公开(公告)号：US10076773B2

公开(公告)日：2018-09-18

申请号：US13817218

申请日：2011-08-12

申请人： Shinya Takahashi ,  Kazuhiko Tasaka ,  Yuichi Tanaka ,  Marie Iwama

发明人： Shinya Takahashi ,  Kazuhiko Tasaka ,  Yuichi Tanaka ,  Marie Iwama

IPC分类号： B08B3/08 ,  B08B3/10 ,  B08B9/08 ,  B08B3/04 ,  C10G1/06 ,  C10G47/22 ,  C10G47/00 ,  C10G21/12 ,  C10G47/36 ,  C10G2/00 ,  B01J38/52 ,  B01J38/56

CPC分类号： B08B3/04 ,  B01J38/52 ,  B01J38/56 ,  B08B9/08 ,  C10G1/06 ,  C10G2/32 ,  C10G21/12 ,  C10G47/00 ,  C10G47/22 ,  C10G47/36 ,  C10G2300/1014 ,  C10G2300/1022 ,  C10G2300/4031 ,  C10G2300/44 ,  Y02P30/20

摘要： The method for cleaning a reactor of the present invention comprises passing a solvent through a wax-fraction hydrocracking apparatus which is charged with a catalyst and to which supply of a wax fraction is stopped, wherein the solvent comprising at least one oil selected from a group consisting of hydrocarbon and vegetable oils, and having a sulfur content of less than 5 ppm and being in a liquid state at 15° C.

公开(公告)号：US09839904B2

公开(公告)日：2017-12-12

申请号：US14007711

申请日：2012-03-26

申请人： Marie Iwama

发明人： Marie Iwama

IPC分类号： B01J29/10 ,  B01J29/16 ,  B01J37/00 ,  B01J29/12 ,  C10G47/14 ,  C10G65/14 ,  C10G45/10 ,  C10G49/06 ,  B01J21/12

CPC分类号： B01J29/126 ,  B01J21/12 ,  B01J29/106 ,  B01J29/166 ,  B01J37/0018 ,  B01J2229/20 ,  B01J2229/42 ,  C10G45/10 ,  C10G47/14 ,  C10G49/06 ,  C10G65/14 ,  C10G2300/1022

摘要： The present invention provides a method for producing a hydroprocessing catalyst including a supporting step of allowing a catalyst support having a content of a carbonaceous substance containing carbon atoms of 0.5% by mass or less in terms of carbon atoms to support an active metal component containing at least one active metal element selected from metals belonging to Group 6, Group 8, Group 9 and Group 10 in the periodic table, to obtain a catalyst precursor, and a calcining step of calcining the catalyst precursor obtained in the supporting step to obtain the hydroprocessing catalyst.

公开(公告)号：US09725656B2

公开(公告)日：2017-08-08

申请号：US14008509

申请日：2012-03-22

申请人： Shuhei Wakamatsu ,  Fuyuki Yagi ,  Tomoyuki Mikuriya ,  Kenichi Kawazuishi

发明人： Shuhei Wakamatsu ,  Fuyuki Yagi ,  Tomoyuki Mikuriya ,  Kenichi Kawazuishi

IPC分类号： C10G2/00 ,  C10G49/00 ,  C10K1/00 ,  C01B3/38 ,  C01B3/54 ,  C10G45/00

CPC分类号： C10G2/30 ,  C01B3/38 ,  C01B3/384 ,  C01B3/54 ,  C01B2203/0233 ,  C01B2203/0238 ,  C01B2203/0415 ,  C01B2203/0435 ,  C01B2203/0465 ,  C01B2203/0475 ,  C01B2203/062 ,  C01B2203/0811 ,  C01B2203/0894 ,  C01B2203/1047 ,  C01B2203/1082 ,  C01B2203/1241 ,  C01B2203/1258 ,  C01B2203/148 ,  C10G45/00 ,  C10G49/00 ,  C10G2300/1025 ,  C10G2300/4081 ,  C10K1/005 ,  C10K1/007 ,  Y02P20/129

摘要： A synthesis gas production apparatus (reformer) to be used for a synthesis gas production step in a GTL (gas-to-liquid) process is prevented from being contaminated by metal components. A method of suppressing metal contamination of a synthesis gas production apparatus operating for a GTL process that includes a synthesis gas production step of producing synthesis gas by causing natural gas and gas containing steam and/or carbon dioxide to react with each other for reforming in a synthesis gas production apparatus in which, at the time of separating and collecting a carbon dioxide contained in the synthesis gas produced in the synthesis gas production step and recycling the separated and collected carbon dioxide as source gas for the reforming reaction in the synthesis gas production step, a nickel concentration in the recycled carbon dioxide is not higher than 0.05 ppmv.

