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1. 发明专利

JP2010153254A Fuel cell system equipped with hydrogen generation apparatus 有权
标题翻译：燃油电池系统配备氢气发生装置
公开(公告)号：JP2010153254A
公开(公告)日：2010-07-08
申请号：JP2008331314
申请日：2008-12-25
申请人： Japan Petroleum Exploration Co Ltd , Kyushu Univ , 国立大学法人九州大学 , 石油資源開発株式会社
发明人： MORITA YASUMASA , CHAGI KAZUHISA , ISHIHARA TATSUKI
IPC分类号： H01M8/06 , C01B3/38 , C01B3/48 , C01B3/56 , H01M8/10
CPC分类号： Y02E60/521
摘要： PROBLEM TO BE SOLVED: To provide a fuel cell system that can supply high-purity hydrogen to the fuel cell with high energy efficiency. SOLUTION: The fuel cell system is provided with: a fuel cell 300; a catalytic combustion apparatus 80; a compound preheater 20 using combustion gas generated by the catalytic combustion apparatus 80; a hydrogen generation apparatus 100 provided with a catalyst reaction chamber 130 and a transmitted hydrogen reception chamber 120 that are partitioned by hydrogen transmission membranes 112 and filled with hydrocarbon reforming catalyst; a means for supplying steam to the transmitted hydrogen reception chamber 120; and a means for supplying the hydrogen generated in the hydrogen generation apparatus 100 to the fuel cell 300. COPYRIGHT: (C)2010,JPO&INPIT
摘要翻译：要解决的问题：提供一种能够以高能量效率向燃料电池供应高纯度氢的燃料电池系统。燃料电池系统设置有：燃料电池300; 催化燃烧装置80; 使用由催化燃烧装置80产生的燃烧气体的复合预热器20; 设置有由氢传递膜112分隔并填充有烃重整催化剂的催化剂反应室130和透氢接收室120的氢气发生装置100; 用于向透射的氢气接收室120供应蒸汽的装置; 以及用于将在氢气产生装置100中产生的氢气供应到燃料电池300的装置。版权所有（C）2010，JPO＆INPIT

2. 发明专利

JP2010153253A Fuel cell system equipped with oxygen generation apparatus and hydrogen generation apparatus 有权
标题翻译：装有氧气发生装置和氢气发生装置的燃油电池系统
公开(公告)号：JP2010153253A
公开(公告)日：2010-07-08
申请号：JP2008331313
申请日：2008-12-25
申请人： Japan Petroleum Exploration Co Ltd , Kyushu Univ , 国立大学法人九州大学 , 石油資源開発株式会社
发明人： MORITA YASUMASA , CHAGI KAZUHISA , ISHIHARA TATSUKI
IPC分类号： H01M8/06 , C01B3/38 , C01B3/56 , C01B13/00 , C01B13/02 , H01M8/10
CPC分类号： Y02P20/126
摘要： PROBLEM TO BE SOLVED: To provide a fuel cell system that can supply high-purity hydrogen to the fuel cell with high energy efficiency.
SOLUTION: The fuel cell system is provided with: a fuel cell 300; an oxygen generation apparatus 70 using an oxygen separation membrane; a hydrogen generation apparatus 100 provided with a catalyst reaction chamber 130 and a transmitted hydrogen reception chamber 120 that are partitioned by hydrogen transmission membranes 112 and filled with hydrocarbon reforming catalyst; a means for supplying the oxygen generated in the oxygen generation apparatus 70 to the catalyst reaction chamber 130; a means for supplying light hydrocarbon to the catalyst reaction chamber 130; a means for supplying steam to the catalyst reaction chamber 130; and a hydrogen supplying means for supplying the hydrogen generated in the hydrogen generation apparatus 100 to the fuel cell 300.
COPYRIGHT: (C)2010,JPO&INPIT
摘要翻译：要解决的问题：提供一种能够以高能量效率向燃料电池供应高纯度氢的燃料电池系统。燃料电池系统设置有：燃料电池300; 使用氧分离膜的氧气生成装置70; 设置有由氢传递膜112分隔并填充有烃重整催化剂的催化剂反应室130和透氢接收室120的氢气发生装置100; 将在氧气发生装置70中产生的氧供给到催化剂反应室130的装置; 用于将轻质烃供应到催化剂反应室130的装置; 用于向催化剂反应室130供应蒸汽的装置; 以及氢供给装置，用于将在氢气产生装置100中产生的氢气供应到燃料电池300。版权所有（C）2010，JPO＆INPIT

