칼륨이 포함된 고온 피셔-트롭쉬 합성 반응용 철-카바이드/탄소 나노복합 촉매의 제조 방법 및 그 촉매, 철-카바이드/탄소 나노복합 촉매를 이용한 액체 탄화수소의 제조방법 및 그 액체 탄화수소
    121.
    发明授权
    칼륨이 포함된 고온 피셔-트롭쉬 합성 반응용 철-카바이드/탄소 나노복합 촉매의 제조 방법 및 그 촉매, 철-카바이드/탄소 나노복합 촉매를 이용한 액체 탄화수소의 제조방법 및 그 액체 탄화수소 有权
    碳纳米管/碳纳米复合催化剂的制备方法,包括用于高温FISCHER-TROPSCH合成反应的添加剂和碳纳米管/碳纳米复合催化剂,以及使用其的液体烃的制造方法及其液体碳氢化合物的制备方法

    公开(公告)号:KR101339902B1

    公开(公告)日:2013-12-10

    申请号:KR1020130032580

    申请日:2013-03-27

    Abstract: The present invention relates to a manufacturing method for an iron-carbide/carbon nanocomposite catalyst containing a potassium additive for high temperature fischer-tropsch synthesis reaction, the iron-carbide/carbon nanocomposite catalyst, a manufacturing method for liquid hydrocarbon using the iron-carbide/carbon nanocomposite catalyst and the liquid hydrocarbon. The purpose of the present invention is to provide the manufacturing method for the iron-carbide/carbon nanocomposite catalyst containing the potassium additive for high temperature fischer-tropsch synthesis reaction which uniformly dips potassium by using various methods such as a prior addition method which uniformly dips heptahydrate salt in an inner portion of a porous carbon support through a melt infiltration method while grinding and putting potassium salt, a middle addition method which infiltrates a potassium solution by a wet dip-coating method after the dip-coating of iron salt and a post addition method, the iron-carbide/carbon nanocomposite catalyst, the manufacturing method for liquid hydrocarbon using the iron-carbide/carbon nanocomposite catalyst and the liquid hydrocarbon. The present invention can produce a highly activated iron-carbide/potassium/carbon-based composite catalyst for a high temperature F-T reaction, wherein 5-30 wt% of activated iron-carbide particles are dipped in the porous carbon support and can manufacture liquid hydrocarbon in a high yield rate since the highly activated iron-carbide/potassium/carbon-based composite catalyst for a high temperature F-T reaction is thermostable in the high temperature F-T reaction of more than 300°C. [Reference numerals] (AA) Iron hydrate;(BB) Porous carbon supporter;(CC) K compound pre-addition method;(DD) Form amorphous Fe-C composites;(EE) K compound mid-addtion method;(FF) Iron-carbide/carbon composite formation;(GG) K compound late-addition method;(HH) Iron-carbide/calcium/carbon composite

    Abstract translation: 本发明涉及含有用于高温费 - 托合成反应的钾添加剂的铁碳化物/碳纳米复合催化剂的制造方法,碳化铁/碳纳米复合催化剂,使用铁碳化物的液体烃的制造方法 /碳纳米复合催化剂和液态烃。 本发明的目的是提供含有用于高温费 - 托合成反应的钾添加剂的碳化铁/碳纳米复合催化剂的制造方法,其通过使用均匀浸渍的各种方法如均匀浸渍钾 七水合盐在多孔碳载体的内部通过熔融渗透法同时研磨和加入钾盐,中间添加方法在浸渍铁盐和后处理之后通过湿式浸涂法渗透钾溶液 铁碳化物/碳纳米复合催化剂,使用碳化铁/碳纳米复合催化剂和液态烃的液态烃的制造方法。 本发明可以生产用于高温FT反应的高活性铁碳化物/钾/碳基复合催化剂,其中将5-30重量%的活性碳化铁颗粒浸入多孔碳载体中,并可制备液体烃 由于高温FT反应的高活性铁碳化物/钾/碳基复合催化剂在高于300℃的高温FT反应中是耐热的,所以以高产率。 (AA)铁水合物;(BB)多孔碳载体;(CC)K化合物预加成法;(DD)非晶态Fe-C复合材料;(EE)K化合物中添加法;(FF) 铁碳化物/碳复合物形成;(GG)K复合后加法;(HH)铁碳化物/钙/碳复合材料

