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公开(公告)号：US10087376B2
公开(公告)日：2018-10-02
申请号：US14801089
申请日：2015-07-16
IPC分类号： C07C4/06 , C10G11/05 , B01J29/80 , C10G47/16 , C10G11/18 , B01J29/08 , B01J29/18 , B01J29/40 , B01J29/70 , B01J37/00
摘要： A catalyst is provided for production of monocyclic aromatic hydrocarbons having a carbon number of 6 to 8 from feedstock in which a 10 vol % distillation temperature is 140° C. or higher and a 90 vol % distillation temperature is 380° C. or lower. The catalyst contains crystalline aluminosilicate including large-pore zeolite having a 12-membered ring structure, and intermediate-pore zeolite having a 10-membered ring structure.
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公开(公告)号：US20150060332A1
公开(公告)日：2015-03-05
申请号：US14388338
申请日：2013-03-29
IPC分类号： C10M101/02 , C10G69/02
CPC分类号： C10G65/14 , B01J29/061 , B01J29/068 , C10G45/58 , C10G45/64 , C10G47/12 , C10G69/02 , C10G2300/1022 , C10M101/02 , C10M2203/1006
摘要： A method for producing a lubricant base oil, the method comprising a first step of fractionating, from a hydrocarbon oil containing a base oil fraction and a heavy fraction that is heavier than the base oil fraction, the base oil fraction and the heavy fraction, and a second step of obtaining a dewaxed oil by isomerization and dewaxing of the base oil fraction fractionated in the first step, wherein a hydrocracked oil obtained by hydrocracking the heavy fraction fractionated in the first step is returned to the first step.
摘要翻译： 一种润滑油基础油的制造方法，其特征在于，包括从含有基油馏分和比基油馏分重的重质馏分，基油馏分和重馏分的烃油分馏的第一工序，以及 第二步，通过在第一步骤中分馏的基础油馏分的异构化和脱蜡获得脱蜡油，其中通过加氢裂化在第一步中分馏的重馏分获得的加氢裂化油返回到第一步骤。
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公开(公告)号：US09868912B2
公开(公告)日：2018-01-16
申请号：US14780768
申请日：2014-03-26
发明人： Kazuaki Hayasaka , Yasushi Wada , Marie Iwama , Koshi Takahama
IPC分类号： C10G45/64 , C10G45/58 , G01N24/08 , C10M101/02
CPC分类号： C10G45/64 , C10G45/58 , C10G2400/10 , C10M101/02 , C10M2203/0206 , C10N2220/022 , C10N2230/02 , G01N24/08 , G01N24/085
摘要： A method for producing a lubricating base oil, comprising: performing a 13C-NMR analysis regarding an oil to be treated and selecting the oil based on a value for dividing an integrated value of a peak for a tertiary carbon atom by an integrated value of all peaks at 0 to 50 ppm, a value for dividing an integrated value of a peak for a carbon atom constituting a main chain by the integrated value of all peaks at 0 to 50 ppm, and a value for dividing an integrated value of a peak for a branched CH3 bonded to a fifth or the following carbon atom from a terminal carbon atom in the main chain by an integrated value of all peaks at 10 to 25 ppm, and obtaining a dewaxed oil by isomerization dewaxing of the oil selected in the first step, is disclosed.
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4.发明授权公开(公告)号：US09827554B2
公开(公告)日：2017-11-28
申请号：US14430026
申请日：2013-09-12
IPC分类号： C07C27/00 , C07C27/06 , B01J21/00 , B01J21/04 , B01J23/00 , B01J23/02 , B01J23/40 , B01J23/42 , B01J23/75 , C10G2/00 , B01J21/08 , B01J23/46 , B01J35/10 , B01J23/89 , B01J37/08 , B01J32/00 , B01J37/18 , B01J37/02 , B01J35/02 , B01J35/08
CPC分类号： B01J23/75 , B01J21/08 , B01J23/462 , B01J23/8913 , B01J32/00 , B01J35/023 , B01J35/08 , B01J35/1019 , B01J35/1038 , B01J35/1061 , B01J37/0201 , B01J37/0207 , B01J37/0244 , B01J37/08 , B01J37/18 , C10G2/00 , C10G2/332 , C10G2/333 , C10G2/334
摘要： A process for producing a Fischer-Tropsch synthesis catalyst according to the present invention comprises a step of calcining a carrier precursor containing silica calcined at a temperature T1 and a zirconium compound at a temperature T2 to obtain a carrier; and a step of calcining a catalyst precursor containing the carrier and a cobalt compound and/or a ruthenium compound at a temperature T3, wherein the content of the zirconium compound in the carrier precursor is 0.01 to 7% by mass in terms of zirconium oxide based on the total mass of the catalyst, and T1, T2, and T3 satisfy conditions represented by expressions (1) to (3): T1≧T3 (1) 250° C.≦T2≦450° C. (2) 250° C.≦T3≦450° C. (3).
