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1. 发明公开

KR1020090061050A 유동층 반응기에서 방향족 아민을 제조하는 방법 无效
标题翻译：在流化床反应器中制备芳族氨基酸的方法
公开(公告)号：KR1020090061050A
公开(公告)日：2009-06-15
申请号：KR1020097007800
申请日：2007-09-14
申请人： 바스프 에스이
发明人： 자이데만로타 , 쾨닉스만루치아 , 슈나이더크리스티안 , 슈밥에케하르트 , 슈튀처디터 , 리켄스셀린느
IPC分类号： C07C209/36 , C07C211/46 , B01J23/70 , B01J8/18
CPC分类号： C07C209/36 , B01J8/006 , B01J8/1836 , B01J8/1845 , B01J8/1872 , B01J8/34 , B01J19/32 , B01J2208/00132 , B01J2219/3221 , B01J2219/32213 , B01J2219/3222 , B01J2219/32227 , B01J2219/32408 , B01J2219/32416 , B01J2219/32466 , B01J2219/32475 , C10G45/20 , C07C211/46
摘要： Disclosed is a method for producing aromatic amines by catalytically hydrogenating the corresponding nitro compound in a fluidized bed reactor. In said method, a gaseous reaction mixture containing the nitro compound and hydrogen flows from the bottom to the top of a heterogeneous particulate catalyst that forms a fluidized bed. Said method is characterized in that baffles are provided in the fluidized bed, said baffles dividing the fluidized bed into a plurality of cells horizontally disposed in the fluidized bed reactor and a plurality of cells vertically disposed in the fluidized bed reactor. Furthermore, the cell walls are gas-permeable and are provided with openings which ensure that the heterogeneous particulate catalyst reaches a transfer rate ranging from 1 to 100 liters/hour per liter of reactor volume in the vertical direction.
摘要翻译：公开了通过在流化床反应器中催化氢化相应的硝基化合物来制备芳族胺的方法。在所述方法中，含有硝基化合物和氢气的气态反应混合物从形成流化床的非均相颗粒催化剂的底部向顶部流动。所述方法的特征在于，在流化床中设置挡板，所述挡板将流化床分成水平设置在流化床反应器中的多个单元和垂直设置在流化床反应器中的多个单元。此外，细胞壁是透气性的并且设置有开口，其确保异相颗粒催化剂在垂直方向上达到每升反应器体积1至100升/小时的转移速率。

2. 发明授权

KR101344182B1 통합된 기체/고체 분리 시스템을 갖는 2개의 유동 반응구역을 구비한 신규한 반응기 有权
标题翻译：具有集成气/固体分离系统的两个流化反应区的新型反应器
公开(公告)号：KR101344182B1
公开(公告)日：2013-12-20
申请号：KR1020060131025
申请日：2006-12-20
申请人： 아이에프피 에너지스 누벨
发明人： 로스죠제프 , 고띠에띠에리 , 앙드류레지
IPC分类号： C10G45/20
CPC分类号： B01J8/1845 , B01J8/003 , B01J8/0055 , B01J8/0065 , B01J8/1809 , B01J8/1818 , B01J8/1827 , B01J8/1836 , B01J8/1854 , B01J8/1863 , B01J8/28 , B01J8/34 , B01J8/386 , B01J8/388 , B01J2208/00141 , B01J2208/00362 , B01J2208/00371 , B01J2208/00557 , B01J2208/00584 , B01J2208/0084 , B01J2208/00849 , B01J2219/00166 , B01J2219/00247 , C10G1/08 , C10G3/49 , C10G3/57 , C10G3/62 , C10G11/18 , C10G2300/1011 , C10G2300/1037 , C10G2300/708 , C10G2400/20 , Y02P30/40 , Y02P30/42 , Y02P30/446
摘要： 본발명은체류시간을정확하게조절하기위하여통합된기체-고체분리시스템을갖는 2개의유동화반응구역을구비한기체-고체반응기에관한것이다.

