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    • 1. 发明专利
    • Method for producing lubricant base oil
    • 生产润滑油基油的方法
    • JP2006188634A
    • 2006-07-20
    • JP2005002880
    • 2005-01-07
    • Nippon Oil CorpPetroleum Energy Center新日本石油株式会社財団法人石油産業活性化センター
    • SUGIURA IZURUSEKI HIROYUKITAGUCHI MASAHIROIKI SUGURUAZUMA MASAHIRO
    • C10G65/12C10G21/16C10G45/58C10G47/12C10G67/04
    • PROBLEM TO BE SOLVED: To provide a method for producing a lubricant base oil, with which a lubricant base oil having low viscosity, a high viscosity index and low evaporation property is efficiently and inexpensively obtained. SOLUTION: The method for producing a lubricant base oil comprises a process for preparing a hydrocracking catalyst obtained by supporting at least one kind of a metal of the group VIa of the periodic table and at least one kind of a metal of the group VIII on a carrier having ≤80% fraction of desorption amount at 300-800°C based on the total desorption amount of NH 3 in NH 3 desorption temperature-dependency evaluation, a process for hydrocracking a raw material oil containing ≥50 vol.% of slack-wax in the presence of the hydrocracking catalyst under 0.1-14 MPa hydrogen partial pressure at 230-430°C average reaction temperature at 0.3-3.0hr -1 LHSV at 50-14,000 scf/b ratio of hydrogen to oil, a process for distilling and separating the obtained hydrocracked oil to give a lubricating oil fraction and a process for dewaxing the lubricating oil fraction. COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:提供一种润滑油基础油的制造方法,通过该方法可有效且廉价地获得具有低粘度,高粘度指数和低蒸发性能的润滑剂基础油。 解决方案:润滑油基础油的制造方法包括制备加氢裂化催化剂的方法,所述加氢裂化催化剂通过将至少一种元素周期表VIa族的金属和至少一种金属组成, VIII在解吸温度依赖性评价中,基于NH 3 SB 3的解吸附量,在300-800℃下具有≤80%解吸量的载体, 在加氢裂化催化剂存在下,在0.1-14MPa氢分压下,在230-430℃,平均反应温度为0.3-3.0hr,加氢裂化含有≥50体积%松弛蜡的原料油的方法 -1 LHSV,氢与油的比例为50-14,000scf / b,用于蒸馏和分离所得加氢裂化油以得到润滑油馏分的方法和使润滑油馏分脱蜡的方法。 版权所有(C)2006,JPO&NCIPI
    • 3. 发明专利
    • Method for hydrocracking wax
    • 水解方法
    • JP2007269897A
    • 2007-10-18
    • JP2006095181
    • 2006-03-30
    • Nippon Oil Corp新日本石油株式会社
    • SEKI HIROYUKIKONNO HIROBUMIAZUMA MASAHIRO
    • C10G47/00C10G47/04C10G47/16
    • B01J29/126B01J21/12B01J37/0009B01J2229/20B01J2229/42C10G47/16
    • PROBLEM TO BE SOLVED: To provide a method for hydrocracking wax, with which the pour point of obtained decomposition product is sufficiently reduced in hydrocracking a raw material containing a normal paraffin and which is useful for producing a gas oil for a cold district. SOLUTION: The method for hydrocracking wax comprises hydrocracking a raw material wax containing ≥70 mass% of a ≥20C normal paraffin in the presence of a hydrocracking catalyst so that a conversion ratio defined by formula (1): conversion ratio (mass%)=mass of fraction having COPYRIGHT: (C)2008,JPO&INPIT
    • 要解决的问题:提供一种加氢裂化蜡的方法,在加氢裂化原料中含有正链烷烃的原料中,所得分解产物的倾点得到充分降低,可用于生产冷区的瓦斯油 。 解决方案:加氢裂化蜡的方法包括在加氢裂化催化剂存在下加氢裂化含有≥70%(≥20%)正常石蜡的原料蜡,使得由式(1)定义的转化率:转化率(质量 %)=具有≥360℃沸点的蜡馏分具有<360℃沸点/质量的馏分的质量(具有≥360℃沸点的蜡馏分的质量是含有≥360℃沸点的蜡馏分的质量含有 在原料蜡中,具有<360℃沸点的馏分的质量分别为通过加氢裂化得到的加氢裂化产物中分别具有<360℃沸点的馏分的质量)为55-95质量%。 版权所有(C)2008,JPO&INPIT
