철촉매의 제조방법
    31.
    发明公开
    철촉매의 제조방법 有权
    制造铁催化剂的方法

    公开(公告)号:KR1020120054477A

    公开(公告)日:2012-05-30

    申请号:KR1020100115873

    申请日:2010-11-19

    CPC classification number: B01J37/04 B01J23/78 B01J37/031 B01J37/06 B01J37/08

    Abstract: PURPOSE: A method for manufacturing an iron catalyst is provided to reduce the amount of distilled water required for filtering and washing by remaining the adequate amount of sodium in the catalyst. CONSTITUTION: A method for manufacturing an iron catalyst includes the following: a mixed solution is prepared by mixing a ferric nitrate aqueous solution and a copper nitrate aqueous solution(S10); at least one of a sodium carbonate aqueous solution or a sodium hydroxide aqueous solution is added into the mixed solution to form precipitated slurry(S20); the precipitated slurry is washed and filtered based on distilled water(S30); fumed silica powder and a potassium carbonate solution are added into the precipitated slurry to be stirred(S40); the precipitated slurry passes through a sieve and is dried to form a powdered iron catalyst(S50); and the iron catalyst is dried and thermally treated(S60).

    Abstract translation: 目的:提供一种制造铁催化剂的方法,以通过在催化剂中保留足够量的钠来减少过滤和洗涤所需的蒸馏水量。 构成:铁催化剂的制造方法包括:将硝酸铁水溶液和硝酸铜水溶液混合制备混合溶液(S10); 向混合溶液中添加碳酸钠水溶液或氢氧化钠水溶液中的至少一种,形成析出的浆料(S20)。 基于蒸馏水洗涤沉淀的浆液并过滤(S30); 将煅制二氧化硅粉末和碳酸钾溶液加入到待搅拌的沉淀浆料中(S40); 沉淀的浆料通过筛子并干燥以形成粉末状铁催化剂(S50); 并对铁催化剂进行干燥和热处理(S60)。

    복합 반응이 가능한 F-T 기포탑 반응기
    32.
    发明公开
    복합 반응이 가능한 F-T 기포탑 반응기 有权
    FISCHER-TROPSCH BUBBLE COLUMN REACTOR FEASIBLE MULTI REACTION

    公开(公告)号:KR1020120033623A

    公开(公告)日:2012-04-09

    申请号:KR1020100095241

    申请日:2010-09-30

    CPC classification number: B01J8/22 B01J8/28 B01J8/44 C10G2/332 C10G2/344

    Abstract: PURPOSE: A complex reactable Fischer-Tropsch(F-T) bubble column reactor is provided to simplify manufacturing facilities and to improve the yield of synthetic fuel by improving energy efficiency of the reactor. CONSTITUTION: A complex reactable F-T bubble column reactor includes a first dispersing unit(20a) and a second dispersing unit(20b). The first dispersing unit and the second dispersing unit define the inside of a bubble column reactor main body(10) such that two complex reaction regions are formed in the main body. A first reaction region(20a-1) is formed at the upper side of the first dispersing unit and implements a F-T reaction with Fe-catalyst. A second reaction region(20b-1) is formed at the upper side of the second dispersing unit and implements a F-T reaction with Fe/Co catalyst or Co catalyst. The F-T bubble column reactor reacts coal synthetic gas with catalyst contained in slurry to generate synthetic fuel.

    Abstract translation: 目的:提供复杂的可反应费 - 托(F-T)气泡塔反应器,以简化制造设施,并通过提高反应堆的能量效率来提高合成燃料的产量。 构成:复合物可反应的F-T鼓泡塔反应器包括第一分散单元(20a)和第二分散单元(20b)。 第一分散单元和第二分散单元限定气泡塔反应器主体(10)的内部,使得在主体中形成两个复合反应区域。 在第一分散单元的上侧形成第一反应区域(20a-1),并与Fe-催化剂进行F-T反应。 第二反应区(20b-1)形成在第二分散单元的上侧,并与Fe / Co催化剂或Co催化剂进行F-T反应。 F-T鼓泡塔式反应器使煤合成气与浆料中所含的催化剂反应生成合成燃料。

    FT 슬러리 기포탑 반응 시스템용 촉매 분리장치
    33.
    发明授权
    FT 슬러리 기포탑 반응 시스템용 촉매 분리장치 有权
    用于FT浆料气泡塔反应体系的催化剂分离装置

    公开(公告)号:KR100906994B1

    公开(公告)日:2009-07-08

    申请号:KR1020080057947

    申请日:2008-06-19

    CPC classification number: C10G2/342

    Abstract: A catalyst separation apparatus for an FT slurry bubble column reaction system is provided to produce synthetic fuel with a high purity by effectively removing an iron catalyst in synthetic fuel and increase the production efficiency of the synthetic fuel by separating the iron catalyst more promptly. A catalyst separation apparatus(100) for an FT slurry bubble column reaction system comprises: a separation tank(110) connected to an FT slurry bubble column reactor to receive synthetic fuel; a catalyst separating unit(130) adhered to an outer peripheral surface of the separation tank to adhere an iron catalyst contained in the synthetic fuel to an inner wall surface of the separation tank by magnetism; and a separation unit(120) transferring the iron catalyst adhered to the inner wall surface of the separation tank to the bottom of the separation tank to resupply the iron catalyst to the FT slurry bubble column reactor through an iron catalyst discharge pipe. The catalyst separating unit includes a magnet(131) and an insulating material(132). The separation unit includes a drive unit(121), a drive shaft, and a screw(122). The screw has a space part(122a) formed therein in the axial direction, and the screw is connected to the drive shaft through a support connected to the space part.

