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    리보일링 장치 및 이를 구비한 재생탑
    31.
    发明授权
    리보일링 장치 및 이를 구비한 재생탑 有权
    再生设备和再生塔

    公开(公告)号：KR101550618B1

    公开(公告)日：2015-09-07

    申请号：KR1020140004321

    申请日：2014-01-14

    Applicant: 현대자동차주식회사 ,  기아자동차주식회사 ,  한국에너지기술연구원

    Inventor： 박성열 ,  윤여일 ,  남성찬 ,  배신태

    IPC: B01D53/14 ,  B01D53/96 ,  B01D53/73

    CPC classification number: B01D19/0073 ,  B01D53/1425 ,  B01D53/1475 ,  B01D53/92 ,  B01D2259/455 ,  Y02C10/06

    Abstract: 본발명은재생대상인가스를함유하는흡수액을끓여상기가스를분리하는리보일링장치및 이를구비한재생탑에관한것이다. 본발명의실시예에따른재생탑은내부에공간이형성된제1하우징; 상기제1하우징의상부에위치하며, 리치흡수액을제1하우징의내부로공급하는리치흡수액공급기; 상기제1하우징의내부에서상기리치흡수액공급부아래에위치하며, 제1하우징의하부로공급되는리치흡수액의흐름을정류하는정류기; 상기제1하우징의내부에서상기정류기아래에위치하며, 리치흡수액을끓여재생가스를리치흡수액으로부터분리시키는리보일러; 리치흡수액탱크로서형성되는제2하우징; 상기정류기로부터공급되는리치흡수액이상기리치흡수액탱크로공급되도록하며, 상기리보일러에서발생한재생가스를상기리보일러로의리치흡수액의공급경로와다른경로로상기제1하우징의내부로우회시키며, 상기리보일러와상기정류기사이의제1하우징내부에배치되는세퍼레이터; 그리고상기리보일러에서재생가스가분리된린 흡수액을받는린 흡수액탱크로서형성되는제3하우징;을포함하며, 상기리보일러는상기리치흡수액탱크를통해서만리치흡수액을공급받을수 있다.

    Abstract translation: 再生塔可以包括：富含吸收液体的供应商，其将丰富的吸收液体供应到第一壳体中; 定位在富吸收液体供应器下方的整流器，并且将在第一壳体中向下供应的富吸收液体的整流流动; 再沸器位于整流器下方，通过沸腾富吸收液体将再生气体与富吸收液体分离; 将富集的吸收剂液体从整流器供给到富吸收液体罐的分离器，通过不同于富吸收剂液体的供给路径到再沸器的路径将再沸器中产生的再生气体旁路到第一壳体中; 以及吸收液体容器，其在再沸器中分离有再生气体的贫吸收液体，再沸器仅通过富吸收液体槽容纳富吸收液体。

    탄소나노섬유의 제조방법
    33.
    发明授权
    탄소나노섬유의 제조방법 有权
    碳纳米纤维的制备方法

    公开(公告)号：KR101457130B1

    公开(公告)日：2014-10-31

    申请号：KR1020130126890

    申请日：2013-10-24

    Applicant: 한국에너지기술연구원

    Inventor： 김성수 ,  박성열 ,  김재민 ,  김진걸

    IPC: D01F9/127 ,  B82Y40/00 ,  B01J21/06 ,  B01J23/881 ,  B01J23/70

    CPC classification number: D01F9/127 ,  B01J21/06 ,  B01J23/70 ,  B01J23/881 ,  B82Y40/00

    Abstract: The present invention relates to a method for manufacturing carbon nanofiber. More specifically, the method includes the steps of: manufacturing carbon nanofiber by performing a synthetic gas reaction at 400-850°C under high pressure so as to manufacture the carbon nanofiber; refining the carbon nanofiber by treating the carbon nanofiber, manufactured in the earlier step, with acid; and neutralizing the carbon nanofiber refined in the earlier step. When compared to the prior method, the method of the present invention: includes significantly shortened processes; is economic; and includes processes that can be continuously performed.