公开(公告)号：US09513051B2

公开(公告)日：2016-12-06

申请号：US14251816

申请日：2014-04-14

申请人： Japan Oil, Gas and Metals National Corporation ,  INPEX Corporation ,  JX Nippon Oil & Energy Corporation ,  Japan Petroleum Exploration Co., Ltd. ,  Cosmo Oil Co., Ltd. ,  Nippon Steel & Sumikin Engineering Co., Ltd.

发明人： Kazuhiko Tasaka

IPC分类号： F25J3/08 ,  C10G2/00 ,  C10G31/06

CPC分类号： F25J3/08 ,  C10G2/30 ,  C10G31/06 ,  C10G2300/1022 ,  C10G2300/4081

摘要： There is provided a method for recovering hydrocarbon compounds from a gaseous by-products generated in the Fisher-Tropsch synthesis reaction, the method comprising a pressurizing step in which the gaseous by-products are pressurized, a cooling step in which the pressurized gaseous by-products are pressurized to liquefy hydrocarbon compounds in the gaseous by-products, and a separating step in which the hydrocarbon compounds liquefied in the cooling step are separated from the remaining gaseous by-products.

摘要翻译： 提供了一种从费 - 托合成反应产生的气态副产物中回收烃化合物的方法，该方法包括加压步骤，其中气态副产物被加压，冷却步骤， 将产物加压至气态副产物中的液化烃化合物，并且将在冷却步骤中液化的烃化合物与剩余气态副产物分离的分离步骤。

公开(公告)号：US09421509B2

公开(公告)日：2016-08-23

申请号：US14004954

申请日：2012-03-13

申请人： Shinya Arai

发明人： Shinya Arai

IPC分类号： B01J8/00 ,  B01J8/08 ,  B01J19/00 ,  B01J19/24 ,  C10G2/00 ,  C07C1/00 ,  C07C1/02

CPC分类号： B01J8/08 ,  B01J2208/00796 ,  C07C1/02 ,  C10G2/00 ,  C10G2300/1022 ,  C10G2300/304 ,  C10G2300/4031

摘要： The hydrocarbon production apparatus is provided with a gas-liquid separator for cooling gaseous state hydrocarbons drawn out from a gas phase portion of a reactor for the Fischer-Tropsch synthesis reaction and liquefying a portion of the hydrocarbons. A light liquid hydrocarbon supply line for supplying light hydrocarbons is disposed between a downstream side line which is downstream from the last stage of a gas-liquid separating unit of the gas-liquid separator, and an upstream side line which is upstream from the last stage of the gas-liquid separating unit of the gas-liquid separator, wherein the downstream side line is a liquid hydrocarbon line on the downstream side through which the light hydrocarbons having cloud points lower than the temperature at an outlet of a cooler in the last stage of the gas-liquid separating unit are flowed.

摘要翻译： 烃制造装置设置有用于冷却从费 - 托合成反应的反应器的气相部分抽出的气态烃并液化一部分烃的气液分离器。 用于供给轻质烃的轻液态碳氢化合物供给管路配置在气液分离器的气液分离装置的最后级的下游侧的下游侧管线和最后级的上游侧的上游侧管线 气液分离器的气液分离单元，其中下游侧线是下游侧的液体碳氢化合物管线，其中浊点低于最后阶段的冷却器出口处的温度 的气液分离装置。

公开(公告)号：US20160046969A1

公开(公告)日：2016-02-18

申请号：US14778916

申请日：2014-03-19

申请人： COSMO OIL CO., LTD.

发明人： Masaru SAITO ,  Taishi YAMAMOTO ,  Haruki KAWANO

IPC分类号： C12P13/00

CPC分类号： C12P13/005 ,  C12N1/00

摘要： Provided is a method for producing 5-aminolevulinic acid or a salt thereof at a high yield using 5-aminolevulinic acid-producing microorganisms. The method for producing 5-aminolevulinic acid or a salt thereof comprises culturing 5-aminolevulinic acid-producing microorganisms in a medium comprising one or more components selected from the group consisting of L-arginine, glutamic acid, and a salt thereof. The content of glutamic acid or the salt thereof is from 42 to 100 mM in the medium as the glutamic acid.