    • 4. 发明专利
    • Method for hydrogenation treatment of wax
    • WAX加氢处理方法
    • JP2007211057A
    • 2007-08-23
    • JP2006030047
    • 2006-02-07
    • Nippon Oil Corp新日本石油株式会社
    • SEKI HIROYUKIAZUMA MASAHIRO
    • C10G47/14B01J23/44C10G2/00
    • B01J23/44B01J21/12B01J23/42B01J37/0009C10G47/00C10G2300/1022C10G2400/04C10G2400/06C10G2400/08
    • PROBLEM TO BE SOLVED: To provide a method for a hydrogenation treatment of wax that enhances catalyst activities of a catalyst deteriorating with time and permits acquisition in a good yield of a fuel base material with a sufficiently reduced normal paraffin content when wax is hydrocracked over a long period of time. SOLUTION: The method for a hydrogenation treatment of wax comprises a first step for hydrocracking wax as a raw material containing at least 70 mass% of a 16C or higher normal paraffin by bringing it into contact in the presence of hydrogen with a catalyst comprising a group VIII metal in the periodic table supported on a carrier comprising an amorphous solid acid, a second step for changing the raw material to a light paraffin containing at least 60 mass% of a 9-21C paraffin and hydrocracking the light paraffin by bringing it into contact with the catalyst in the presence of hydrogen, and a third step for changing the raw material to the wax and bringing it into contact with the catalyst in the presence of hydrogen. COPYRIGHT: (C)2007,JPO&INPIT
    • 待解决的问题:提供一种加氢处理蜡的方法,其增强催化剂的催化剂活性随时间而劣化,并且当蜡为蜡时能以足够降低的正链烷烃含量获得燃料基材料的良好产率 长时间加氢裂化。 解决方案:蜡的氢化处理方法包括:通过在氢存在下与催化剂接触来加氢裂化作为含有至少70质量%的16C或更高级正链烷烃的蜡的蜡的第一步骤 包括负载在包含无定形固体酸的载体上的元素周期表中的Ⅷ族金属,第二步,将原料转化为含有至少60质量%的9-21C石蜡的轻链烷烃,并通过将 在氢的存在下与催化剂接触,第三步是将原料转化为蜡,并在氢的存在下与催化剂接触。 版权所有(C)2007,JPO&INPIT
    • 5. 发明专利
    • Method for hydrogenation treatment
    • 氢化处理方法
    • JP2007204505A
    • 2007-08-16
    • JP2006021287
    • 2006-01-30
    • Nippon Oil Corp新日本石油株式会社
    • SEKI HIROYUKIAZUMA MASAHIRO
    • C10G65/12B01J23/42B01J23/44B01J29/12C10G45/06C10G45/10C10G47/18C10G47/20
    • PROBLEM TO BE SOLVED: To provide a method for hydrogenation treatment, which maintains yield of middle distillate being the objective substance of wax hydrocracking and isomerization ratio of normal paraffin to isoparaffin at high levels in simultaneously carrying out the hydrorefining of a liquid fuel base containing normal paraffin and wax hydrocracking. SOLUTION: In a fixed bed reactor equipped with a hydrocracking part 1a at the upstream side and a hydrorefining part 1b at the downstream side, respectively, a distance d 2 from the upstream end to the downstream end of a hydrorefining catalyst layer 3 is smaller than a distance d 1 from the upstream end to the downstream end of a hydrocracking catalyst layer 2, wax is fed to the hydrocracking part 1a, a liquid fuel base containing normal paraffin is fed to the hydrorefining part 1b, respectively, and wax hydrocracking is carried out at the hydrocracking part 1a and the hydrorefining of the decomposition product from the hydrocracking part 1a and the hydrorefining of the liquid fuel base are carried out at the hydrorefining part 1b, respectively. COPYRIGHT: (C)2007,JPO&INPIT