3. 发明公开

KR1020090131507A 탄소나노튜브 합성 장치 有权
标题翻译：用于合成碳纳米管的装置
公开(公告)号：KR1020090131507A
公开(公告)日：2009-12-29
申请号：KR1020080057417
申请日：2008-06-18
申请人： 세메스 주식회사
发明人： 장석원
IPC分类号： B82B3/00 , B82Y40/00
CPC分类号： C01B32/16 , B01J8/1818 , B01J8/1845 , B01J8/382 , B82Y30/00 , B82Y40/00 , C01B32/162
摘要： PURPOSE: An apparatus for manufacturing a carbon nanotube is provided to maintain the fluidity of a catalyst to be constant irrespective of the density of a catalyst and the manufacturing method of a catalyst. CONSTITUTION: An apparatus(100) for manufacturing a carbon nanotube comprises a rector(110) which is formed long perpendicularly; a heating part(120) which heats the inside of the reactor to the temperature necessary for the synthesis of a carbon nanotube; a gas supply nozzle(130) which is installed long from the upper end of the reactor toward the lower end containing a catalyst so as to spray a reaction gas toward the catalyst; a carbon nanotube recovery unit(150); and an ventilation part which ventilates the unreacted reaction gas to the outside of the reactor.
摘要翻译：目的：提供用于制造碳纳米管的装置，以保持催化剂的流动性恒定，而与催化剂的密度和催化剂的制造方法无关。构成：用于制造碳纳米管的装置（100）包括垂直形成的反射器（110）; 将反应器内部加热到合成碳纳米管所需的温度的加热部件（120）; 气体供给喷嘴（130），其从所述反应器的上端朝向下端设置有包含催化剂的喷出反应气体朝向所述催化剂的长度; 碳纳米管回收单元（150）; 以及将未反应的反应气体通向反应器外部的通风部。

4. 发明授权

KR101572399B1 유동 교란기를 구비한 라이저 반응기 有权
标题翻译：具有流量破坏器的上升反应器
公开(公告)号：KR101572399B1
公开(公告)日：2015-11-26
申请号：KR1020147009669
申请日：2012-09-07
申请人： 유오피 엘엘씨
发明人： 샌닥츠,마이클에스.
IPC分类号： B01J8/24 , B01J19/00 , C10G11/18 , C04B35/66
CPC分类号： B01J8/1845 , B01J8/1872 , B01J8/34 , B01J19/02 , B01J2208/00938 , B01J2219/024 , C10G11/18 , F27D1/10 , F27D1/14 , F27D1/141 , F27D1/1626 , F27D2001/1631
摘要： 본발명의실시양태는공급원료및 촉매를반응시키기위한라이저반응기를포함한다. 그라이저반응기벽은내부를한정한다. 연속적내화성라이닝이반응기벽에부착되고그 벽으로부터반응기내부내로내향연장하고공급원료및 촉매의유동패턴을교란하는복수의유동교란기를한정한다.
摘要翻译：本发明的一个实施方案包括用于使原料和催化剂反应的提升管反应器。立管反应器壁限定内部。连续的耐火衬里连接到反应器壁上，并且限定了从壁向内延伸进入反应器内部并破坏原料和催化剂的流动模式的多个流动破碎器。

5. 发明公开

KR1020140069138A 유동 교란기를 구비한 라이저 반응기 有权
标题翻译：具有流量破坏器的上升反应器
公开(公告)号：KR1020140069138A
公开(公告)日：2014-06-09
申请号：KR1020147009669
申请日：2012-09-07
申请人： 유오피 엘엘씨
发明人： 샌닥츠,마이클에스.
IPC分类号： B01J8/24 , B01J19/00 , C10G11/18 , C04B35/66
CPC分类号： B01J8/1845 , B01J8/1872 , B01J8/34 , B01J19/02 , B01J2208/00938 , B01J2219/024 , C10G11/18 , F27D1/10 , F27D1/14 , F27D1/141 , F27D1/1626 , F27D2001/1631
摘要： 본 발명의 실시양태는 공급원료 및 촉매를 반응시키기 위한 라이저 반응기를 포함한다. 그 라이저 반응기 벽은 내부를 한정한다. 연속적 내화성 라이닝이 반응기 벽에 부착되고 그 벽으로부터 반응기 내부 내로 내향 연장하고 공급원료 및 촉매의 유동 패턴을 교란하는 복수의 유동 교란기를 한정한다.
摘要翻译：本发明的一个实施方案包括用于使原料和催化剂反应的提升管反应器。立管反应器壁限定内部。连续的耐火衬里连接到反应器壁上，并且限定了从壁向内延伸进入反应器内部并破坏原料和催化剂的流动模式的多个流动破碎器。

