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1.发明申请公开(公告)号：US20170120225A1
公开(公告)日：2017-05-04
申请号：US15335163
申请日：2016-10-26
Applicant: KOREA INSTITUTE OF SCIENCE AND TECHNOLOGY
Inventor： Dong Ju MOON , Eun Hyeok YANG , Gi Hoon HONG , Sung Soo LIM , Jae Sun JUNG , Young Su Noh , Na Young KIM , Jae Suk LEE , Ji In PARK , Sang Yong LEE
IPC: B01J23/755 , B01J35/10 , C01B3/40 , B01J23/10
CPC classification number: B01J23/755 , B01J23/10 , B01J23/83 , B01J35/002 , B01J35/1009 , B01J37/031 , B01J37/084 , B01J37/086 , B01J37/088 , B01J37/16 , C01B3/40 , C01B2203/0233 , C01B2203/0238 , C01B2203/1058 , C01B2203/1082 , C01B2203/1241
Abstract: A nickel-supported catalyst for combined steam and carbon dioxide reforming, as a catalyst which is used in a process of preparing a synthesis gas by combined steam and carbon dioxide reforming with natural gas, is provided. More particularly, in the nickel-supported catalyst, nickel is supported as an active metal on a lanthanum oxide support.
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2.发明申请METHOD FOR PREPARING SYNTHETIC FUEL FROM NATURAL GAS OF STRANDED GAS FIELD AND ASSOCIATED GAS FROM OIL & GAS FIELDS BY GTL-FPSO PROCESS 有权从GTL-FPSO工艺的油气田相关气体自然气体制备合成燃料的方法公开(公告)号：US20160186071A1
公开(公告)日：2016-06-30
申请号：US14951857
申请日：2015-11-25
Applicant: KOREA INSTITUTE OF SCIENCE AND TECHNOLOGY
Inventor： Dong Ju MOON , Jae Sun JUNG , Eun Hyeok YANG , Jae Suk LEE , Young Su NOH , Gi Hoon HONG , Sang Yong LEE , Sung Soo LIM , Na Young KIM
CPC classification number: C10G2/332 , C01B3/382 , C01B2203/0233 , C01B2203/0238 , C01B2203/0244 , C01B2203/0283 , C01B2203/062 , C01B2203/1241 , C01B2203/1258 , C10G47/00
Abstract: The present invention relates to a method for preparing a synthetic fuel on a vessel above a stranded gas field or an oil & gas field by a GTL-FPSO process, more particularly to a method for preparing a synthetic fuel with superior economic feasibility, productivity and efficiency using a compact GTL (gas to liquid) apparatus that can be used for a stranded gas field or an oil & gas field and an FPSO (floating production, storage and offloading) process under a condition optimized for the ratio of carbon dioxide in the stranded gas field or the oil & gas field and an apparatus for the same.
Abstract translation: 本发明涉及一种通过GTL-FPSO方法在绞合气田或油气田上方的容器上制备合成燃料的方法，更具体地涉及一种制备具有优良经济可行性，生产率的合成燃料的方法和 使用可用于绞合气田或石油和天然气领域的紧凑型GTL（气体对液体）设备的效率以及在针对二氧化碳的比例优化的条件下的FPSO（浮式生产，储存和卸载） 绞合气田或油气田及其设备。
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Patent Agency Ranking
3.发明申请PROCESS FOR PREPARING COBALT BASED CATALYSTS FOR FISCHER-TROPSCH SYNTHESIS 有权制备基于钴的催化剂进行FISCHER-TROPSCH合成的方法公开(公告)号：US20140349845A1
公开(公告)日：2014-11-27
申请号：US13971204
申请日：2013-08-20
Applicant: KOREA INSTITUTE OF SCIENCE AND TECHNOLOGY
Inventor： Dong Ju MOON , Jae Sun JUNG , Jae Suk LEE , Eun Hyeok YANG , Hyun Jin KIM , Bang Hee KIM , Seung Hwan LEE , Yun Ju LEE , Ga Ram CHOI
IPC: B01J23/89
CPC classification number: B01J23/8913 , B01J21/04 , B01J35/002 , B01J35/1019 , B01J35/1038 , B01J35/1061 , B01J37/0205 , B01J37/0242 , B01J37/0244 , B01J37/08 , C10G2/00 , C10G2/332
Abstract: The present invention relates to a method for preparing a cobalt-based catalyst for Fischer-Tropsch synthesis, more particularly to a method for preparing a cobalt-based catalyst represented by Ir—Co/η-Al2O3 wherein cobalt and iridium are supported at high density by repeating impregnation and drying tens of times on a spherical η-alumina support having many acidic sites.The catalyst prepared according to the present invention can provide improved conversion rate of carbon monoxide and selectivity for liquid hydrocarbons when used for Fischer-Tropsch synthesis.
