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1.发明申请公开(公告)号：US20210354113A1
公开(公告)日：2021-11-18
申请号：US17281114
申请日：2019-05-14
Inventor： Yong Ki PARK , Won Choon CHOI , Daesung PARK , Hawon PARK , Changyeol SONG , Deuk Soo PARK , Ung Gi HONG , Miyoung LEE
Abstract: Disclosed is a catalyst for producing an olefin including an oxygen carrier material and a dehydrogenation catalyst. The catalyst allows hydrogen to be converted into water by using oxygen inside the lattice of an oxide catalyst without the additional supply of oxygen, and thus, the conversion can be increased while the decrease in selectivity, which is a disadvantage of an additional oxidative dehydrogenation reaction (ODHP), is suppressed.
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2.发明申请公开(公告)号：US20220401930A1
公开(公告)日：2022-12-22
申请号：US17776432
申请日：2020-11-24
Inventor： Deuk Soo PARK , Ung Gi HONG , Hae Bin SHIN , Daesung PARK , Hawon PARK , Changyeol SONG , Won Choon CHOI , Yong Ki PARK
Abstract: A dehydrogenation catalyst for producing olefins from alkane gases, in which cobalt and zinc are supported on alumina. A method for preparing the dehydrogenation catalyst for producing olefins from alkane gases, includes: preparing a mixed solution by mixing cobalt and zinc precursors with water; preparing a supported catalyst by impregnating alumina with the mixed solution; drying the supported catalyst; and calcining the dried supported catalyst at 500° C. to 900° C.
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公开(公告)号：US20210354112A1
公开(公告)日：2021-11-18
申请号：US17281132
申请日：2019-12-04
Applicant: SK GAS CO., LTD. , KOREA RESEARCH INSTITUTE OF CHEMICAL TECHNOLOGY , KOREA NATIONAL UNIVERSITY OF TRANSPORTATION INDUSTRY-ACADEMIC COOPERATION FOUNDATION
Inventor： Yong Ki PARK , Won Choon CHOI , Daesung PARK , Hawon PARK , Changyeol SONG , Deuk Soo PARK , Ung Gi HONG , Miyoung LEE , Sungwon KIM , Chaeeun YEO
IPC: B01J21/06 , B01J8/38 , C07C5/333 , B01J21/04 , B01J35/02 , B01J23/26 , B01J23/30 , B01J35/10 , B01J37/08
Abstract: Disclosed is a method of producing an olefin using a circulating fluidized bed process, including: (a) supplying a hydrocarbon mixture including propane and a dehydrogenation catalyst to a riser which is in a state of a fast fluidization regime, and thus inducing a dehydrogenation reaction; (b) separating an effluent from the dehydrogenation reaction into the catalyst and a propylene mixture; (c) stripping, in which a residual hydrocarbon compound is removed from the catalyst separated in step (b); (d) mixing the catalyst stripped in step (c) with a gas containing oxygen and thus continuously regenerating the catalyst; (e) circulating the catalyst regenerated in step (d) to step (a) and thus resupplying the catalyst to the riser; and (f) cooling, compressing, and separating the propylene mixture, which is a reaction product separated in step (b), and thus producing a propylene product.
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公开(公告)号：US20160016108A1
公开(公告)日：2016-01-21
申请号：US14773968
申请日：2014-03-12
Inventor： Yong Ki PARK , Won Choon CHOI , Na Young KANG , Hwi Min SEO
IPC: B01D53/04
CPC classification number: B01D53/0462 , B01D53/08 , B01D53/12 , B01D53/62 , B01D2251/30 , B01D2251/40 , B01D2253/102 , B01D2253/106 , B01D2253/108 , B01D2253/204 , B01D2257/504 , B01D2258/025 , B01D2258/0283 , B01D2259/40098 , Y02A50/2342 , Y02C10/04 , Y02C10/06 , Y02C10/08
Abstract: The present invention relates to a carbon dioxide capture apparatus having a temperature swing adsorption mode for selective separation of carbon dioxide from flue gases. The carbon dioxide capture apparatus comprises: a carbon dioxide sorption column including a carbon dioxide adsorption unit in which adsorption of carbon dioxide from flue gases occurs; a carbon dioxide desorption column connected to the carbon dioxide sorption column and including a carbon dioxide desorption unit in which desorption of the adsorbed carbon dioxide occurs; a carbon dioxide absorbent repeatedly adsorbing and desorbing carbon dioxide while circulating through the carbon dioxide sorption column and the carbon dioxide desorption column; and a heat exchange unit in which heat exchange occurs between the absorbent after carbon dioxide adsorption and the absorbent after carbon dioxide desorption.