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5.发明授权公开(公告)号：US09713807B2
公开(公告)日：2017-07-25
申请号：US14388945
申请日：2013-03-29
CPC分类号： B01J29/7484 , B01J29/076 , B01J29/703 , B01J29/74 , B01J29/7461 , B01J29/78 , B01J29/7861 , B01J29/7884 , B01J29/7892 , B01J2229/186 , C07C5/2791 , C10G45/62 , C10G45/64
摘要： A method for producing a hydroisomerization catalyst according to the present invention includes: a first step of preparing a catalyst to be treated, which contains a support having a one-dimensional porous structure including a 10-membered ring and at least one metal selected from the group consisting of: group 8 to 10 metals of the periodic table, Mo, and W supported on the hydroisomerization catalyst; and a second step of producing a hydroisomerization catalyst having a carbon content of 0.4 to 2.5% by mass by subjecting the catalyst to be treated to a coking treatment by means of a carbon-containing compound.
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公开(公告)号：US20150094505A1
公开(公告)日：2015-04-02
申请号：US14388548
申请日：2013-03-29
IPC分类号： C10M101/02
CPC分类号： C10G45/58 , B01J29/068 , B01J2229/42 , C10G45/62 , C10G45/64 , C10G71/00 , C10G2300/301 , C10M101/02 , C10M101/025 , C10M177/00 , C10M2203/065 , C10N2220/021 , C10N2270/00
摘要： A method for producing a lubricant base oil that has a predetermined boiling point range, the method including a first step of bringing a feedstock containing a first hydrocarbon oil having a boiling point in the above boiling point range and a second hydrocarbon oil having a lower boiling point than the boiling point range into contact with a hydroisomerization catalyst, wherein the catalyst contains a support that includes a zeolite having a one-dimensional porous structure including a 10-membered ring and a binder, and platinum and/or palladium supported on the support.
摘要翻译： 一种制造具有预定沸点范围的润滑剂基础油的方法，所述方法包括使包含沸点在上述沸点范围内的第一烃油的原料和具有较低沸点的第二烃油的第一步骤 比沸点范围与加氢异构化催化剂接触，其中催化剂含有载体，其包含具有包含10元环和粘合剂的一维多孔结构的沸石，以及负载在载体上的铂和/或钯 。
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公开(公告)号：US20150060328A1
公开(公告)日：2015-03-05
申请号：US14388986
申请日：2013-04-01
发明人： Kazuo Tagawa , Kazuaki Hayasaka
IPC分类号： C10M101/02 , C10G67/02
CPC分类号： C10M101/02 , C10G67/02 , C10G67/16 , C10G2300/1022 , C10G2300/302 , C10G2400/10 , C10M107/02 , C10M171/02 , C10M2203/1025 , C10M2205/163 , C10M2205/173 , C10M2209/084 , C10N2220/022 , C10N2220/025 , C10N2220/028 , C10N2230/02 , C10N2230/06 , C10N2230/10 , C10N2230/36 , C10N2240/10 , C10N2270/00
摘要： A lubricant base oil that is a hydrocarbon oil that satisfies any of the following conditions (i), (ii) and (iii): (i) a hydrocarbon oil having a kinematic viscosity at 100° C. of 3.0 to 5.0 mm2/s, a viscosity index of 145 or more, and an SBV viscosity at −20° C. of 3,000 to 60,000 mPa·s, (ii) a hydrocarbon oil having a kinematic viscosity at 100° C. of 5 to 9 mm2/s, a viscosity index of 155 or more, and an SBV viscosity at −20° C. of 3,000 to 30,000 mPa·s, and (iii) a hydrocarbon oil having a kinematic viscosity at 100° C. of 2.0 to 3.0 mm2/s, a viscosity index of 130 or more, and an SBV viscosity at −30° C. of 1,000 to 30,000 mPa·s.
摘要翻译： 一种润滑油基油，其为满足以下条件（i），（ii）和（iii）中的任何一种的烃油：（i）100℃下的运动粘度为3.0〜5.0mm 2 / s的烃油 粘度指数为145以上，-20℃下的SBV粘度为3000〜60000mPa·s，（ii）100℃下的运动粘度为5〜9mm 2 / s的烃油， 粘度指数为155以上，-20℃下的SBV粘度为3,000〜30,000mPa·s，（iii）100℃下的运动粘度为2.0〜3.0mm 2 / s的烃油， 粘度指数为130以上，-30℃下的SBV粘度为1000〜30,000mPa·s。
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8.发明申请CATALYST FOR PRODUCING MONOCYCLIC AROMATIC HYDROCARBONS, AND METHOD FOR PRODUCING MONOCYCLIC AROMATIC HYDROCARBONS 审中-公开用于生产单环芳香烃的催化剂，以及生产单环芳香烃的方法公开(公告)号：US20140364667A1
公开(公告)日：2014-12-11
申请号：US14467707
申请日：2014-08-25
IPC分类号： C07C4/06
CPC分类号： C07C4/06 , B01J29/061 , B01J29/405 , B01J37/28 , B01J2229/37 , C07C2529/06 , C07C2529/40 , C07C2529/87 , C10G45/68 , C10G2300/1033 , C10G2300/1044 , C10G2300/1048 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2300/301 , C10G2400/30
摘要： A catalyst for producing monocyclic aromatic hydrocarbons of 6 to 8 carbon number from a feedstock oil having a 10 volume % distillation temperature of at least 140° C. and an end point temperature of not more than 400° C., or a feedstock oil having a 10 volume % distillation temperature of at least 140° C. and a 90 volume % distillation temperature of not more than 360° C., wherein the catalyst contains a crystalline aluminosilicate, gallium and/or zinc, and phosphorus, and the amount of phosphorus supported on the crystalline aluminosilicate is within a range from 0.1 to 1.9% by mass based on the mass of the crystalline aluminosilicate; and a method for producing monocyclic aromatic hydrocarbons, the method involving bringing a feedstock oil having a 10 volume % distillation temperature of at least 140° C. and an end point temperature of not more than 400° C., or a feedstock oil having a 10 volume % distillation temperature of at least 140° C. and a 90 volume % distillation temperature of not more than 360° C., into contact with the above-mentioned catalyst for producing monocyclic aromatic hydrocarbons.