Abstract translation: 本发明涉及一种用于费 - 托合成的钴基催化剂的制备方法，更具体地涉及一种由Ir-Co / e-Ag-Al2O3表示的钴基催化剂的制备方法，其中钴和铱负载在高 通过在具有许多酸性位点的球形和氧化铝载体上重复浸渍和干燥数十次来实现密度。 根据本发明制备的催化剂可以提供改善的一氧化碳转化率和用于费 - 托合成时液体烃的选择性。
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4.发明申请公开(公告)号：US20140349836A1
公开(公告)日：2014-11-27
申请号：US14265989
申请日：2014-04-30
Applicant: KOREA INSTITUTE OF SCIENCE AND TECHNOLOGY
Inventor： Dong Ju MOON , Jae Sun JUNG , Eun Hyeok YANG , Sang Woo KIM , Jae Suk LEE , Bang Hee KIM , Jong Tae JUNG , Hyun Jin KIM , Ga Ram CHOI , Byoung Sung AHN
IPC: B01J23/755
CPC classification number: B01J23/755 , B01J21/04 , B01J23/83 , B01J35/002 , B01J35/08 , B01J35/1019 , B01J35/1038 , B01J35/1061 , B01J37/0207 , B01J37/08 , C01B3/04 , C01B3/40 , C01B2203/0233 , C01B2203/0238 , C01B2203/1058 , C01B2203/1082 , Y02P20/52
Abstract: The present invention relates to a method for preparing a nickel-based catalyst for steam carbon dioxide reforming (SCR) of natural gas using steam and carbon dioxide, more particularly to a method for preparing a nickel-based catalyst represented by Ni/η-Al2O3, which is prepared by supporting nickel on a spherical η-alumina support having many acid sites at high density by repeating impregnation and drying tens of times.The catalyst prepared according to the present invention exhibits superior catalytic activity when used in steam carbon dioxide reforming reaction (SCR) even under harsh conditions of high temperature and high pressure and hardly exhibits carbon deposition due to superior durability.