Abstract translation: 本发明涉及具有用于从烟道气中选择性分离二氧化碳的变温吸附模式的二氧化碳捕集装置。 二氧化碳捕获装置包括：二氧化碳吸附塔，其包括二氧化碳吸附单元，其中发生来自烟道气的二氧化碳的吸附; 连接到二氧化碳吸附塔的二氧化碳解吸塔，并且包括二氧化碳解吸单元，其中发生吸附的二氧化碳的解吸; 二氧化碳吸收剂在循环通过二氧化碳吸附塔和二氧化碳解吸塔时反复吸附和解吸二氧化碳; 以及在二氧化碳吸附后的吸收剂与二氧化碳解吸后的吸收剂之间发生热交换的热交换单元。
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5.发明申请公开(公告)号：US20200055028A1
公开(公告)日：2020-02-20
申请号：US16349843
申请日：2017-12-28
Inventor： Won Choon CHOI , Yong Ki PARK , Su Jin GONG , Seo Hyun SHIM , Deuk Soo PARK , Ung Gi HONG
IPC: B01J23/652 , B01J23/06 , B01J21/06 , B01J37/02 , B01J38/04 , B01J38/02 , C07C5/32 , C07C9/08 , C07C11/06
Abstract: Disclosed is a catalyst for producing the olefin. The catalyst includes a support including alumina and a sub-support component, and a metal oxide impregnated on the support. The metal oxide includes anyone selected from an oxide of chromium, vanadium, manganese, iron, cobalt, molybdenum, copper, zinc, cerium and nickel; and the sub-support component includes anyone selected from zirconium, zinc and platinum.
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Patent Agency Ranking
公开(公告)号：US20190388884A1
公开(公告)日：2019-12-26
申请号：US16468204
申请日：2018-05-01
Inventor： Deuk Soo PARK , Ung Gi HONG , Hyeongchan AHN , Won Choon CHOI , Yong Ki PARK
Abstract: Disclosed is an olefin production method including: pretreating a catalyst by providing reduction gas to an alumina type catalyst to produce olefin from the hydrocarbon including not less than 90 wt % of LPG (Stage 1); producing the olefin by providing the catalyst pretreated at Stage 1 into Riser of Fast Fluidization Regime to dehydrogenate the hydrocarbon (Stage 2); separating the mixture of the produced propylene and the catalyst used at Stage 2, and regenerating the separated catalyst (Stage 3); and recycling the catalyst regenerated at Stage 3 to the process of Stage 1 (Stage 4).
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公开(公告)号：US20190330125A1
公开(公告)日：2019-10-31
申请号：US16471383
申请日：2018-05-01
Inventor： Deuk Soo PARK , Ung Gi HONG , Hyeongchan AHN , Won Choon CHOI , Yong Ki PARK
Abstract: Disclosed is an olefin production method which includes: (a) providing the regenerated catalyst and the hydrocarbon including not less than 90 wt % of LPG into Riser of Fast Fluidization Regime, and dehydrogenating in the presence of an alumina type catalyst; (b) separating an effluent from the dehydrogenation reaction into the catalyst and propylene mixture; (c) stripping to remove the hydrocarbon compound included in the catalyst separated at stage (b); (d) mixing the catalyst stripped at stage (c) with the gas including oxygen, and continuously regenerating it; (e) recycling the catalyst regenerated at stage (d) to stage (a), and providing it again into Riser; and (f) producing propylene product by cooling, compressing and separating propylene mixture of the reaction product separated at stage (b).