    수화된 금속염의 용융함침을 이용한 금속 또는 산화금속 촉매 담지체의 제조 방법 및 그 금속 또는 산화금속 촉매 담지체
    122.
    发明授权
    수화된 금속염의 용융함침을 이용한 금속 또는 산화금속 촉매 담지체의 제조 방법 및 그 금속 또는 산화금속 촉매 담지체 有权
    使用金属水合物盐和金属或金属氧化物催化剂载体的熔融渗透法制备金属或金属氧化物催化剂载体的方法

    公开(公告)号:KR101317723B1

    公开(公告)日:2013-10-15

    申请号:KR1020110075280

    申请日:2011-07-28

    Abstract: 본 발명은 수화된 금속염의 용융함침을 이용한 금속 또는 산화금속 촉매 담지체의 제조 방법 및 그 금속 또는 산화금속 촉매 담지체에 관한 것으로, 그 목적은 질산수화물 금속염이나 염화수화물 금속염의 낮은 용융점을 이용하여 금속 또는 산화금속 촉매 담지체를 대량으로 쉽고, 빠르게 제조하는 방법 및 그 금속 또는 산화금속 촉매 담지체를 제공하는 데 있다.
    본 발명은 a) 금속 수화물 염을 다공 구조의 금속 지지체와 혼합하는 단계와; b) 혼합후 금속 수화물 염의 융점에서 용융 함침시켜 금속 수화물 염을 지지체에 담지하는 단계와; c) 지지체에 담지된 금속 수화물 염을 고온 소성시켜 분해하여 나노 입자화하는 단계;로 이루어진 수화된 금속염의 용융함침을 이용한 금속 또는 산화금속 촉매 담지체의 제조 방법 및 이로부터 제조된 금속 또는 산화금속 촉매 담지체를 발명의 특징으로 한다.

    동적 기체분배기 및 그를 적용한 기포탑 반응기
    124.
    发明公开
    동적 기체분배기 및 그를 적용한 기포탑 반응기 有权
    动态气体分布器和包含动态气体分配器的气瓶

    公开(公告)号:KR1020130046344A

    公开(公告)日:2013-05-07

    申请号:KR1020120094731

    申请日:2012-08-29

    Abstract: PURPOSE: A dynamic gas distributor and a bubble column reactor applying the same are provided to improve a catalyst and a reaction efficiency in the reactor main body and to prevent a malfunction of the dynamic gas distributor and the loss of the catalyst by minimizing the back flow of the slurry in the reactor main body to the dynamic gas distributor during the reaction or at the completion of reaction. CONSTITUTION: A bubble column reactor comprises a reactor main body(10) and a dynamic gas distributor(20) arranged to be connected to the lower part of the reactor main body. The reactor main body stores the slurry containing the catalyst. The synthetic fuel is produced by the reaction of the slurry containing the catalyst with the synthesis gas introduced in the main body. The gas distributor disperses the synthesis gas supplied through the inlet tube(24) by rotation, converts the dispersed synthesis gas into the uniform bubble particle, and supplies this to the inside of the reactor main body.

    Abstract translation: 目的:提供动态气体分配器和应用其的气泡塔型反应器,以改善反应器主体中的催化剂和反应效率,并通过最小化反向流动来防止动态气体分配器的故障和催化剂的损失 的反应器主体中的浆料在反应期间或在反应完成时传递给动态气体分布器。 构成:泡罩塔反应器包括反应器主体(10)和布置成连接到反应器主体的下部的动态气体分配器(20)。 反应器主体储存含有催化剂的浆料。 合成燃料通过含有催化剂的浆料与引入主体的合成气的反应而产生。 气体分配器通过旋转分散通过入口管(24)供应的合成气,将分散的合成气转化成均匀的气泡颗粒,并将其提供给反应器主体的内部。

    철-코발트 복합 촉매 및 그 제조 방법과 이를 촉매로 이용한 피셔-트롭쉬 합성 반응에서의 수성가스전환반응 활성구현과 고선택적 액체 연료 제조방법
    125.
    发明公开
    철-코발트 복합 촉매 및 그 제조 방법과 이를 촉매로 이용한 피셔-트롭쉬 합성 반응에서의 수성가스전환반응 활성구현과 고선택적 액체 연료 제조방법 有权
    铁钴催化剂,其制造方法和获得水煤气移动反应活性的方法以及使用铁钴催化剂的FISCHER-TROPSCH合成中的高选择性液体燃料生产方法