    • 待解决的问题:提供一种氢化处理方法,其在同时进行液体燃料的加氢精制的同时,将中间馏分的产率保持为蜡加氢裂化的目标物质和正链烷烃与异链烷烃的异构化比例高水平 碱含有正常的石蜡和蜡加氢裂化。 解决方案:在装有上游侧的加氢裂化部分1a和下游侧的加氢精制部分1b的固定床反应器中,从上游端到下游的距离d SB> 2 加氢精制催化剂层3的末端小于加氢裂化催化剂层2的上游端到下游端的距离d SB> 1 ,将蜡送入加氢裂化部1a,将含有 正常石蜡分别进料到加氢精制部分1b,在加氢裂化部分1a进行蜡加氢裂化,加氢裂化部分1a对分解产物进行加氢精制,加氢精制部分进行加氢精制 1b。 版权所有(C)2007,JPO&INPIT
    • 7. 发明专利
    • Method for hydrotreating
    • 氢化方法
    • JP2007246663A
    • 2007-09-27
    • JP2006071205
    • 2006-03-15
    • Nippon Oil Corp新日本石油株式会社
    • AOKI NOBUOSEKI HIROYUKIAZUMA MASAHIRO
    • C10G65/00B01J23/42B01J35/02C10G45/62C10G45/64C10G47/14C10G47/18
    • PROBLEM TO BE SOLVED: To provide a method for hydrotreating a paraffinic hydrocarbon by which the yield of both a component useful as a fuel base and a component useful as a lubricating oil base can be improved without increasing the amount of a catalyst and the low-temperature fluidity of the component useful as the fuel base can sufficiently be improved. SOLUTION: The method for the hydrotreating is carried out as follows. A material which is to be treated and contains the paraffinic hydrocarbon is passed through a first catalyst bed having a hydrocracking ability and/or a hydroisomerization ability and a second catalyst bed having a higher hydrocracking ability and/or hydroisomerization ability than those of the first catalyst bed in the presence of hydrogen in the order mentioned. COPYRIGHT: (C)2007,JPO&INPIT
    • 要解决的问题:提供一种用于加氢处理链烷烃的方法,通过该方法可以提高用作燃料基质的组分和可用作润滑油基质的组分的产率,而不增加催化剂的量, 可以充分提高用作燃料基料的组分的低温流动性。 解决方案:加氢处理方法如下进行。 待处理并含有链烷烃的材料通过具有加氢裂化性和/或加氢异构化能力的第一催化剂床和比第一催化剂具有更高加氢裂化性和/或加氢异构化能力的第二催化剂床 在氢气存在下按所提到的顺序进行床。 版权所有(C)2007,JPO&INPIT
    • 9. 发明专利
    • Method for producing liquid fuel
    • 生产液体燃料的方法
    • JP2008133369A
    • 2008-06-12
    • JP2006320586
    • 2006-11-28
    • Nippon Oil Corp新日本石油株式会社
    • SEKI HIROYUKIAZUMA MASAHIRO
    • C10G45/64C10G2/00C10G45/60C10G65/12
    • PROBLEM TO BE SOLVED: To provide a method for producing a liquid fuel, capable of achieving a high level of intermediate fraction selectivity in producing the liquid fuel from a paraffin-based hydrocarbon.
      SOLUTION: This method for producing the liquid fuel comprises a first process of performing the hydroisomerization treatment of the paraffin-based hydrocarbon by using a prescribed catalyst, and a second process of performing the hydrocracking treatment on the treated material obtained in the first process by using a catalyst containing a crystalline alminosilicate having ≥50 molar ratio of silica/alumina.
      COPYRIGHT: (C)2008,JPO&INPIT
    • 要解决的问题:提供一种能够在从石蜡基烃生产液体燃料中获得高水平的中间馏分选择性的液体燃料的生产方法。 解决方案:这种制备液体燃料的方法包括通过使用规定的催化剂进行石蜡基烃的加氢异构化处理的第一种方法和对第一种方法获得的处理材料进行加氢裂化处理的第二种方法 通过使用含有≥50摩尔比的二氧化硅/氧化铝的结晶硅酸铝的催化剂的方法。 版权所有(C)2008,JPO&INPIT