公开(公告)号：EP2000203A4

公开(公告)日：2012-07-25

申请号：EP07740182

申请日：2007-03-22

申请人： NIPPON OIL CORP

发明人： HIGASHI MASAHIRO ,  SEKI HIROYUKI ,  SAITO SUMIO ,  KURODA RYUZO ,  KAMEOKA TAKASHI

IPC分类号： B01J29/12 ,  C10G47/18

CPC分类号： B01J29/126 ,  B01J21/12 ,  B01J35/002 ,  B01J35/023 ,  B01J37/0009 ,  B01J2229/20 ,  B01J2229/42 ,  C10G47/16 ,  C10G47/18 ,  C10G2300/1022

公开(公告)号：EP2119757A1

公开(公告)日：2009-11-18

申请号：EP08825881.9

申请日：2008-03-04

申请人： Nippon Oil Corporation

发明人： NAGAYASU, Yoshiyuki ,  SEGAWA, Atsushi ,  MIYAZAWA, Kazunori ,  KOBORI, Yoshihiro

IPC分类号： C10L3/00 ,  B01J29/12 ,  B01J29/14 ,  C01B3/38 ,  C01B39/22 ,  C01B39/24 ,  C10G25/03 ,  H01M8/06 ,  H01M8/10

CPC分类号： C10L3/12 ,  B01D53/02 ,  B01D53/04 ,  B01D2253/108 ,  B01D2253/1124 ,  B01D2256/245 ,  B01D2257/306 ,  B01D2257/308 ,  B01D2259/4145 ,  B01J20/186 ,  C01B3/384 ,  C01B2203/0233 ,  C01B2203/0261 ,  C01B2203/0283 ,  C01B2203/0405 ,  C01B2203/044 ,  C01B2203/047 ,  C01B2203/0822 ,  C01B2203/0827 ,  C01B2203/1058 ,  C01B2203/1064 ,  C01B2203/107 ,  C01B2203/1223 ,  C01B2203/1258 ,  C01B2203/127 ,  C10G25/05 ,  C10G53/08 ,  C10G2300/202 ,  C10G2400/28 ,  C10L3/102 ,  H01M8/0618 ,  H01M8/0668 ,  H01M8/0675 ,  H01M2008/1095 ,  Y02P20/128 ,  Y02P20/52 ,  Y10S502/517

摘要： The present invention provides a desulfurization system for desulfurizing a hydrocarbon fuel containing a light amount of methanol and a slight amount of water. The desulfurization system comprises a Y-type zeolite-based desulfurizing agent containing at least copper arranged upstream of the system and an X-type zeolite-based desulfurizing agent containing at least silver arranged downstream of the system and thus can maintain desulfurization effect for a long period of time.

公开(公告)号：EP1354853A4

公开(公告)日：2009-08-19

申请号：EP02710339

申请日：2002-01-24

申请人： PANASONIC CORP

发明人： TAGUCHI KIYOSHI ,  UKAI KUNIHIRO ,  FUJIWARA SEIJI ,  TOMIZAWA TAKESHI ,  WAKITA HIDENOBU

IPC分类号： B01J23/00 ,  B01J23/63 ,  B01J23/64 ,  B01J23/652 ,  B01J23/656 ,  B01J23/89 ,  C01B3/16 ,  C01B3/48 ,  C10K3/04 ,  H01M8/06 ,  B01J23/42 ,  B01J29/068 ,  B01J29/072 ,  B01J29/12 ,  B01J29/14 ,  B01J29/16 ,  B01J29/22 ,  B01J29/44 ,  B01J29/62 ,  B01J29/74 ,  B01J29/89

CPC分类号： H01M8/0662 ,  B01J8/009 ,  B01J8/0453 ,  B01J8/048 ,  B01J8/0496 ,  B01J19/2485 ,  B01J23/002 ,  B01J23/63 ,  B01J23/64 ,  B01J23/652 ,  B01J23/6567 ,  B01J23/89 ,  B01J23/8993 ,  B01J2208/00194 ,  B01J2208/00495 ,  C01B3/16 ,  C01B3/48 ,  C01B2203/0233 ,  C01B2203/0283 ,  C01B2203/0288 ,  C01B2203/044 ,  C01B2203/047 ,  C01B2203/066 ,  C01B2203/0811 ,  C01B2203/0822 ,  C01B2203/0827 ,  C01B2203/0883 ,  C01B2203/1023 ,  C01B2203/1064 ,  C01B2203/1076 ,  C01B2203/1082 ,  C01B2203/1094 ,  C01B2203/1241 ,  C01B2203/1288 ,  C01B2203/1604 ,  C01B2203/1609 ,  C01B2203/1619 ,  C01B2203/1661 ,  C01B2203/1676 ,  C10K3/04 ,  H01M8/0612 ,  Y02P20/128 ,  Y02P20/52

摘要： Conventional hydrogen purification apparatuses cannot be used satisfactorily for applications in which much time is required for startup of the apparatus, and the apparatus is repeatedly started and stopped at frequent intervals because of complicated handling. In a hydrogen purification apparatus comprising at least a catalysis body 1 removing carbon monoxide from a reformed gas containing hydrogen, carbon monoxide and steam, the catalyst body 1 is constituted by a carrier comprised of a complex oxide in which at least one of Mo, W and Re is compounded with Zr, or comprised of an oxide of one of Mo, W, Re and Zr, and at least one of Pt, Pd, Rh and Ru carried on the surface of the carrier.