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8.发明公开公开(公告)号：US20240300871A1
公开(公告)日：2024-09-12
申请号：US18269165
申请日：2021-11-16
Inventor： Daesung PARK , Hawon PARK , Changyeol SONG , Eun Sang KIM , Yong Ki PARK , Won Choon CHOI , Ung Gi HONG , Miyoung LEE , Hae Bin SHIN , Sanghyeon PARK , Deuk Soo PARK
CPC classification number: C07C5/325 , C07C7/005 , C07C2521/02 , C07C2521/04 , C07C2523/42 , C07C2523/89
Abstract: A method for producing olefins using a circulating fluidized bed process, includes: supplying a propane-containing hydrocarbon mixture and a dehydrogenation catalyst into a riser, which is a fast fluidization regime, to cause a dehydrogenation reaction; separating, from a propylene mixture, the catalyst which is a product of the dehydrogenation reaction; removing unseparated hydrocarbon compounds remaining in the catalyst separated in the separating; continuously regenerating the catalyst by mixing the catalyst stripped in the removing with a gas containing oxygen; circulating the catalyst regenerated in the continuously regenerating to the supplying and resupplying it into the riser; and preparing propylene by cooling, compressing, and separating the propylene mixture which is a reaction product separated in the separating.
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9.发明申请公开(公告)号：US20230127784A1
公开(公告)日：2023-04-27
申请号：US17909241
申请日：2020-12-24
Inventor： Daesung PARK , Hawon PARK , Changyeol SONG , Yong Ki PARK , Won Choon CHOI , Ung Gi HONG , Hae Bin SHIN , Miyoung LEE , Deuk Soo PARK
Abstract: The present disclosure is to provide a catalyst for olefin production which is eco-friendly and has excellent conversion rates and selectivity and a preparation method thereof, and the catalyst for olefin production according to the present disclosure is one in which cobalt and zinc are supported with alumina. Particularly, the catalyst according to the present disclosure uses an amount of platinum that is about 400 times smaller than that of the conventional catalysts, and has high conversion rates and selectivity under conditions in which continuous reaction-regeneration process is possible without an additional hydrogen reduction process.
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10.发明申请METHOD FOR PRODUCING HIGH SILICA ZEOLITE USING RECOVERED SILICA FILTRATE, AND HIGH SILICA ZEOLITE PRODUCED ACCORDING TO SAID METHOD 有权使用回收的二氧化硅过滤器生产高硅沸石的方法以及按照方法生产的高硅沸石公开(公告)号：US20150139898A1
公开(公告)日：2015-05-21
申请号：US14603759
申请日：2015-01-23
Inventor： Na Young KANG , Yong ki PARK , Won Choon CHOI , Hwi Min SEO , Chul Wee LEE
IPC: C01B39/38
CPC classification number: C01B39/38 , C01B39/02 , C01B39/26 , C01P2002/72 , C01P2004/03
Abstract: Provided are a method of manufacturing a high silica zeolite using a recovered silica filtrate, and a high silica zeolite manufactured according to the method. To this end, the present invention provides the method of manufacturing the high silica zeolite using the recovered silica filtrate, including manufacturing a solated agglomerated silica from the silica filtrate including a metal salt (step 1); filtering and washing the solated agglomerated silica of step 1 to manufacture a silica cake from which the metal salt is removed (step 2); peptizing the silica cake to manufacture a silica sol (step 3); and manufacturing the high silica zeolite using the silica sol manufactured in step 3 as a silica source (step 4). Further, the present invention provides a high silica zeolite manufactured from a recovered silica filtrate through the manufacturing method and having a Si/Al mole ratio of 5 or more. According to the present invention, it is possible to provide a process of manufacturing a high silica zeolite, in which economic feasibility, a manufacturing cost, and a manufacturing time of process steps are reduced, by reusing a recovered silica filtrate to manufacture the zeolite.
Abstract translation: 提供了使用回收的二氧化硅滤液和根据该方法制造的高二氧化硅沸石制造高二氧化硅沸石的方法。 为此，本发明提供使用回收的二氧化硅滤液制造高二氧化硅沸石的方法，包括从包含金属盐的二氧化硅滤液制备溶胶凝聚二氧化硅（步骤1）; 过滤并洗涤步骤1的固化的附聚二氧化硅，以制造除去金属盐的二氧化硅饼（步骤2）; 将硅胶胶化以制造硅溶胶（步骤3）; 并使用步骤3中制造的硅溶胶作为二氧化硅源制造高硅石沸石（步骤4）。 此外，本发明提供了通过制造方法由回收的二氧化硅滤液制备的高硅石沸石，Si / Al摩尔比为5以上。 根据本发明，通过重新利用回收的二氧化硅滤液来制造沸石，可以提供制造经济可行性，制造成本和加工步骤的制造时间的高二氧化硅沸石的制造方法。
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