    Abstract translation: 碳纳米纤维的制造方法技术领域本发明涉及碳纳米纤维的制造方法。 更具体地说，该方法包括以下步骤：通过在高压下在400-850℃下进行合成气体反应来制造碳纳米纤维，以制造碳纳米纤维; 通过用酸处理在前面步骤中制造的碳纳米纤维来精炼碳纳米纤维; 并中和前面步骤中精制的碳纳米纤维。 当与现有方法相比时，本发明的方法包括显着缩短的工艺; 是经济的 并且包括可以连续执行的处理。

    이산화탄소 분리용 이미다졸륨 이온성 액체 및 그 용도
    34.
    发明公开
    이산화탄소 분리용 이미다졸륨 이온성 액체 및 그 용도 有权
    基于二氧化碳的选择性分离的IMMIDAZOLIUM CATION基离子液体及其使用

    公开(公告)号：KR1020130110358A

    公开(公告)日：2013-10-10

    申请号：KR1020120032247

    申请日：2012-03-29

    Applicant: 한국에너지기술연구원

    Inventor： 백일현 ,  남성찬 ,  박정훈 ,  윤여일 ,  정순관 ,  박성열 ,  박기태 ,  박상도 ,  최수현

    IPC: C07D233/58 ,  B01D53/14 ,  B01D53/62

    CPC classification number: B01D53/1475 ,  B01D53/62 ,  B01D2252/30 ,  B01D2257/504 ,  C07D233/58 ,  Y02C10/04 ,  Y02C10/06 ,  Y02P20/152

    Abstract: PURPOSE: An imidazolium-based ionic liquid for isolating carbon dioxide is provided to have superior carbon dioxide absorbing ability and to easily separate absorbed carbon dioxide by heating. CONSTITUTION: An imidazolium-based ionic liquid compound has carbon dioxide absorption ability and is denoted by chemical formula 1. A carbon dioxide absorbing agent contains the compound. A method for isolating carbon dioxide from a gas mixture comprises the steps of: absorbing carbon dioxide from the gas mixture using the carbon dioxide absorbing agent; and deaerating the absorbed carbon dioxide.

    Abstract translation: 目的：提供用于分离二氧化碳的基于咪唑鎓的离子液体，以具有优异的二氧化碳吸收能力，并通过加热容易地分离吸收的二氧化碳。 构成：咪唑鎓离子液体化合物具有二氧化碳吸收能力，由化学式1表示。二氧化碳吸收剂含有该化合物。 从气体混合物中分离二氧化碳的方法包括以下步骤：使用二氧化碳吸收剂从气体混合物中吸收二氧化碳; 并吸收二氧化碳。

    생물체에서 유래된 지질과 하이드로탈사이트를 이용하는 연속적인 탄화수소 생산 방법 및 장치
    36.
    发明公开
    생물체에서 유래된 지질과 하이드로탈사이트를 이용하는 연속적인 탄화수소 생산 방법 및 장치 有权
    使用氢化钙作为催化剂从生物原料制备碳氢化合物的连续方法和装置

    公开(公告)号：KR1020120058241A

    公开(公告)日：2012-06-07

    申请号：KR1020100119935

    申请日：2010-11-29

    Applicant: 한국에너지기술연구원

    Inventor： 고창현 ,  나정걸 ,  김종남 ,  박성열 ,  박종호 ,  범희태 ,  한상섭 ,  이보은

    IPC: C10G3/00 ,  C07C1/213 ,  B01J21/00 ,  B01J38/50

    CPC classification number: Y02P20/584 ,  Y02P30/20 ,  C10G3/00 ,  B01J21/00 ,  B01J38/50 ,  C07C1/213

    Abstract: PURPOSE: Continuous method and apparatus for preparing hydrocarbon using biological originated lipid and hydrotalcite are provided to produce the hydrocarbon without using hydrogen, and to reduce the operational costs. CONSTITUTION: A continuous method for preparing hydrocarbon using biological originated lipid and hydrotalcite comprises the following steps: supplying raw materials selected from triglyceride, fatty acid, or fatty acid derivative into a first reactor(2); contacting the raw material in the first reactor with a hydrotalcite catalyst to obtain the hydrocarbon; recycling the used hydrotalcite after the termination of the reaction inside the first reactor; supplying the raw materials into a second reactor(3) during the recycling process of the hydrotalcite; contacting the raw materials in the second reactor with the hydrotalcite catalyst to obtain the hydrocarbon; and recycling the used hydrotalcite after the termination of the reaction inside the second reactor, and repeating previous steps.

