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公开(公告)号：KR100870756B1
公开(公告)日：2008-11-26
申请号：KR1020070039406
申请日：2007-04-23
Applicant: 한국에너지기술연구원
Abstract: 본 발명은 두 개의 유동층 반응기 사이에서 고체분사노즐, 고체상승관, 및 고체재순환관을 포함한 고체이송순환 방법 및 장치에 관한 것으로, 더욱 상세하게는 고체유입구멍을 갖는 고체분사노즐을 이용하여 고체를 분사시키고, 고체상승관과 고체재순환관을 통해 다른 반응기로 이송하는 방법 및 장치에 관한 것이다.
유동층 반응기, 고체분사노즐, 고체 상승관, 사이클론, 고체 재순환관-
公开(公告)号：KR1020110138118A
公开(公告)日：2011-12-26
申请号：KR1020100058261
申请日：2010-06-18
Applicant: 한국에너지기술연구원
Abstract: PURPOSE: A fluidized bed reaction apparatus using a solid spraying nozzle with a bent part is provided to bend the solid spraying nozzle and to install the solid spraying nozzle in the second region of fluidized bed reactors. CONSTITUTION: A fluidized bed reaction apparatus includes distributing plates(112a, 112b), solid spraying nozzles(115a, 115b), bent parts(116a, 116b), and solid circulating pipes(130a, 130b). The distributing plates separate a first region(111a) and a second region(113a). Reaction gas is contained in the first region. Solid particles are contained in the second region. The distributing plates form a plurality of holes to transfer reaction gas to the second region. The solid spraying nozzles introduce and emit gas for solid spraying gas. The bent parts are formed between one end part and another end part of the solid spraying nozzles. The solid circulating pipes are in connection with another end part of the solid spraying nozzles.
Abstract translation: 目的：提供使用具有弯曲部分的固体喷嘴的流化床反应装置来弯曲固体喷雾喷嘴并将固体喷雾喷嘴安装在流化床反应器的第二区域中。 构成：流化床反应装置包括分配板（112a，112b），固体喷嘴（115a，115b），弯曲部分（116a，116b）和固体循环管（130a，130b）。 分配板分离第一区域（111a）和第二区域（113a）。 反应气体包含在第一区域中。 固体颗粒包含在第二区域中。 分配板形成多个孔，以将反应气体转移到第二区域。 固体喷嘴引入并排出固体喷雾气体。 弯曲部分形成在固体喷嘴的一端部和另一端部之间。 固体循环管与固体喷嘴的另一端部连接。
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Patent Agency Ranking
公开(公告)号：KR1020110008759A
公开(公告)日：2011-01-27
申请号：KR1020090066265
申请日：2009-07-21
Applicant: 한국에너지기술연구원
CPC classification number: F23C10/20 , F23C10/22 , F23C2206/10
Abstract: PURPOSE: A CLC(Chemical-Looping Combustor) and a chemical-looping combustion method using the same are provided to improve the reaction efficiency by distributing the fuel, which is injected into a reduction reactor, to a lower fuel inlet and side gas inlets. CONSTITUTION: A CLC(100) comprises an oxidation reactor(110), a reduction reactor(120), a lower fuel inlet(121), and one or more side gas inlets(123,124). The lower fuel inlet is located in the lower part of the reduction reactor. The side gas inlets are located on one side of the reduction reactor.
Abstract translation: 目的：提供CLC（化学循环燃烧器）和使用其的化学循环燃烧方法，以通过将注入还原反应器的燃料分配到较低的燃料入口和侧气体入口来提高反应效率。 构成：CLC（100）包括氧化反应器（110），还原反应器（120），下燃料入口（121）和一个或多个侧气体入口（123,124）。 下部燃料入口位于还原反应器的下部。 侧气体入口位于还原反应器的一侧。
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公开(公告)号：KR1020100023382A
公开(公告)日：2010-03-04
申请号：KR1020080082107
申请日：2008-08-21
Applicant: 한국에너지기술연구원
CPC classification number: F27B15/10 , F27D7/04 , F27D2099/0086
Abstract: PURPOSE: A gas distribution plate of a fluidized bed reactor is provided to reduce the amount of a losing pressure by increasing a spray pressure using a mesh network in between an upper plate and the lower plate. CONSTITUTION: A gas distribution plate of a fluidized bed reactor(10) divides the inside of the fluidized bed reactor into an upper pulverized body flow chamber and an lower gas inflow chamber. The gas distribution plate of the fluidized bed reactor includes a mesh(30). The main body board of the gas distribution plate includes multiple jet holes. The through-holes of the mesh are smaller than the diameter of a pulverized body. The gas distribution plate of the fluidized bed reactor prevents the pulverized body from flowing in the gas inflow chamber.
