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

IPC: B01J29/46 ,  B01J35/00 ,  B01J35/02 ,  B01J35/10 ,  B01J29/40 ,  B01J23/75

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。

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

IPC: C10G2/00 ,  C10L1/04 ,  C01B3/34 ,  C10G47/00

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。

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

IPC: B01J8/06 ,  F28F13/06 ,  F28D7/02

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.

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

IPC: B01J8/06 ,  B01J8/08

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.