6. 发明公开

KR1020170104418A 고체 입자 체류시간 증가를 위한 유동 제어를 통한 순환 유동층 반응기 및 반응 방법 审中-实审
标题翻译：循环流化床反应器和流量控制反应法增加固体颗粒保留时间
公开(公告)号：KR1020170104418A
公开(公告)日：2017-09-15
申请号：KR1020170112070
申请日：2017-09-01
申请人： 연세대학교 산학협력단 , 한국화학연구원
发明人： 조형희 , 유환주 , 문호규 , 서휘민 , 박용기 , 최원춘 , 강나영 , 박선영
IPC分类号： B01J8/18 , B01J19/30
CPC分类号： B01J8/1881 , B01J8/1827 , B01J8/1845 , B01J19/30
摘要： 본발명의일 실시예에따른순환유동층반응기는반응기체가상승되며, 상기반응기체와고체입자의반응이일어나는주반응부, 상기주반응부와연결되어형성되며, 상기반응기체와상기고체입자의분리가일어나는분리부및 상기고체입자가하강되며, 다시주반응부로유입되도록하는하강부를포함하되, 상기주반응부는복수개의확장부를포함하며, 상기확장부내에서고체입자의순환이증가하여고체입자의체류시간이증가되는것을특징으로한다.
摘要翻译：根据本发明的实施方式的循环流化床反应器包括主反应部分和反应部分，其中反应气体升高并且反应气体和固体颗粒之间发生反应，反应部分与主反应部分连接形成，其中主反应部分包括多个膨胀部分，并且膨胀部分中固体颗粒的循环增加，使得固体颗粒的量停留时间增加。

7. 发明公开

KR1020090080043A 기상 반응을 수행하기 위한 유동층 반응기 无效
标题翻译：用于实施气相反应的流化床反应器
公开(公告)号：KR1020090080043A
公开(公告)日：2009-07-23
申请号：KR1020097007799
申请日：2007-09-14
申请人： 바스프 에스이
发明人： 자이데만로타 , 슈튀처디터 , 그라슬러토마스 , 카헤스마틴 , 슈나이더크리스티안
IPC分类号： B01J8/18 , B01J19/32
CPC分类号： B01J8/1845 , B01J8/006 , B01J8/1836 , B01J8/1872 , B01J8/34 , B01J19/32 , B01J2208/00132 , B01J2219/3221 , B01J2219/32213 , B01J2219/3222 , B01J2219/32227 , B01J2219/32237 , B01J2219/32262 , B01J2219/32408 , B01J2219/32416 , B01J2219/32425 , B01J2219/32441 , B01J2219/32466 , B01J2219/32475 , B01J2219/32483 , C10G2/344 , C10G45/20
摘要： Disclosed is a fluidized bed reactor for carrying out a gas phase reaction. A gaseous reaction mixture flows from the bottom to the top of a heterogeneous particulate catalyst that forms a fluidized bed in which baffles are arranged. Said fluidized bed reactor is characterized in that the baffles divide the fluidized bed into a plurality of cells horizontally disposed in the fluidized bed reactor and a plurality of cells vertically disposed in the fluidized bed reactor, the cell walls being gas-permeable and being provided with openings which ensure that the heterogeneous particulate catalyst reaches a transfer rate ranging from 1 to 100 liters/hour per liter of reactor volume in the vertical direction.
摘要翻译：公开了一种用于进行气相反应的流化床反应器。气态反应混合物从形成流化床的非均相颗粒催化剂的底部向顶部流动，其中布置有挡板。所述流化床反应器的特征在于，挡板将流化床分成水平设置在流化床反应器中的多个细胞和垂直设置在流化床反应器中的多个细胞，细胞壁是透气的并且具有确保异相颗粒催化剂在垂直方向上达到每升反应器体积1至100升/小时的转移速率的开口。