摘要翻译： 提供了使用5-氨基乙酰丙酸生产微生物以高产率生产5-氨基乙酰丙酸或其盐的方法。 生产5-氨基乙酰丙酸或其盐的方法包括在包含一种或多种选自L-精氨酸，谷氨酸及其盐的组分的培养基中培养5-氨基乙酰丙酸生产微生物。 在作为谷氨酸的培养基中，谷氨酸或其盐的含量为42〜100mM。

公开(公告)号：US09186658B2

公开(公告)日：2015-11-17

申请号：US14008164

申请日：2012-03-26

申请人： Yuichi Tanaka ,  Takuya Niitsuma ,  Kazuhiko Tasaka ,  Marie Iwama

发明人： Yuichi Tanaka ,  Takuya Niitsuma ,  Kazuhiko Tasaka ,  Marie Iwama

IPC分类号： B01J29/12 ,  C10G47/18 ,  C10G45/60 ,  C10G45/70 ,  C10G11/18 ,  B01J35/02 ,  B01J37/00 ,  C10G45/62 ,  C10G45/64

CPC分类号： B01J29/126 ,  B01J29/12 ,  B01J35/023 ,  B01J35/026 ,  B01J37/0018 ,  B01J2229/24 ,  C10G11/18 ,  C10G45/60 ,  C10G45/62 ,  C10G45/64 ,  C10G45/70 ,  C10G47/18 ,  C10G2300/1048 ,  C10G2300/301 ,  C10G2400/30

摘要： The hydrocracking catalyst of the present invention is a hydrocracking catalyst comprising a catalyst support comprising a zeolite and an amorphous composite metal oxide having solid acidity, and at least one active metal supported by the catalyst support and selected from noble metals of Group 8 to Group 10 in the periodic table, wherein the hydrocracking catalyst contains a carbonaceous substance comprising a carbon atom, and the content of the carbonaceous substance in the hydrocracking catalyst is 0.05 to 1% by mass in terms of the carbon atom.

摘要翻译： 本发明的加氢裂化催化剂是包含催化剂载体的加氢裂化催化剂，该催化剂载体包含沸石和具有固体酸度的无定形复合金属氧化物，以及至少一种由催化剂载体负载的活性金属，并选自第8〜10族的贵金属 在周期表中，其中加氢裂化催化剂含有碳原子的碳质物质，加氢裂化催化剂中的碳质物质的含量相对于碳原子为0.05〜1质量％。

公开(公告)号：US20150166900A1

公开(公告)日：2015-06-18

申请号：US14628777

申请日：2015-02-23

申请人： JAPAN OIL, GAS AND METALS NATIONAL CORPORATION ,  INPEX CORPORATION ,  JX NIPPON OIL & ENERGY CORPORATION ,  JAPAN PETROLEUM EXPLORATION CO., LTD. ,  COSMO OIL CO., LTD. ,  NIPPON STEEL & SUMIKIN ENGINEERING CO., LTD.

发明人： Yuichi TANAKA

IPC分类号： C10G2/00 ,  B01J8/18 ,  B01J8/22

CPC分类号： C10G2/34 ,  B01D37/048 ,  B01D43/00 ,  B01J8/006 ,  B01J8/1809 ,  B01J8/22 ,  B01J2208/00017 ,  B01J2219/00083 ,  C10G2/342 ,  C10G3/60 ,  C10G2300/4006 ,  Y02P30/20

摘要： The present invention provides a process for producing a hydrocarbon oil by performing a Fischer-Tropsch synthesis reaction using a reactor for a Fischer-Tropsch synthesis including a reaction apparatus having a slurry containing catalyst particles and a gaseous phase located above the slurry to obtain a hydrocarbon oil, wherein the Fischer-Tropsch reaction is performed while controlling a temperature of the slurry so that a difference T2−T1 between the average temperature T1 of the slurry and a temperature T2 at the liquid level of the slurry in contact with the gaseous phase is 5 to 30° C.