3. 发明专利

JP2010153255A Fuel cell system equipped with hydrogen generation apparatuses in multiple stages 有权
标题翻译：燃料电池系统配备多个级别的氢气发生装置
公开(公告)号：JP2010153255A
公开(公告)日：2010-07-08
申请号：JP2008331315
申请日：2008-12-25
申请人： Japan Petroleum Exploration Co Ltd , Kyushu Univ , 国立大学法人九州大学 , 石油資源開発株式会社
发明人： MORITA YASUMASA , CHAGI KAZUHISA , ISHIHARA TATSUKI
IPC分类号： H01M8/06 , C01B3/38
CPC分类号： Y02E60/50
摘要： PROBLEM TO BE SOLVED: To provide a fuel cell system that can supply high-purity hydrogen to the fuel cell with high energy efficiency. SOLUTION: The fuel cell system is provided with: a fuel cell 300; a catalytic combustion apparatus 80; a compound preheater 20 using combustion gas generated by the catalytic combustion apparatus 80; a first hydrogen generation apparatus 100; a second hydrogen generation apparatus 120; and a hydrogen supplying means for supplying the hydrogen generated in the first hydrogen generation apparatus 100 and the second hydrogen generation apparatus 120 to the fuel cell 300. In this case, the residual gas generated in a catalyst reaction chamber 116 of the first hydrogen generation apparatus 100 is supplied to a catalyst reaction chamber 126 of the second hydrogen generation apparatus 120. COPYRIGHT: (C)2010,JPO&INPIT
摘要翻译：要解决的问题：提供一种能够以高能量效率向燃料电池供应高纯度氢的燃料电池系统。燃料电池系统设置有：燃料电池300; 催化燃烧装置80; 使用由催化燃烧装置80产生的燃烧气体的复合预热器20; 第一氢生成装置100; 第二氢气生成装置120; 以及用于将在第一氢生成装置100和第二氢生成装置120中生成的氢供给到燃料电池300的氢供给装置。在这种情况下，在第一氢生成装置的催化剂反应室116中产生的残留气体 100被供应到第二氢气产生装置120的催化剂反应室126.版权所有（C）2010，JPO＆INPIT