Abstract translation: 本发明涉及一种使用蒸汽和二氧化碳制备天然气蒸汽二氧化碳重整（SCR）的镍基催化剂的方法，更具体地涉及一种由Ni / eegr- Al2O3，其通过重复浸渍和干燥几次而以高密度将镍支撑在具有多个酸性位点的球形和氧化铝载体上来制备。 根据本发明制备的催化剂即使在高温高压的苛刻条件下也用于蒸汽二氧化碳重整反应（SCR）中也显示出优异的催化活性，并且由于耐久性优异，几乎不显示碳沉积。
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5.发明申请CORE-SHELL COBALT CATALYSTS FOR FISCHER-TROPSCH SYNTHESIS REACTION AND PREPARING METHOD THEREOF 审中-公开用于FISCHER-TROPSCH合成反应的核壳钴催化剂及其制备方法公开(公告)号：US20170028388A1
公开(公告)日：2017-02-02
申请号：US14983849
申请日：2015-12-30
Applicant: KOREA INSTITUTE OF SCIENCE AND TECHNOLOGY
Inventor： Dong Ju MOON , Jae Sun JUNG , Jae Suk LEE , Gi Hoon HONG , Eun Hyeok YANG , Sung Soo LIM , Young Su NOH , Kwang Hyeok LEE , Sang Yong LEE , Na Young KIM
CPC classification number: B01J29/46 , B01J23/75 , B01J29/072 , B01J35/0086 , B01J35/1057 , B01J35/1061 , B01J35/109
Abstract: The present invention relates to a core-shell cobalt catalyst used for a Fischer-Tropsch synthesis reaction and a method for preparing the same. More particularly, it relates to a cobalt catalyst, which has a core-shell structure including a cobalt-supported and sintered alumina particle as a core and a zeolite powder coated on the surface of the alumina particle to a thickness of 50 μm or greater through mechanical alloying as a shell and is used to prepare hydrocarbons with high octane numbers through a Fischer-Tropsch synthesis reaction, and a method for preparing the same.
Abstract translation: 本发明涉及用于费 - 托合成反应的核 - 壳钴催化剂及其制备方法。 更具体地说，本发明涉及一种钴催化剂，其具有核 - 壳结构，其包括以钴负载和烧结的氧化铝颗粒为核心，以及通过在氧化铝颗粒的表面上涂覆厚度为50μm以上的沸石粉末 机械合金化作为壳，并用于通过费 - 托合成反应制备具有高辛烷值的烃及其制备方法。
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公开(公告)号：US20170274340A1
公开(公告)日：2017-09-28
申请号：US15203604
申请日：2016-07-06
Applicant: KOREA INSTITUTE OF SCIENCE AND TECHNOLOGY
Inventor： Dong Ju MOON , Gi Hoon HONG , Jae Suk LEE , Jae Sun JUNG , Eun Hyeok YANG , Sung Soo LIM , Young Su NOH , Ji In PARK
CPC classification number: B01J8/067 , B01J8/065 , B01J8/22 , B01J2208/00221 , B01J2208/025 , B01J2208/065 , F28D7/0083 , F28D7/026 , F28D7/103 , F28D2021/0022 , F28F13/06 , F28F2009/226 , F28F2230/00
Abstract: The present disclosure relates to a shell-and-multi-double concentric-tube reactor and a shell-and-multi-double concentric-tube heat exchanger, and to a shell- and-multi-double concentric-tube reactor and a shell-and-multi-double concentric-tube heat exchanger which provide a new type of reactor and a heat exchanger, thereby maximizing catalyst performance and improving performance of the reactor by optimizing heat exchange efficiency and a heat flow, uniformly distributing a reactant, and increasing a flow rate of the reactant, and accordingly making the reactor and the heat exchanger compact.
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公开(公告)号：US20170274339A1
公开(公告)日：2017-09-28
申请号：US15203420
申请日：2016-07-06
Applicant: KOREA INSTITUTE OF SCIENCE AND TECHNOLOGY
Inventor： Dong Ju MOON , Gi Hoon HONG , Jae Suk LEE , Jae Sun JUNG , Eun Hyeok YANG , Sung Soo LIM , Young Su NOH , Ji In PARK
CPC classification number: B01J8/067 , B01J8/065 , B01J8/22 , B01J2208/00132 , B01J2208/00221 , F28D7/103
Abstract: The present disclosure relates to a shell-and-multi-triple concentric-tube reactor and a shell-and-multi-triple concentric-tube heat exchanger, and to a shell-and-multi-triple concentric-tube reactor and a shell-and-multi-triple concentric-tube heat exchanger which provide a new type of reactor and heat exchanger, thereby maximizing catalyst performance and improving performance of the reactor by optimizing heat exchange efficiency and a heat flow, uniformly distributing a reactant, and increasing a flow rate of the reactant, and accordingly making the reactor and the heat exchanger compact.
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