8. 发明公开

KR1020070065841A 통합된 기체/고체 분리 시스템을 갖는 2개의 유동 반응구역을 구비한 신규한 반응기 有权
标题翻译：具有集成气/固体分离系统的两个流化反应区的新型反应器
公开(公告)号：KR1020070065841A
公开(公告)日：2007-06-25
申请号：KR1020060131025
申请日：2006-12-20
申请人： 아이에프피 에너지스 누벨
发明人： 로스죠제프 , 고띠에띠에리 , 앙드류레지
IPC分类号： C10G45/20
CPC分类号： B01J8/1845 , B01J8/003 , B01J8/0055 , B01J8/0065 , B01J8/1809 , B01J8/1818 , B01J8/1827 , B01J8/1836 , B01J8/1854 , B01J8/1863 , B01J8/28 , B01J8/34 , B01J8/386 , B01J8/388 , B01J2208/00141 , B01J2208/00362 , B01J2208/00371 , B01J2208/00557 , B01J2208/00584 , B01J2208/0084 , B01J2208/00849 , B01J2219/00166 , B01J2219/00247 , C10G1/08 , C10G3/49 , C10G3/57 , C10G3/62 , C10G11/18 , C10G2300/1011 , C10G2300/1037 , C10G2300/708 , C10G2400/20 , Y02P30/40 , Y02P30/42 , Y02P30/446
摘要： A reactor having two fluidized reaction zones with an integrated gas/solid separation system is provided to properly control the total residence time and distribution in several reaction zones. In the reactor having two fluidized reaction zones with an integrated gas/solid separation system, second reaction zones(15,16) are directly connected to a first gas-solid separator. The first gas-solid separator comprises a separation chamber(17) and a stripping chamber(18). The chambers are arranged in turn around the lateral sides of the second reaction zones of a transportation mode. The second reaction zones of a transportation mode communicate with each separation chamber through an opening unit(19) formed on a side wall of the second transportation reaction zone. The separation chamber has a round upper wall(20) and parallel deflectors(21) and separates solid particles and gas without dust. The solid particles stay at the lower side of the separation chamber and then move toward a stripping zone(30) through the opening unit. The gas flows into the stripping chamber. A lower part(31) of the stripping chamber communicates with the stripping zone and is adjacent to the separation chamber through an opening unit cut on a vertical wall of the separation chamber positioned under the deflectors and an upper part communicates with at least a second gas-solid separation system through a line(26).
摘要翻译：提供了具有两个具有集成气/固分离系统的流化反应区的反应器，以适当地控制在几个反应区中的总停留时间和分布。在具有两个具有集成气/固分离系统的流化反应区的反应器中，第二反应区（15,16）直接连接到第一气 - 固分离器。第一气固分离器包括分离室（17）和汽提室（18）。这些腔室依次布置在运输模式的第二反应区域的侧面。运输模式的第二反应区通过形成在第二输送反应区的侧壁上的开口单元（19）与每个分离室连通。分离室具有圆形的上壁（20）和平行的偏转器（21），并分离固体颗粒和气体而没有灰尘。固体颗粒停留在分离室的下侧，然后通过开口单元移动到汽提区（30）。气体流入汽提室。汽提室的下部（31）与汽提区连通，并且通过开口单元与分离室相邻，所述打开单元切割在位于偏转器下方的分离室的垂直壁上，并且上部与至少第二气体 - 固体分离系统（26）。

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