4. 发明专利

JP2005281609A Process and apparatus for producing synthesis gas for fischer-tropsch synthesis 有权
标题翻译：用于生产合成气的方法和设备用于FISCHER-TROPSCH SYNTHESIS
公开(公告)号：JP2005281609A
公开(公告)日：2005-10-13
申请号：JP2004100941
申请日：2004-03-30
申请人： Chiyoda Corp , Cosmo Oil Co Ltd , Inpex Corp , Japan Oil Gas & Metals National Corp , Japan Petroleum Exploration Co Ltd , Nippon Steel Corp , コスモ石油株式会社 , 千代田化工建設株式会社 , 国際石油開発株式会社 , 新日本製鐵株式会社 , 独立行政法人石油天然ガス・金属鉱物資源機構 , 石油資源開発株式会社
发明人： IHARA MASARU , SUEHIRO YOSHIFUMI , MORITA YASUMASA , INABA KIYOSHI , SHIMIZU TOSHIO , IWAMOTO OSAMU , MIKURIYA TOMOYUKI , KAJIYAMA RYUICHIRO , FUJIMOTO KENICHIRO , ONISHI YASUHIRO
IPC分类号： C10L3/10 , B01D53/86 , B01J8/04 , B01J10/00 , C01B3/24 , C01B3/26 , C01B3/32 , C01B3/38 , C01B32/40 , C01B32/50 , C10G2/00 , C10K1/02 , C10K1/04
CPC分类号： C10G2/32 , B01D53/8603 , B01D2253/102 , B01D2257/306 , B01D2259/40 , B01J2219/00006 , C01B3/384 , C01B2203/0233 , C01B2203/0238 , C01B2203/04 , C01B2203/0475 , C01B2203/0495 , C01B2203/062 , C01B2203/0816 , C01B2203/0894 , C01B2203/1041 , C01B2203/1052 , C01B2203/1241 , C01B2203/127 , C01B2203/148 , Y02P20/124
摘要： PROBLEM TO BE SOLVED: To provide a process and an apparatus for producing a synthesis gas for Fischer-Tropsch synthesis (FT synthesis) that can produce the synthesis gas for FT synthesis having a molar ratio of hydrogen/carbon monoxide suitable for FT synthesis without inclusion of soot, can suppress the occurrence of a side reaction in a hydrodesulfurizer and the deterioration in catalytic activity due to oxidation of a reforming catalyst and is applicable to large-scale production equipment. SOLUTION: The production of the synthesis gas for FT synthesis is effected by using a production apparatus provided with an adsorption tank 11 containing an activated carbon therein for adsorbing and removing impurities in natural gas, a hydrodesulfurizer 13 for hydrogenating and desulfurizing the sulfur content in the natural gas under the condition of a hydrogen partial pressure of 100-200 kPa, a second hydrogen supply line 50 for supplying hydrogen to natural gas present between the hydrodesulfurizer 13 and a reactor 15, a reactor 15 for reacting natural gas, carbon dioxide and steam in the presence of a reforming catalyst to produce a synthesis gas and a heat recovery boiler 19 for cooling the synthesis gas at a cooling rate of 2,000-4,000°C/sec. COPYRIGHT: (C)2006,JPO&NCIPI
摘要翻译：要解决的问题：提供一种用于制备用于费 - 托合成（FT合成）的合成气的方法和设备，其可以生产适合FT的摩尔比为氢/一氧化碳的FT合成的合成气合成而不包含烟灰，可以抑制加氢脱硫剂中的副反应的发生和由于重整催化剂的氧化引起的催化活性的劣化，并且适用于大规模的生产设备。解决方案：用于FT合成的合成气的生产通过使用设置有吸附罐11的制造装置来进行，该制造装置含有用于吸附和去除天然气中的杂质的活性炭，用于使硫磺氢化和脱硫的加氢脱硫剂13 在氢分压为100-200kPa的条件下天然气中的含量，用于向存在于加氢脱硫器13和反应器15之间的天然气供应氢气的第二氢气供应管线50，用于使天然气反应的反应器15 二氧化碳和蒸汽，以产生合成气和用于以2,000-4,000℃/秒的冷却速度冷却合成气的热回收锅炉19。版权所有（C）2006，JPO＆NCIPI

5. 发明专利

JP2009242158A Method for operating synthesis gas reformer in gtl plant 有权
标题翻译： GTL工厂合成气改造方法
公开(公告)号：JP2009242158A
公开(公告)日：2009-10-22
申请号：JP2008089737
申请日：2008-03-31
申请人： Chiyoda Kako Kensetsu Kk , Cosmo Oil Co Ltd , Inpex Corp , Japan Oil Gas & Metals National Corp , Japan Petroleum Exploration Co Ltd , Nippon Oil Corp , Nippon Steel Engineering Co Ltd , コスモ石油株式会社 , 千代田化工建設株式会社 , 国際石油開発帝石株式会社 , 新日本石油株式会社 , 新日鉄エンジニアリング株式会社 , 独立行政法人石油天然ガス・金属鉱物資源機構 , 石油資源開発株式会社
发明人： MORITA YASUMASA , KAERUISHI KENICHI
IPC分类号： C01B3/38
CPC分类号： C01B3/384 , C01B2203/0233 , C01B2203/0238 , C01B2203/0405 , C01B2203/0415 , C01B2203/043 , C01B2203/0475 , C01B2203/0495 , C01B2203/062 , C01B2203/0811 , C01B2203/0827 , C01B2203/0894 , C01B2203/1058 , C01B2203/1258 , C01B2203/148 , C01B2203/1614 , C01B2203/1628 , C01B2203/169 , C01B2203/1695
摘要： PROBLEM TO BE SOLVED: To provide a method for operating a synthesis gas reformer in a GTL (gas to liquid) plant, in which the outlet temperature of the synthesis gas reformer is controlled precisely. SOLUTION: The method for operating the synthesis gas reformer 20 in the GTL plant 8 comprises the steps of: calculating the calorie required for the synthesis gas reformer 20 at any time by using operating conditions of the synthesis gas reformer 20, the composition of natural gas 111, the inlet temperature of the synthesis gas reformer 20 and the outlet pressure of the synthesis gas reformer 20; and adjusting the pressure of fuel gas according to the amount of the fuel gas 122 to be required for the calculated calorie. COPYRIGHT: (C)2010,JPO&INPIT
摘要翻译：要解决的问题：提供一种操作合成气重整器的方法，该GTL（气 - 液）装置中合成气重整器的出口温度被精确地控制。解决方案：在GTL设备8中操作合成气重整器20的方法包括以下步骤：通过使用合成气重整器20的操作条件，任意时间计算合成气重整器20所需的卡路里，组成天然气111，合成气重整器20的入口温度和合成气重整器20的出口压力; 并且根据所计算的卡路里所需的燃料气体量122来调节燃料气体的压力。版权所有（C）2010，JPO＆INPIT