公开(公告)号：EP1953208A1

公开(公告)日：2008-08-06

申请号：EP07706962.3

申请日：2007-01-18

申请人： Nippon Oil Corporation

发明人： SEKI, Hiroyuki ,  HIGASHI, Masahiro ,  HATAYAMA, Minoru

IPC分类号： C10G65/10 ,  B01J29/12 ,  C10G47/18 ,  C10G47/20

CPC分类号： B01J29/084 ,  B01J21/02 ,  B01J29/126 ,  B01J35/023 ,  B01J2229/20 ,  B01J2229/42 ,  C10G47/12 ,  C10G47/16 ,  C10G47/18 ,  C10G2300/1022 ,  C10G2300/4081

摘要： The hydrocracking method of wax of the invention is a hydrocracking process wherein crude wax is subjected to hydrocracking and the untreated wax fraction that is produced after the hydrocracking is re-supplied for hydrocracking, and wherein hydrocracking of the mixture of the crude wax and untreated wax fraction is carried out in such a manner for a conversion ratio of 50-85 % by mass from the wax fraction with a boiling point of 360°C or above to the light fraction with a boiling point of below 360°C in the presence of a hydrocracking catalyst. It is thereby possible to simultaneously achieve both an increased heart-cut fraction yield (as the product of the hydrocracking) and a reduced normal paraffin content in the heart-cut fraction when the untreated wax is hydrocracked by a bottom recycling system.

摘要翻译： 本发明的蜡的加氢裂化方法是加氢裂化方法，其中将粗蜡进行加氢裂化，再加氢裂化后产生的未处理的蜡馏分用于加氢裂化，其中粗蜡和未处理蜡的混合物的加氢裂化 从沸点为360℃以上的蜡馏分的转化率为50〜85质量％，沸点低于360℃的轻馏分在存在下进行， 加氢裂化催化剂。 因此，当未处理的蜡被底部回收系统加氢裂化时，可以同时实现增加的心切分数产率（作为加氢裂化产物）和降心馏分中降低的正链烷烃含量。

公开(公告)号：EP1614739A1

公开(公告)日：2006-01-11

申请号：EP04717744.9

申请日：2004-03-05

申请人： Nippon Oil Corporation

发明人： IKI, Hideshi, c/o Nippon Oil Corporation ,  SUGIURA, Yukihiro, c/o Nippon Oil Corporation ,  TANAKA, Yuichi, c/o Nippon Oil Corporation

IPC分类号： C10G45/10 ,  C10G45/44 ,  C10G65/04 ,  B01J23/44 ,  B01J29/12

CPC分类号： C10G45/44 ,  B01J29/126 ,  C10G2300/1059 ,  C10G2300/202 ,  C10G2300/301 ,  C10G2300/4018 ,  C10G2400/06

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： 本发明的瓦斯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，总芳族化合物含量为10-25体积％和沸点范围为150的加氢精制石油基烃油 -380℃作为原料油，并在加氢催化剂存在下对原料油进行加氢处理，以获得硫含量不超过1质量ppm且总芳族含量低的超低硫和低芳烃轻油馏分 不大于1体积％。 该加氢处理方法允许以有效且可靠的方式生产“零硫”和“零芳族”瓦斯油馏分，而无需提供特殊的操作条件或设备投资。

公开(公告)号：EP1560898A1

公开(公告)日：2005-08-10

申请号：EP03776274.7

申请日：2003-10-10

申请人： Chevron U.S.A. Inc.

发明人： TIMKEN, Hye, Kyung, C.

IPC分类号： C10G47/16 ,  C10G47/18 ,  C10G47/20 ,  B01J29/10 ,  B01J29/12 ,  B01J29/16

CPC分类号： C10G47/18 ,  B01J29/084 ,  B01J29/126 ,  B01J29/166 ,  B01J2229/16 ,  B01J2229/42 ,  C10G45/06 ,  C10G45/08 ,  C10G45/10 ,  C10G45/12 ,  C10G45/62 ,  C10G45/64 ,  C10G47/20 ,  C10G2300/1059 ,  C10G2400/10

摘要： A catalyst composition comprising a minor amount of a low acidity, highly dealuminated ultra stable Y zeolite having an Alpha value of less than about 5, preferable less than about 3 and Broensted acidity measured by FT-IR from about 1 to about 20, preferably from about 1-10, micro mole/g of, a homogeneous, amorphous silica-alumina cracking component having an SB ratio of from about 0.7 to about 1.3, wherein a crystalline alumina phase is present in an amount of no greater than about 10%, preferably no greater than 5% and a catalytic amount of hydrogenation component selected from the group consisting of a Group VI metal, a Group VIII metal, and mixtures thereof is disclosed. The present invention provides for a process for converting hydrocarbonaceous oils comprising contacting the hydrocarbonaceous oils with the catalyst under suitable hydrocarbon conversion conditions. Such processes in include, but are not limited to, single stage hydrocracking, two-stage hydrocracking, series-flow hydrocracking, mild hydrocracking, lube hydrocracking, hydrotreating, lube hydrofinishing, hydrodesulphurization, hydrode nitrification, catalytic dewaxing and catalytic cracking.