摘要翻译： 本发明提供一种通过使用费 - 托合成反应器进行费 - 托合成反应的方法，包括具有含有催化剂颗粒的淤浆和位于浆料上方的气相的反应装置，以获得烃 油，其中在控制浆料的温度的同时进行费 - 托反应，使得浆料的平均温度T1与在与气相接触的浆料的液面处的温度T2之间的差T2-T1为 5〜30℃

公开(公告)号：US08951408B2

公开(公告)日：2015-02-10

申请号：US12998198

申请日：2009-09-25

申请人： Yuichi Tanaka ,  Hidekatsu Honda

发明人： Yuichi Tanaka ,  Hidekatsu Honda

IPC分类号： C07C5/02 ,  C07C5/09 ,  C07C5/10 ,  C07C5/11 ,  C10G45/02 ,  C10G45/00 ,  C10G59/02

CPC分类号： C10G45/02 ,  C10G45/00 ,  C10G59/02 ,  C10G2300/1022 ,  C10G2300/1044 ,  C10G2300/4031 ,  C10G2300/44 ,  C10G2400/02

摘要： A method for starting-up a naphtha fraction hydrotreating reactor which subjects a naphtha fraction obtained in a fractionator by fractional distillation of hydrocarbon compounds produced by a Fischer-Tropsch synthesis reaction to hydrotreating, the method comprising: charging in advance an inactive hydrocarbon compound corresponding to the naphtha fraction into a vapor-liquid separator to which hydrogenated naphtha, which has been subjected to hydrotreating in the naphtha fraction hydrotreating reactor, is transferred; mixing the inactive hydrocarbon compound drawn from the vapor-liquid separator and the naphtha fractions being transferred from the fractionator to the naphtha fraction hydrotreating reactor, and supplying a mixture of the naphtha fractions and the inactive hydrocarbon compound to the naphtha fraction hydrotreating reactor.

摘要翻译： 一种用于启动石脑油馏分加氢处理反应器的方法，该方法包括：将通过费 - 托合成反应生产的烃化合物通过分馏在分馏塔中获得的石脑油馏分进行加氢处理，所述方法包括：预先将对应于 石脑油馏分转移到已经在石脑油馏分加氢处理反应器中进行加氢处理的氢化石脑油的气液分离器中; 将从气液分离器抽取的惰性烃化合物和从分馏塔转移到石脑油馏分加氢处理反应器的石脑油馏分混合，并将石脑油馏分和非活性烃化合物的混合物供给石脑油馏分加氢处理反应器。

公开(公告)号：US08906314B2

公开(公告)日：2014-12-09

申请号：US12998203

申请日：2009-09-25

申请人： Yasuhiro Onishi ,  Yuzuru Kato ,  Eiichi Yamada ,  Atsushi Murata ,  Osamu Wakamura

发明人： Yasuhiro Onishi ,  Yuzuru Kato ,  Eiichi Yamada ,  Atsushi Murata ,  Osamu Wakamura

IPC分类号： B01J8/22 ,  C07C1/04 ,  C10G2/00

CPC分类号： C10G2/342 ,  B01J8/22 ,  B01J2208/00141 ,  B01J2208/00203 ,  B01J2208/00548 ,  B01J2208/0061 ,  B01J2219/00006 ,  C10G2/32

摘要： A bubble column reactor includes a reactor body which contains a slurry having solid catalyst particles suspended in a liquid, an inflow port which is provided at the bottom of the reactor body and allows a synthesis gas including a carbon monoxide gas and a hydrogen gas as the main components to flow into the slurry therethrough, and an outflow port which is provided at the top of the reactor body and allows gaseous hydrocarbons synthesized by a chemical reaction between the synthesis gas and the slurry, an unreacted synthesis gas, and the like to flow out therethrough. The distance in a vertical direction between the liquid surface of the slurry and the outflow port is 1.4 m or more and 10 m or less.

摘要翻译： 泡罩塔反应器包括反应器主体，其包含悬浮在液体中的固体催化剂颗粒的浆料，设置在反应器主体的底部并允许包含一氧化碳气体和氢气的合成气作为流入口的流入口 主要组分流入浆料，以及流出口，其设置在反应器主体的顶部，并允许通过合成气和浆料之间的化学反应合成的气态烃，未反应的合成气等流动 从中穿过。 浆液的液面与流出口之间的垂直方向的距离为1.4μm以上且10μm以下。