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    METHOD OF PRODUCING LIQUID FUEL
    3.
    发明申请
    METHOD OF PRODUCING LIQUID FUEL 有权
    生产液体燃料的方法

    公开(公告)号：US20100122935A1

    公开(公告)日：2010-05-20

    申请号：US12451158

    申请日：2008-04-26

    申请人： Hiroyuki Seki ,  Masahiro Higashi ,  Sumio Saito ,  Ryuzo Kuroda ,  Takashi Kameoka

    发明人： Hiroyuki Seki ,  Masahiro Higashi ,  Sumio Saito ,  Ryuzo Kuroda ,  Takashi Kameoka

    IPC分类号： C10G47/04

    CPC分类号： B01J29/084 ,  B01J21/02 ,  B01J21/12 ,  B01J29/126 ,  B01J37/0009 ,  B01J2229/20 ,  B01J2229/36 ,  B01J2229/42 ,  C10G45/52 ,  C10G45/54 ,  C10G45/62 ,  C10G45/64 ,  C10G47/18 ,  C10G2300/1022 ,  C10G2300/304 ,  C10G2300/307 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2300/4018 ,  C10G2300/4025 ,  C10G2400/06

    摘要： The present invention provides a method of producing a liquid fuel enabling production of middle distillate at a high yield from a feed oil containing paraffinic hydrocarbons having 20 to 100 carbon atoms as main components without losing the high cracking activity and also enabling provision of high quality gas oil included in the middle distillate.A feed oil containing paraffinic hydrocarbons having 20 to 100 carbon atoms as main components is subjected to hydrotreating in the present of a prespecified hydrotreating catalyst and under the conditions for hydrotreating including a temperature of 200 to 350° C., a liquid hourly space velocity of 0.1 to 5.0 h−1, and a partial pressure of hydrogen of 0.5 to 8 MPa to obtain an effluent oil, and then the effluent oil is fractionated to obtain middle distillate including a gas oil with a cetane number of 75 or over and a pour point of −27.5° C. or below at a yield of 55% or over against a total weight of the feed oil.

    摘要翻译： 本发明提供一种液体燃料的制造方法，其能够从含有20〜100个碳原子的链烷烃作为主要成分以高收率生产中间馏分，而不会失去高的裂解活性，并且还能够提供优质的气体 包含在中间馏分油中。 将含有20〜100个碳原子的链烷烃作为主要成分的原料油在预先指定的加氢处理催化剂中进行加氢处理，并在包括温度在200〜350℃的加氢处理条件下进行加氢处理， 0.1〜5.0h-1，氢分压为0.5〜8MPa，得到流出油，然后对流出油进行分馏，得到中间馏分，其中含有十六烷值为75以上的瓦斯油， 点为-27.5℃以下，相对于原料油的总重量为55％以上的收率。

    Method of producing liquid fuel
    5.
    发明授权
    Method of producing liquid fuel 有权
    液体燃料的生产方法

    公开(公告)号：US08366911B2

    公开(公告)日：2013-02-05

    申请号：US12451158

    申请日：2008-04-26

    申请人： Hiroyuki Seki ,  Masahiro Higashi ,  Sumio Saito ,  Ryuzo Kuroda ,  Takashi Kameoka

    发明人： Hiroyuki Seki ,  Masahiro Higashi ,  Sumio Saito ,  Ryuzo Kuroda ,  Takashi Kameoka

    IPC分类号： C10G47/14 ,  C10G47/18

    CPC分类号： B01J29/084 ,  B01J21/02 ,  B01J21/12 ,  B01J29/126 ,  B01J37/0009 ,  B01J2229/20 ,  B01J2229/36 ,  B01J2229/42 ,  C10G45/52 ,  C10G45/54 ,  C10G45/62 ,  C10G45/64 ,  C10G47/18 ,  C10G2300/1022 ,  C10G2300/304 ,  C10G2300/307 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2300/4018 ,  C10G2300/4025 ,  C10G2400/06

    摘要： The present invention provides a method of producing a liquid fuel enabling production of middle distillate at a high yield from a feed oil containing paraffinic hydrocarbons having 20 to 100 carbon atoms as main components without losing the high cracking activity and also enabling provision of high quality gas oil included in the middle distillate.A feed oil containing paraffinic hydrocarbons having 20 to 100 carbon atoms as main components is subjected to hydrotreating in the present of a prespecified hydrotreating catalyst and under the conditions for hydrotreating including a temperature of 200 to 350° C., a liquid hourly space velocity of 0.1 to 5.0 h−1, and a partial pressure of hydrogen of 0.5 to 8 MPa to obtain an effluent oil, and then the effluent oil is fractionated to obtain middle distillate including a gas oil with a cetane number of 75 or over and a pour point of −27.5° C. or below at a yield of 55% or over against a total weight of the feed oil.