    Abstract translation: 目的：提供使用生物来源的脂质和水滑石制备碳氢化合物的连续方法和设备，以生产不使用氢气的烃，并降低运行成本。 构成：使用生物来源的脂质和水滑石制备烃的连续方法包括以下步骤：将选自甘油三酯，脂肪酸或脂肪酸衍生物的原料供应到第一反应器（2）中; 使第一反应器中的原料与水滑石催化剂接触以获得烃; 在第一反应器内的反应结束后再循环使用的水滑石; 在水滑石的回收过程中将原料供应到第二反应器（3）中; 使第二反应器中的原料与水滑石催化剂接触以获得烃; 并且在第二反应器内部的反应结束后再循环使用的水滑石，并重复以前的步骤。

    질소산화물의 저감을 위한 온도조절기능을 가지는 충전층촉매반응기
    37.
    发明授权
    질소산화물의 저감을 위한 온도조절기능을 가지는 충전층촉매반응기 有权
    包装床催化反应器，通过温度控制除去NOX

    公开(公告)号：KR100794390B1

    公开(公告)日：2008-01-15

    申请号：KR1020070007370

    申请日：2007-01-24

    Applicant: 한국에너지기술연구원

    Inventor： 문승현 ,  현주수 ,  박성열 ,  최원길 ,  백일현

    IPC: B01D53/86 ,  B01D53/56 ,  B01J8/02

    Abstract: A packed bed type catalytic reactor is provided to bring input gas into complete contact with catalysts, thereby securing the maximum performance of the catalysts, by forming the catalytic reactor in a lattice shape, blocking upper and lower portions of a catalytic layer, and blocking an input gas discharging unit adjacent to the catalytic layer so that the input gas passes the catalytic layer vertically. A catalytic reactor comprises a plurality of exhaust gas input units(10), a plurality of exhaust gas output units(30), and a plurality of catalyst units(20), which are arranged in a lattice structure. Each of the exhaust gas input units has a closed upper portion, an exhaust gas input port formed in a lower portion thereof, and an exhaust gas input space formed therein. Each of the exhaust gas output units has a closed lower portion, an exhaust gas output port formed in an upper portion thereof, and an exhaust gas output space formed therein. Each of the catalyst units has catalysts therein, and closed upper and lower portions. A lateral portion of the catalyst unit is contacted with a lateral portion of the exhaust gas input unit and a lateral portion of the exhaust gas output unit. The exhaust gas input unit and the exhaust gas output unit are separated by the catalyst unit. Further, a net type unit for supporting catalyst is installed at a side of the plurality of catalyst units.

    Abstract translation: 提供了一种填充床式催化反应器，以使输入气体与催化剂完全接触，从而确保催化剂的最大性能，通过形成格子状的催化反应器，阻止催化剂层的上部和下部，并阻断催化剂层 与催化剂层相邻的输入气体排出单元，使得输入气体垂直地通过催化剂层。 催化反应器包括多个废气输入单元（10），多个废气输出单元（30）和多个催化单元（20），它们以格子结构排列。 每个废气输入单元具有封闭的上部部分，形成在其下部的排气输入端口和形成在其中的废气输入空间。 每个废气输出单元具有封闭的下部，形成在其上部的废气输出端口和形成在其中的废气输出空间。 每个催化剂单元都具有催化剂，封闭的上部和下部。 催化剂单元的侧部与废气输入单元的侧部和排气输出单元的侧部接触。 废气输入单元和排气输出单元由催化剂单元分离。 此外，用于支撑催化剂的净型单元安装在多个催化剂单元的一侧。

    선택적비촉매환원법에서 질소산화물 저감을 위한 내부관통형 3중관 환원제 분사기
    38.
    发明授权
    선택적비촉매환원법에서 질소산화물 저감을 위한 내부관통형 3중관 환원제 분사기 有权
    COMBUSTOR交叉三通管式减压剂注射器通过选择性非催化还原减少NOX

