
    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。