摘要翻译： 一种催化剂，用于从具有10体积％蒸馏温度至少为140℃，终点温度不高于400℃的原料油生产6至8个碳原子的单环芳族烃，或具有 至少140℃的10体积％蒸馏温度和不高于360℃的90体积％蒸馏温度，其中所述催化剂含有结晶硅铝酸盐，镓和/或锌和磷，以及 在结晶硅铝酸盐上负载的磷的含量相对于结晶性铝硅酸盐的质量为0.1〜1.9质量％ 和单环芳烃的制造方法，其特征在于，使具有10体积％馏出温度的原料油为至少140℃，终点温度为400℃以下的方法， 10体积％的蒸馏温度为至少140℃，90体积％蒸馏温度为不高于360℃，与上述用于制备单环芳烃的催化剂接触。
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9.发明申请CATALYST FOR PRODUCING MONOCYCLIC AROMATIC HYDROCARBONS, AND METHOD FOR PRODUCING MONOCYCLIC AROMATIC HYDROCARBONS 审中-公开用于生产单环芳香烃的催化剂，以及生产单环芳香烃的方法公开(公告)号：US20140364666A1
公开(公告)日：2014-12-11
申请号：US14466444
申请日：2014-08-22
IPC分类号： C07C4/06
CPC分类号： C07C4/06 , B01J29/061 , B01J29/405 , B01J37/28 , B01J2229/37 , C07C2529/06 , C07C2529/40 , C07C2529/85 , C07C2529/87 , C10G2300/1033 , C10G2300/1044 , C10G2300/1048 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2300/301 , C10G2400/30
摘要： A catalyst for producing monocyclic aromatic hydrocarbons, used for producing monocyclic aromatic hydrocarbons of 6 to 8 carbon number from a feedstock oil having a 10 volume % distillation temperature of at least 140° C. and an end point temperature of not more than 400° C., wherein the catalyst contains a crystalline aluminosilicate, gallium and/or zinc, and phosphorus, the molar ratio between silicon and aluminum (Si/Al ratio) in the crystalline aluminosilicate is not more than 100, the molar ratio between the phosphorus supported on the crystalline aluminosilicate and the aluminum of the crystalline aluminosilicate (P/Al ratio) is not less than 0.01 and not more than 1.0, and the amount of gallium and/or zinc is not more than 1.2% by mass based on the mass of the crystalline aluminosilicate.
摘要翻译： 一种用于生产单环芳烃的催化剂，用于从具有10体积％蒸馏温度至少为140℃，终点温度不超过400℃的原料油制备6至8个碳原子的单环芳烃 ，其中催化剂含有结晶硅铝酸盐，镓和/或锌和磷，结晶硅铝酸盐中硅和铝之间的摩尔比（Si / Al比）不大于100，所支持的磷之间的摩尔比 结晶硅铝酸盐和结晶硅铝酸盐（P / Al比）的结晶铝硅酸盐和铝的含量不小于0.01且不大于1.0，镓和/或锌的量不超过1.2质量％ 结晶硅铝酸盐。
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公开(公告)号：US09663422B2
公开(公告)日：2017-05-30
申请号：US14388377
申请日：2013-03-29
CPC分类号： C07C5/2775 , B01J29/068 , B01J2229/42 , C07C4/06 , C07C5/02 , C07C2529/068 , C10G45/58 , C10G45/64 , C10G65/043 , C10G2300/301
摘要： A method for producing a lubricant base oil which comprises a first step of carrying out isomerization dewaxing by contacting, in the presence of hydrogen, a hydrocarbon oil containing normal paraffin having a boiling point of 360° C. or higher, with a hydroisomerization catalyst under conditions such that a cracking rate defined in the following formula (1) is 10 mass % or less, and a second step of carrying out the above isomerization dewaxing by temporarily switching the above conditions to conditions such that the cracking rate is 13 mass % or more. Cracking rate (mass %)=[(C1−C2)/C1]×100 (1) wherein C1 represents the mass ratio of a fraction having a boiling point of 360° C. or higher in the above hydrocarbon oil, and C2 represents the mass ratio of the fraction having a boiling point of 360° C. or higher in the above hydrocarbon oil after the isomerization dewaxing.
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