6. 发明专利

JP2006022283A Slurry bed reaction system for bubbling tower type fisher-tropsh synthesis 有权
标题翻译：用于泡澡塔式渔船 - 混合物合成的浆液反应系统
公开(公告)号：JP2006022283A
公开(公告)日：2006-01-26
申请号：JP2004203864
申请日：2004-07-09
申请人： Cosmo Oil Co Ltd , Inpex Corp , Japan Oil Gas & Metals National Corp , Japan Petroleum Exploration Co Ltd , Nippon Steel Corp , コスモ石油株式会社 , 国際石油開発株式会社 , 新日本製鐵株式会社 , 独立行政法人石油天然ガス・金属鉱物資源機構 , 石油資源開発株式会社
发明人： FUJIMOTO KENICHIRO , ONISHI YASUHIRO , IHARA MASARU , SUEHIRO YOSHIFUMI , MORITA YASUMASA , INABA KIYOSHI , SHIMIZU TOSHIO , IWAMOTO OSAMU
IPC分类号： C10G2/00 , B01J8/22
摘要： PROBLEM TO BE SOLVED: To provide a slurry bed reaction system for bubbling-tower-type Fisher-Tropsh (FT) synthesis, which has a simple operation system for separating and guiding a catalyst and a liquid hydrocarbon product from the slurry in a gas-liquid-solid three phase and can suppress deterioration due to powdering of a catalyst particle, and the like. SOLUTION: The FT synthesis reaction system comprises a slurry bed reaction process for bubbling-tower-type FT synthesis, wherein a synthesis gas that is continuously supplied from the bottom part of a reactor 11 is caused to come into contact with a suspended catalyst particle to generate a liquid hydrocarbon, a gaseous hydrocarbon, and water, a process for separating the catalyst particle from the generated liquid product using a separation container 12, a process for transferring the generated gaseous product to the separation container and guiding the product to go out from the top, a process for guiding the generated liquid product to go out from the middle part of the separation container, and a process for guiding a slurry resulting from condensation of the catalyst particle from the bottom part of the separation container so as to cause the slurry to circulate toward the bottom part of the reactor. These processes are run by a driving force of the synthesis gas that is introduced from the reactor bottom part and ascends within the reactor containing the slurry bed. COPYRIGHT: (C)2006,JPO&NCIPI
摘要翻译：要解决的问题：提供一种用于起泡塔型Fisher-Tropsh（FT）合成的浆料床反应系统，其具有用于从浆料中分离和引导催化剂和液体烃产物的简单操作系统气 - 液 - 固三相，并且可以抑制由于催化剂颗粒的粉化引起的劣化等。解决方案：FT合成反应系统包括用于鼓泡塔型FT合成的浆料床反应方法，其中使从反应器11的底部连续供应的合成气与悬浮的催化剂颗粒以产生液体烃，气态烃和水，使用分离容器12将催化剂颗粒与生成的液体产物分离的方法，将产生的气态产物转移到分离容器并将产物引导至从顶部排出，用于引导生成的液体产物从分离容器的中部排出的过程，以及用于引导来自分离容器的底部的催化剂颗粒的缩合产生的浆料的方法，以便以使浆料朝向反应器的底部循环。这些过程由从反应器底部引入的合成气的驱动力运行，并在含有浆料床的反应器内上升。版权所有（C）2006，JPO＆NCIPI