    摘要翻译： 本发明提供一种液体燃料的制造方法，其能够从含有20〜100个碳原子的链烷烃作为主要成分以高收率生产中间馏分，而不会失去高的裂解活性，并且还能够提供优质的气体 包含在中间馏分油中。 将含有20〜100个碳原子的链烷烃作为主要成分的原料油在预先指定的加氢处理催化剂中进行加氢处理，并在包括温度在200〜350℃的加氢处理条件下进行加氢处理， 0.1〜5.0h-1，氢分压为0.5〜8MPa，得到流出油，然后对流出油进行分馏，得到中间馏分，其中含有十六烷值为75以上的瓦斯油， 点为-27.5℃以下，相对于原料油的总重量为55％以上的收率。

    Method for manufacturing zeolite Y with aluminum and titanium inserted therein
    6.
    发明申请
    Method for manufacturing zeolite Y with aluminum and titanium inserted therein 有权
    用插入其中的铝和钛制造沸石Y的方法

    公开(公告)号：US20110251049A1

    公开(公告)日：2011-10-13

    申请号：US13067687

    申请日：2011-06-21

    申请人： Ryuzo Kuroda ,  Masaru Ushio

    发明人： Ryuzo Kuroda ,  Masaru Ushio

    IPC分类号： B01J29/89

    CPC分类号： B01J29/89 ,  B01J29/084 ,  B01J29/166 ,  B01J35/10 ,  B01J35/1042 ,  B01J35/1057 ,  B01J35/1061 ,  B01J35/1066 ,  B01J35/1071 ,  B01J2229/183 ,  B01J2229/20 ,  B01J2229/42 ,  C10G49/08 ,  C10G2300/70

    摘要： A catalytic composition for hydrotreating of hydrocarbons is made in which a metallic component for hydrogenation is carried on a carrier formed of zeolite Y with aluminum and titanium inserted therein and a porous inorganic oxide. The zeolite Y has: unit cell dimension in a range from 24.25 to 24.60 Å, crystallinity of 95% or more, specific surface area of 500 m2/g or more, total pore volume of a group of pores each having a diameter of 600 Å or below in a range from 0.45 to 0.70 ml/g, pore volume of a group of pores each having a diameter in a range from 100 to 600 Å in a range from 0.10 to 0.40 ml/g, and pore volume of a group of pores each having a diameter in a range from 35 to 50 Å in a range 0.03 to 0.15 ml/g.

    摘要翻译： 制备用于加氢处理烃的催化组合物，其中用于氢化的金属组分承载在由沸石Y形成的载体上，铝和钛插入其中，以及多孔无机氧化物。 沸石Y具有：单位尺寸在24.25至24.60埃的范围内，结晶度为95％或更高，比表面积为500m 2 / g或更高，每个直径为600埃的孔组的总孔体积 以下，在0.45〜0.70ml / g的范围内，孔直径在100〜600范围内的孔隙体积为0.10〜0.40ml / g，孔体积为 孔径各自为35〜50，范围为0.03〜0.15ml / g。

    Method for manufacturing zeolite Y with aluminum and titanium inserted therein
    8.
    发明授权
    Method for manufacturing zeolite Y with aluminum and titanium inserted therein 有权
    用插入其中的铝和钛制造沸石Y的方法

    公开(公告)号：US08148285B2

    公开(公告)日：2012-04-03

    申请号：US13067687

    申请日：2011-06-21

    申请人： Ryuzo Kuroda ,  Masaru Ushio

    发明人： Ryuzo Kuroda ,  Masaru Ushio

    IPC分类号： B01J29/08 ,  B01J29/89

    CPC分类号： B01J29/89 ,  B01J29/084 ,  B01J29/166 ,  B01J35/10 ,  B01J35/1042 ,  B01J35/1057 ,  B01J35/1061 ,  B01J35/1066 ,  B01J35/1071 ,  B01J2229/183 ,  B01J2229/20 ,  B01J2229/42 ,  C10G49/08 ,  C10G2300/70