Abstract translation: 目的：提供一种流化床反应器的气体分配板，通过使用上板和下板之间的网状网络增加喷射压力来减少失压的量。 构成：流化床反应器（10）的气体分配板将流化床反应器的内部分成上部粉碎体流动室和下部气体流入室。 流化床反应器的气体分配板包括网（30）。 气体分配板的主体板包括多个喷射孔。 网孔的通孔小于粉碎体的直径。 流化床反应器的气体分布板防止粉碎体在气体流入室中流动。
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公开(公告)号：KR101214115B1
公开(公告)日：2012-12-20
申请号：KR1020100058261
申请日：2010-06-18
Applicant: 한국에너지기술연구원
Abstract: 본발명은유동층반응장치에관한것으로서, 반응기체와고체입자가반응하는복수의유동층반응기의내부에장착되어반응기체가수용되는제1영역과고체입자가수용되는제2영역을분리하는분산판과, 각유동층반응기의상부에유동층반응기에비해상대적으로좁게형성되어제2영역에수용된고체입자가상승되는고체순환관과, 제2영역내에설치되어일측단부는고체순환관내까지연장되고, 타측단부는유동층반응기의측부를관통하며양단사이가 1회이상절곡된절곡부가형성되고절곡부는분산판에인접한영역까지연장된고체분사노즐을포함한다. 이에의해, 고체분사노즐의설치가용이하고고체분사노즐의변형을방지할수 있을뿐만아니라, 고체순환량의조절이용이하고, 유동층반응기내부의온도저하를방지할수 있다.
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公开(公告)号：KR101035663B1
公开(公告)日：2011-05-19
申请号：KR1020090066265
申请日：2009-07-21
Applicant: 한국에너지기술연구원
Abstract: 본 발명은 매체 순환식 연소기 및 이를 이용한 매체 순환식 연소 방법에 관한 것으로, 구체적으로는 산화 반응기 및 환원 반응기를 포함하는 매체 순환식 연소기에 있어서, 상기 환원 반응기의 하부에 위치한 하부 연료 주입구; 및 상기 환원 반응기의 일 측면에 위치한 연료 기체를 주입할 수 있는 다단의 측면 기체 주입구를 포함하는 것을 특징으로 하는 매체 순환식 연소기 및 이를 이용한 매체 순환식 연소 방법을 제공한다.
본 발명은 환원 반응기에 유입되는 연료를 하부 연료 주입구와 측면 기체 주입구로 분산하여 유입시킴으로써 환원 반응기의 상부에서의 반응 속도가 감소되지 않게 하여 반응 효율을 증가시키며 이로 인해 불완전 연소 생성물인 CO의 발생량을 줄일 수 있다.
매체 순환식 연소, 다단 기체 주입구, 측면 기체 주입구-
公开(公告)号：KR1020080095069A
公开(公告)日：2008-10-28
申请号：KR1020070039406
申请日：2007-04-23
Applicant: 한국에너지기술연구원
Abstract: A method and an apparatus are provided to circulate solids, control the solid circulating speed easily, reduce the leakage of gas, reduce the process volume while simplifying the entire process, and increase the residence time of the gas without requiring gas and flow control equipment between two fluidized-bed reactors. As a fluidized-bed reaction apparatus for circulating solids from one fluidized-bed reactor to the other fluidized-bed reactor between two or more fluidized-bed reactors applied to a fluidized-bed process of two columns or more comprising a carbon dioxide absorbing and regenerating process, an oxidation-reduction process of a chemical-looping combustor, sorption enhanced steam methane reforming of natural gas, or chemical-looping hydrogen generation process, the fluidized-bed reaction apparatus comprises: fluidized-bed reactors(21,22) in which incoming reaction gases(27,29) and solids are reacted with each other; solid ascension pipes(24a,24b) installed on top parts of the fluidized-bed reactors to ascend solids from the fluidized-bed reactors at a flow rate higher than a terminal velocity of the solids; solid spray nozzles(23a,23b) which are penetrated into the fluidized-bed reactors and extend to the solid ascension pipes in parallel to vertical axes of the fluidized-bed reactors, and which have solid inflow holes(31) formed therein at the location within the fluidized-bed reactors; cyclones(25a,25b) which separate solids and gases from the solid ascension pipes, and on which gas and solid outlets are formed; and solid circulation pipes(26a,26b) for recirculating solids from the cyclone into the fluidized-bed reactors.
Abstract translation: 提供了一种循环固体的方法和装置，可以容易地控制固体循环速度，减少气体的泄漏，减少过程体积，同时简化整个过程，并且增加气体的停留时间，而不需要气体和流量控制设备 两个流化床反应器。 作为用于将固体从一个流化床反应器循环到另一个流化床反应器的流化床反应装置，其应用于两塔或更多流化床方法的两个或多个流化床反应器之间，其包含二氧化碳吸收和再生 过程，化学循环燃烧器的氧化还原过程，天然气的吸附增强蒸汽甲烷重整或化学循环氢气生成过程，流化床反应设备包括：流化床反应器（21,22），其中 进入的反应气体（27,29）和固体彼此反应; 安装在流化床反应器的顶部的固体提升管（24a，24b）以高于固体末端速度的流速从流化床反应器中提升固体; 固体喷嘴（23a，23b）穿透入流化床反应器并延伸到与流化床反应器的垂直轴平行的固体提升管，并且在该位置处形成有固体流入孔（31） 在流化床反应器内; 旋风分离器（25a，25b），其从固体上升管分离固体和气体，并在其上形成气体和固体出口; 以及用于将固体从旋风分离器再循环到流化床反应器中的固体循环管道（26a，26b）。
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