    公开(公告)号：KR100794389B1

    公开(公告)日：2008-01-15

    申请号：KR1020070007369

    申请日：2007-01-24

    Applicant: 한국에너지기술연구원

    Inventor： 문승현 ,  엄태인 ,  현주수 ,  박성열

    IPC: B01D53/34 ,  B01D53/56

    Abstract: A reducing agent injector is provided to inject a reducing agent into a combustion room uniformly, thereby maximizing the efficiency in removal of nitrogen oxides, by installing a triple-pipe type injector passing through a wall of the combustion room. A reducing agent injector(14) injects a reducing agent into a combustion room, wherein the reducing agent reacts with nitrogen oxides contained in a combustion gas. The injector is installed such that the injector penetrates both walls(9) of the combustion room. The injector comprises a reducing agent supply pipe(10) having a plurality of injection nozzles(11), a cooling water supply pipe(12) for wrapping the reducing agent supply pipe, and a cooling water discharge pipe(13) communicating with the cooling water supply pipe and wrapping the cooling water supply pipe. The injection nozzles pass through the cooling water supply pipe and the cooling water discharge pipe to be exposed to an outside of the cooling water discharge pipe.

    Abstract translation: 提供还原剂注入器，以通过安装穿过燃烧室的壁的三重管式注射器，将还原剂均匀地注入燃烧室中，从而使氮氧化物的去除效率最大化。 还原剂注入器（14）将还原剂注入燃烧室，其中还原剂与燃烧气体中所含的氮氧化物反应。 喷射器被安装成使得喷射器穿过燃烧室的两个壁（9）。 喷射器包括具有多个注射喷嘴（11）的还原剂供给管（10），用于包装还原剂供给管的冷却水供给管（12）和与冷却水连通的冷却水排出管 供水管和包装冷却水供水管。 注射喷嘴通过冷却水供给管和冷却水排出管，以暴露于冷却水排出管的外部。

    초임계수 결정화법에 의한 바륨페라이트의 연속식 제조방법및 이를 이용한 이산화탄소의 분해 방법
    39.
    发明授权
    초임계수 결정화법에 의한 바륨페라이트의 연속식 제조방법및 이를 이용한 이산화탄소의 분해 방법 有权
    以一种相辅相成的方式生产硼铁矿的方法和使用巴西铁矿粉分解二氧化碳

    公开(公告)号：KR100770691B1

    公开(公告)日：2007-10-29

    申请号：KR1020060053803

    申请日：2006-06-15

    Applicant: 한국에너지기술연구원

    Inventor： 남성찬 ,  김종기 ,  백일현 ,  박성열

    IPC: C01G49/00 ,  B22F9/00 ,  C01F11/00 ,  B01J23/745

    CPC classification number: Y02P20/544 ,  C01G49/0036 ,  B01J2219/0059 ,  C01B32/05

    Abstract: A method for decomposing carbon dioxide using the barium ferrite is provided to decompose almost 100% of carbon dioxide at a quick reaction rate, and to be capable of operating processes continuously by cyclone type of recovery method. A method for decomposing carbon dioxide using the barium ferrite includes the steps of: performing a hydrolysis reaction of an aqueous alkali solution(2) and a mixture(1) of aqueous nitrate solutions containing iron and barium at ambient temperature under a reaction pressure of 30-50 MPa; supplying preheated water(6) to the hydrolysis reaction step to raise the reaction temperature to 100-400 °C, and staying the preheated water for 3-10 seconds to form critical nuclei; supplying preheated water(8) to heat the hydrolysate to the supercritical temperature for water, performing a final dehydration reaction in a reactor(9) maintaining a supercritical state to collect barium ferrite continuously; and hydrogenating the barium ferrite, and then reacting the hydrogenated barium ferrite with carbon dioxide.

    Abstract translation: 提供使用钡铁氧体分解二氧化碳的方法，以快速反应速率分解几乎100％的二氧化碳，并且能够通过旋风式回收方法连续操作。 使用钡铁氧体分解二氧化碳的方法包括以下步骤：在环境温度下，在30℃的反应压力下进行碱金属溶液（2）和含铁和钡的硝酸盐水溶液的混合物（1）的水解反应 -50 MPa; 向水解反应步骤中提供预热水（6），将反应温度升高至100-400℃，并将预热水保持3-10秒，形成临界核; 提供预热水（8）将水解产物加热至超临界温度，在反应器（9）内进行最终脱水反应，保持超临界状态，连续收集钡铁氧体; 并使钡铁氧体氢化，然后使氢化钡铁氧体与二氧化碳反应。

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