    公开(公告)号:KR1020130005848A

    公开(公告)日:2013-01-16

    申请号:KR1020110067491

    申请日:2011-07-07

    Abstract: PURPOSE: A method for preparing iron-cobalt composite catalyst and a method for implementing water-gas shift reaction activity in Fischer-Tropsch synthesis and producing highly selective liquid fuel using the same are provided to enhance the yield of liquid. CONSTITUTION: A method for preparing iron-cobalt composite catalyst comprises: a step of supporting 5-20 parts by weight of cobalt with respect to 100 parts by weight of an iron catalyst(S140); and drying the supported iron-cobalt at 100-150 deg.C. for 3-5 hours(S150). The method further comprises a step of plasticizing the iron-cobalt; and a step of reducing the iron-cobalt under a hydrogen atmosphere. [Reference numerals] (AA) Start; (BB) End; (S100) Precipitating iron(Fe), copper(Cu), and Na_2CO_3; (S110) Washing for removing sodium elements from precipitate; (S120) Mixing an SiO_2 solution and a K_2CO_3 solution with the precipitate; (S130) Spray-drying; (S140) Supporting the predetermined amount of cobalt; (S150) Drying the supported iron-cobalt

    Abstract translation: 目的:提供一种制备铁 - 钴复合催化剂的方法和一种在费 - 托合成中实现水煤气变换反应活性的方法,并使用该方法生产高选择性液体燃料,以提高液体的产率。 构成:制备铁 - 钴复合催化剂的方法包括:相对于100重量份的铁催化剂(S140),支持5-20重量份的钴的步骤; 并在100-150℃干燥负载的铁 - 钴。 持续3-5小时(S150)。 该方法还包括使铁 - 钴增塑的步骤; 以及在氢气氛下还原铁钴的工序。 (附图标记)(AA)开始; (BB)结束; (S100)沉淀铁(Fe),铜(Cu)和Na_2CO_3; (S110)从沉淀物中除去钠元素的洗涤液; (S120)将沉淀物与SiO 2溶液和K 2 CO 3溶液混合; (S130)喷雾干燥; (S140)支持规定量的钴; (S150)干燥负载的铁钴

    철촉매의 제조방법
    126.
    发明授权
    철촉매의 제조방법 有权
    制造铁催化剂的方法

    公开(公告)号:KR101219644B1

    公开(公告)日:2013-01-08

    申请号:KR1020100115873

    申请日:2010-11-19

    Abstract: 본발명에의한철촉매의제조방법은질산철(Fe(NO))수용액과질산구리(Cu(NO))수용액을혼합하여혼합용액을제조하는혼합단계; 상기혼합용액에탄산나트륨(NaCO) 또는수산화나트륨(NaOH)수용액중 적어도하나를첨가하여침전슬러리를형성시키는침전슬러리형성단계; 상기침전슬러리를증류수를이용하여여과및 세척하는세척단계; 상기침전슬러리에건식실리카(Fumed Silica) 파우더와탄산칼륨(KCO)용액을첨가하고교반하는실리카첨가단계; 상기침전슬러리를 30㎛내지 100㎛크기의체(sieve)에통과시킨후, 분무건조방식을이용하여건조시켜분말형태의철촉매를제조하는건조단계; 상기철촉매를 50℃내지 150℃의온도에서건조시킨후, 300℃내지 500℃에서열처리하는열처리단계;를포함하여이루어지는것을특징으로한다. 본발명에의하면, 철, 구리, 칼륨, 코발트, 나트륨, 실리카등을최적의비율로혼합함으로써, 합성반응에서의반응성을현저히향상시킬수 있으며, 종래와달리, 제조공정에서적절한양의나트륨을촉매에자연스럽게잔류시킴으로써, 여과및 세척에필요한증류수의양을 80%이상줄일수 있어, 친환경적이면서경제적일뿐만아니라, 여과및 세척에필요한시간또한 15시간에서최대 2시간까지현저히단축시킬수 있어생산성또한우수한장점이있다.