7. 发明专利

JP2010202678A Cleaning method for ft synthetic hydrocarbon and ft synthetic hydrocarbon distillation separator 有权
标题翻译： FT合成碳氢化合物和FT合成烃分离器清洗方法
公开(公告)号：JP2010202678A
公开(公告)日：2010-09-16
申请号：JP2009046152
申请日：2009-02-27
申请人： Cosmo Oil Co Ltd , Inpex Corp , Japan Oil Gas & Metals National Corp , Japan Petroleum Exploration Co Ltd , Jx Nippon Oil & Energy Corp , Jx日鉱日石エネルギー株式会社 , Nippon Steel Engineering Co Ltd , コスモ石油株式会社 , 国際石油開発帝石株式会社 , 新日鉄エンジニアリング株式会社 , 独立行政法人石油天然ガス・金属鉱物資源機構 , 石油資源開発株式会社
发明人： TANAKA YUICHI , MORITA YASUMASA , KAERUISHI KENICHI
IPC分类号： C10G7/00
CPC分类号： C10G7/00 , C10G2/32 , C10G53/16 , C10G2300/1022 , C10G2400/02 , C10G2400/06 , C10G2400/08
摘要： PROBLEM TO BE SOLVED: To provide a cleaning method for FT synthetic hydrocarbon capable of efficiently recovering a hydrocarbon corresponding to naphtha from the FT synthetic hydrocarbon and reducing energy cost when a naphtha part, an intermediate distillation part and a wax part are separated, and an FT synthetic hydrocarbon distillation separator.
SOLUTION: In the cleaning method for the FT synthetic hydrocarbon, the FT synthetic hydrocarbon produced by Fischer-Tropsch synthetic reaction is fractionated according to a boiling point and hydrogenation and cleaning treatment are performed to manufacture a liquid fuel product. The cleaning method is provided with a heavy FT synthetic hydrocarbon fractionation step S3 for fractionating the heavy FT synthetic hydrocarbon produced from an FT synthetic reactor as a first intermediate distillation fraction and a wax distillation fraction, and a soft FT synthetic hydrocarbon fractionation step S5 for fractionating the soft FT synthetic hydrocarbon produced from the FT synthetic reactor as a light gas fraction and a second intermediate distillation fraction separately from the heavy FT synthetic hydrocarbon fractionation step S3.
COPYRIGHT: (C)2010,JPO&INPIT
摘要翻译：要解决的问题：提供一种能够有效地从FT合成烃中回收对应于石脑油的烃的FT合成烃的清洗方法，并且当石脑油部分，中间蒸馏部分和蜡部分分离时能降低能量成本，和FT合成烃蒸馏分离器。解决方案：在FT合成烃的清洗方法中，通过费 - 托合成反应生产的FT合成烃根据沸点分馏，进行氢化和清洗处理以制造液体燃料产物。清洗方法具有重FT合成烃分馏步骤S3，用于分馏由FT合成反应器生产的重FT合成烃作为第一中间蒸馏馏分和蜡蒸馏馏分，以及用于分馏的软FT合成烃分馏步骤S5 由FT合成反应器生产的轻质FT合成烃作为轻质气体馏分和与重FT合成烃分馏步骤S3分开的第二中间蒸馏馏分。版权所有（C）2010，JPO＆INPIT

8. 发明专利

JP2004313868A Catalyst for manufacturing olefin oligomer and method for manufacturing olefin oligomer 有权
公开(公告)号：JP2004313868A
公开(公告)日：2004-11-11
申请号：JP2003108799
申请日：2003-04-14
申请人： Japan Petroleum Exploration Co Ltd , Takeshige Takahashi , 石油資源開発株式会社 , 武重高橋
发明人： TAKAHASHI TAKESHIGE , YONETANI SEIJURO , MORITA YASUMASA , OKADO HIDEO
IPC分类号： B01J31/02 , C07B61/00 , C07C2/26 , C07C11/02
CPC分类号： Y02P20/52
摘要： PROBLEM TO BE SOLVED: To produce a catalyst for manufacturing an olefin oligomer which can be easily separated from the olefin oligomer, has no corrosiveness to apparatus, does not form a heavy-duty tar-like material, is easy in the control of reaction, and is composed of continuous components to prevent the carbon number of the obtained olefin oligomer from deviating to the multiple of the carbon number of a raw material olefin, and to provide a method for manufacturing the olefin oligomer using the same. SOLUTION: The olefin oligomer is obtained by bringing the raw material olefin into contact with the catalyst for manufacturing the olefin oligomer and containing a compound expressed by the formula (I): RSO 3 H (I) (where R represents an alkyl group), more preferably methanesulfonic acid. COPYRIGHT: (C)2005,JPO&NCIPI

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