    摘要： A catalytic composition for hydrotreating of hydrocarbons is made in which a metallic component for hydrogenation is carried on a carrier formed of zeolite Y with aluminum and titanium inserted therein and a porous inorganic oxide. The zeolite Y has: unit cell dimension in a range from 24.25 to 24.60 Å, crystallinity of 95% or more, specific surface area of 500 m2/g or more, total pore volume of a group of pores each having a diameter of 600 Å or below in a range from 0.45 to 0.70 ml/g, pore volume of a group of pores each having a diameter in a range from 100 to 600 Å in a range from 0.10 to 0.40 ml/g, and pore volume of a group of pores each having a diameter in a range from 35 to 50 Å in a range 0.03 to 0.15 ml/g.

    摘要翻译： 制备用于加氢处理烃的催化组合物，其中用于氢化的金属组分承载在由沸石Y形成的载体上，铝和钛插入其中，以及多孔无机氧化物。 沸石Y具有：单位尺寸在24.25至24.60埃的范围内，结晶度为95％或更高，比表面积为500m 2 / g或更高，每个直径为600埃的孔组的总孔体积 以下，在0.45〜0.70ml / g的范围内，孔直径在100〜600范围内的孔隙体积为0.10〜0.40ml / g，孔体积为 孔径各自为35〜50，范围为0.03〜0.15ml / g。

    Catalytic composition for hydrotreating of hydrocarbons and method for hydrotreating
    10.
    发明申请
    Catalytic composition for hydrotreating of hydrocarbons and method for hydrotreating 审中-公开
    用于加氢处理烃的催化组合物和加氢处理方法

    公开(公告)号：US20090283443A1

    公开(公告)日：2009-11-19

    申请号：US11991378

    申请日：2006-09-06

    申请人： Ryuzo Kuroda ,  Masaru Ushio

    发明人： Ryuzo Kuroda ,  Masaru Ushio

    IPC分类号： C10G47/20 ,  B01J29/06

    CPC分类号： B01J29/89 ,  B01J29/084 ,  B01J29/166 ,  B01J35/10 ,  B01J35/1042 ,  B01J35/1057 ,  B01J35/1061 ,  B01J35/1066 ,  B01J35/1071 ,  B01J2229/183 ,  B01J2229/20 ,  B01J2229/42 ,  C10G49/08 ,  C10G2300/70

    摘要： A catalytic composition for hydrotreating of hydrocarbons in which a metallic component for hydrogenation is carried on a carrier comprising zeolite Y with aluminum and titanium inserted therein and a porous inorganic oxide, the zeolite Y having the following characteristics: (a) unit cell dimension (UD) in a range from 24.25 to 24.60 Å, (b) crystallinity of 95% or more, (c) specific surface area (SA) of 500 m2/g or more, (d) total pore volume (PVt) of a group of pores each having a diameter of 600 Å or below in a range from 0.45 to 0.70 ml/g, (e) pore volume (PVm) of a group of pores each having a diameter in a range from 100 to 600 Å in a range from 0.10 to 0.40 ml/g, (f) pore volume (PVs) of a group of pores each having a diameter in a range from 35 to 50 Å in a range 0.03 to 0.15 ml/g, and (g) percentage of 4-coordinate aluminum atoms against total aluminum atoms in the zeolite of 60 atom % or more.

    摘要翻译： 一种用于加氢处理烃的催化组合物，其中用于氢化的金属组分载于包含沸石Y的铝载体和多孔无机氧化物的载体上，沸石Y具有以下特征：（a）晶胞尺寸（UD） ），（b）结晶度为95％以上，（c）比表面积（SA）为500m 2 / g以上，（d）一组的总孔体积（PVt） 孔径各自为直径在600或以下的孔径为0.45〜0.70ml / g，（e）孔直径在100〜600范围内的孔体积（PVm）范围为 0.10至0.40ml / g，（f）孔直径在35至500范围内的孔隙体积（PVs）范围为0.03至0.15ml / g，（g）4- 将铝原子与沸石中的总铝原子配位为60原子％以上。