    합성가스의 전환율을 높이기 위한 2단 피셔-트롭쉬 반응기 시스템
    127.
    发明公开
    합성가스의 전환율을 높이기 위한 2단 피셔-트롭쉬 반응기 시스템 有权
    第二阶段FISCHER-TROPSCH反应系统,以提高合成气转化率

    公开(公告)号:KR1020120111650A

    公开(公告)日:2012-10-10

    申请号:KR1020110030269

    申请日:2011-04-01

    Abstract: PURPOSE: A two stage F-T reactor system for improving the conversion ratio of synthetic gas is provided to maximize the yield of synthetic fuel for extending the lifetime of a catalyst. CONSTITUTION: A two stage F-T reactor system for improving the conversion ratio of synthetic gas includes a first reactor(10) and a second reactor(20). The first reactor receives first synthetic gas containing H2 and CO in a composition ratio of 0.6-1.2, and controls the flow speed of the first synthetic gas, the internal temperature, and the pressure for securing the 50-80% of CO conversion ratio. The second reactor receives second synthetic gas containing H2 and CO in a composition ratio of 1.8-2.0, and controls the flow speed of the second synthetic gas, the internal temperature, and the pressure for securing the 90-95% of CO conversion ratio.

    Abstract translation: 目的:提供用于提高合成气转化率的两级F-T反应器系统,以最大化合成燃料的产率,延长催化剂的使用寿命。 构成:用于提高合成气体的转化率的两级F-T反应器系统包括第一反应器(10)和第二反应器(20)。 第一反应器以0.6-1.2的组成比接收含有H 2和CO的第一合成气体,并控制第一合成气体的流速,内部温度和用于确保50-80%CO转化率的压力。 第二反应器以1.8-2.0的组成比接收含H2和CO的第二合成气体,并控制第二合成气体的流速,内部温度和压力,以确保90-95%的CO转化率。

    고온 용융로용 인산알루미늄-함유 크롬계 내화재 및 이의 제조방법
    129.
    发明公开
    고온 용융로용 인산알루미늄-함유 크롬계 내화재 및 이의 제조방법 无效
    含ALPO4的高温熔融炉用基于成份的耐火材料及其制备方法

    公开(公告)号:KR1020100048242A

    公开(公告)日:2010-05-11

    申请号:KR1020080107311

    申请日:2008-10-30

    Abstract: PURPOSE: A chromium-based refractory material and a method for manufacturing the same are provided to enhance resistance to fusion slag infiltration and to improve hot strength. CONSTITUTION: A chromium-based refractory material contains 0.1-10 weight% of AIPO based on the total refractory material. The chromium-based refactory material is alumina-chromic material. The chromium-based refractory material contains 40-90 weight% of alumina ingredient and 10-50 weight% of chrome ingredient based on total weight.

    Abstract translation: 目的:提供铬基耐火材料及其制造方法,以增强熔融熔渣渗透性,提高热强度。 构成:基于耐火材料的铬基耐火材料含有0.1-10重量%的AIPO。 铬基的重构材料是氧化铝 - 铬材料。 基于铬的耐火材料包含40-90重量%的氧化铝成分和10-50重量%的铬成分,基于总重量。

    F―T 고정층 반응기 온도조절 장치
    130.
    发明授权
    F―T 고정층 반응기 온도조절 장치 失效
    FISCHER-TROPSCH固定床反应器的温度控制装置

    公开(公告)号:KR100939662B1

    公开(公告)日:2010-02-03

    申请号:KR1020080075163

    申请日:2008-07-31

    CPC classification number: C10G2/341 B01J23/75 C10G2300/703

    Abstract: PURPOSE: A temperature control apparatus of Fischer-Tropsch Fixed-Bed Reactor is provided to constantly maintain inner temperature of Fischer-Tropsch Fixed-Bed Reactor and minimize methane gas and carbon dioxide generation. CONSTITUTION: A temperature control apparatus of Fischer-Tropsch Fixed-Bed reactor comprises: a upper/lower partition plate(11,12) which is placed at the upper and lower portion to fix plural catalyst pipes(70) inside the reactor; a synthetic gas inlet space(21); catalyst fixation space(22); synthetic fuel collection space(23); a heating unit(30) which is connected to the catalyst fixation space and heats the catalyst pipe by reaction temperature; and a cooling unit(40) which is mounted at the catalyst pipe fixation space and cools the catalyst pipe to prevent temperature rise.

    Abstract translation: 目的:提供费 - 托固定床反应器的温度控制装置,以不断保持费 - 托固定床反应器的内部温度,并最大限度地减少甲烷气和二氧化碳的产生。 构成:费托固定床反应器的温度控制装置包括:上/下分隔板(11,12),其放置在上部和下部以将多个催化剂管道(70)固定在反应器内部; 合成气体入口空间(21); 催化剂固定空间(22); 合成燃料收集空间(23); 加热单元(30),其连接到催化剂固定空间,并通过反应温度加热催化剂管; 以及安装在催化剂管固定空间并冷却催化剂管以防止升温的冷却单元(40)。

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