公开(公告)号：EP1342708A4

公开(公告)日：2004-03-31

申请号：EP01270512

申请日：2001-12-03

申请人： IDEMITSU PETROCHEMICAL CO

发明人： KOJIMA AKIO ,  KODOI KOUICHI ,  TSURUTA SHUNJI ,  OGATA MASAMITSU

IPC分类号： C07C6/10 ,  B01J29/06 ,  B01J29/08 ,  B01J29/12 ,  C07B61/00 ,  C07C5/27 ,  C07C5/29 ,  C07C13/615 ,  B01J37/30

CPC分类号： C07C5/2702 ,  B01J29/061 ,  B01J29/085 ,  B01J29/126 ,  B01J2229/18 ,  B01J2229/24 ,  B01J2229/36 ,  B01J2229/37 ,  C07C5/29 ,  C07C2523/42 ,  C07C2529/08 ,  C07C2603/74 ,  C07C13/615

摘要： There is provided a process for producing adamantane and analogues thereof, namely a hydrocarbon having an adamantane structure which process comprises isomerizing a tricyclic saturated hydrocarbon having ten or more carbon atoms in the presence of a catalyst in which one or two or more metals selected from among the metals belonging to group VIII in the Periodic Table (group 8 to 10 in the new Periodic Table) are supported on zeolite by means of an ion exchange method. It is made possible by the above process to efficiently produce adamantane and analogues thereof in the presence of a solid catalyst without the use of hydrogen chloride.

摘要翻译： 提供了一种生产金刚烷及其类似物的方法，即具有金刚烷结构的烃，该方法包括在催化剂存在下异构化具有十个以上碳原子的三环饱和烃，其中一种或两种以上选自 属于周期表第VIII族的金属（新的周期表中的第8至10个）通过离子交换法负载在沸石上。 通过上述方法可以在不使用氯化氢的情况下在固体催化剂的存在下有效地产生金刚烷及其类似物。

公开(公告)号：EP0708807A4

公开(公告)日：1996-06-12

申请号：EP94923458

申请日：1994-07-11

IPC分类号： B01J29/08 ,  B01J29/40 ,  B01J29/70 ,  B01J29/80 ,  C10G11/05 ,  B01J29/10 ,  B01J29/12 ,  C10G11/18

CPC分类号： C10G11/05 ,  B01J29/084 ,  B01J29/40 ,  B01J29/7007 ,  B01J29/80

摘要： A novel catalyst composition and process for catalytic cracking of a hydrocarbon oil. The catalyst comprises zeolite beta and a shape selective cracking component, preferably ZSM-5, and may include conventional cracking catalyst components such as zeolite Y. These components may be present in one particle or as a blend of separate particle additives. The composition increases light olefin yields and gasoline octane as compared to catalyst containing either, but not both of, ZSM-5 and zeolite beta.

摘要翻译： 一种用于烃油催化裂化的新型催化剂组合物和方法。 该催化剂包含沸石β和形状选择性裂化组分，优选ZSM-5，并且可以包括常规裂化催化剂组分如沸石Y.这些组分可以存在于一个颗粒中或作为单独颗粒添加剂的混合物存在。 与含有ZSM-5和沸石β的催化剂相比，该组合物增加了轻质烯烃产率和汽油辛烷值。

公开(公告)号：EP0016495B1

公开(公告)日：1982-07-21

申请号：EP80200214.7

申请日：1980-03-06

申请人： SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.

发明人： Wagstaff, Nigel

IPC分类号： C07C9/04 ,  C07C9/06 ,  C07C4/06 ,  C07C6/10 ,  B01J29/04 ,  B01J29/12

CPC分类号： C07C4/06 ,  B01J29/70 ,  B01J29/7049 ,  B01J29/74 ,  B01J2229/40 ,  C07C2521/08 ,  C07C2523/40 ,  C07C9/06 ,  C07C9/04

公开(公告)号：EP0016495A1

公开(公告)日：1980-10-01

申请号：EP80200214.7

申请日：1980-03-06

申请人： SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.

发明人： Wagstaff, Nigel

IPC分类号： C07C9/04 ,  C07C9/06 ,  C07C4/06 ,  C07C6/10 ,  B01J29/04 ,  B01J29/12

CPC分类号： C07C4/06 ,  B01J29/70 ,  B01J29/7049 ,  B01J29/74 ,  B01J2229/40 ,  C07C2521/08 ,  C07C2523/40 ,  C07C9/06 ,  C07C9/04

摘要： A mixture of methane and ehtane is prepared from C 2 - 4 paraffins of which the average numbers of carbon atoms is at least 0.5 higher, by contacting the paraffins at a pressure above 10 bar with ZSM-5 having an Al 2 O 3 /SiO 2 molar ratio of at least 0.005.