    Abstract translation: 提供了一种用于FT浆料鼓泡塔反应体系的催化剂分离装置,通过有效地除去合成燃料中的铁催化剂,通过更迅速地分离铁催化剂,提高合成燃料的生产效率,从而生产高纯度的合成燃料。 一种用于FT浆料鼓泡塔反应体系的催化剂分离装置(100)包括:连接到FT浆液鼓泡塔反应器以接收合成燃料的分离罐(110) 催化剂分离单元(130),粘附到分离罐的外周表面,以将含有合成燃料的铁催化剂通过磁力粘附到分离罐的内壁表面; 以及分离单元(120),其将粘附到分离罐的内壁表面的铁催化剂转移到分离罐的底部,以通过铁催化剂排出管将铁催化剂再供给FT浆料鼓泡塔反应器。 催化剂分离单元包括磁体(131)和绝缘材料(132)。 分离单元包括驱动单元(121),驱动轴和螺钉(122)。 螺杆在轴向上形成有空间部分(122a),并且螺钉通过连接到空间部分的支撑件连接到驱动轴。

    이차 전지의 잔류 아연 측정 및 제거 방법

    公开(公告)号:KR102225660B1

    公开(公告)日:2021-03-12

    申请号:KR1020190170328

    申请日:2019-12-19

    Abstract: 본발명은아연기반흐름전지에서충전시음극에전착되는금속아연의양을정확히측정하고, 이를효과적으로제거될수 있도록하는이차전지의잔류아연측정및 제거방법에관한것이다. 본발명에따른잔류아연측정방법은셀 내에존재하는전해액을회수하는단계, 산화바나듐을포함하는용액을셀에넣고순환시켜잔류아연을용해시키는단계, 잔류아연을용해시킨후 감소된 VO2+양을통해잔류아연의양을계산하는단계를포함한다.

    흐름식 에너지 저장장치 및 그에 사용되는 반응셀
    36.
    发明授权
    흐름식 에너지 저장장치 및 그에 사용되는 반응셀 有权
    其中使用流动型储能装置和反应池

    公开(公告)号:KR101830079B1

    公开(公告)日:2018-02-20

    申请号:KR1020150054409

    申请日:2015-04-17

    Abstract: 본발명은유체의흐름이개선된흐름식에너지저장장치에관한것으로, 유동성물질을이용하여전기를저장하는흐름식에너지저장장치에있어서, 상기유동성물질이전기를충전또는방출하는반응영역의단면이 8각형인것을특징으로한다. 본발명은, 반응영역의형상을제어하여유동성물질의흐름을개선함으로써, 충방전사이클을반복하여도전기적특성에변화가거의없는흐름식에너지저장장치를제공할수 있는효과가있다. 또한, 본발명은유입공과유출공의구조를복잡하게구성하거나내부에유체의흐름을제어하는별도의부품을사용하지않기때문에, 흐름식에너지저장장치를제조하는과정에서추가적인비용이소요되지않는효과가있다.

    Abstract translation: 流体型储能装置技术领域本发明涉及一种流体型储能装置,其具有改进的流体流动,其中填充或排出流通型物质转移装置的反应区域的横截面为8 并有一个方形的形状。 本发明的效果在于提供一种即使通过控制反应区域的形状来反复进行充放电循环,电特性几乎不变化,流动型的蓄电装置也能够改善流体材料的流动的效果。 另外,由于本发明不使用流入孔和流出孔的复杂结构或用于控制流入孔和流出孔内的流体的流动的单独部件, 一。

    펠트 전극 특성 분석용 셀의 작업 전극 및 이를 구비하는 펠트 전극 분석용 셀
    37.
    发明授权
    펠트 전극 특성 분석용 셀의 작업 전극 및 이를 구비하는 펠트 전극 분석용 셀 有权
    用于分析毡电极特性的电池的工作电极和用于分析具有工作电极的毡电极的电池

    公开(公告)号:KR101763382B1

    公开(公告)日:2017-08-02

    申请号:KR1020150121091

    申请日:2015-08-27

    CPC classification number: H01M8/188 H01M4/86 H01M8/04 Y02E60/528

    Abstract: 본발명은레독스플로우전지(redox flow battery)에사용되는펠트전극의특성을분석하기위한펠트전극특성분석용셀에관한것으로, 전해질이충진되는공간이형성된전해질챔버와, 분석의기준값이되는기준전극을구비하는기준전극부, 기준전극부를기준으로일측면에배치되며, 분석대상이되는펠트전극인작업전극을구비하고, 작업전극에가해지는압력을일정하게유지한상태로작업전극으로부터응답하는전류측정을위한작업전극부, 기준전극부를기준으로작업전극부의반대편에배치되며, 상대전극을구비하여작업전극부에서전자전달이이루어짐에따른전하밸런스를유지하는상대전극부를포함하여펠트전극의전기적특성을정확하게분석할수 있다.

    Abstract translation: 本发明涉及一种毡电极表征yongsel用于分析在氧化还原液流电池(氧化还原液流电池)中使用的毡尖电极,和电解质腔室,形成的空间电解质yichungjin,基准电极,其是分析的参考值的特性 具有参考电极部件,参考被放置在一侧,以引用的电极部件,具有工作电极毡电极,其可以保留所述分析物,和一个常数变压力为从工作电极的响应在工作电极状态的电流测量 工作电极部分,所述参考电极设置在工作电极部的另一侧到部件的标准为,包括由具有对置电极的对置电极部分,以保持从工作电极的部分准确地毡尖电极的电性质的电子转移yirueojim的电荷平衡 你可以分析。

    레독스 흐름 전지
    38.
    发明授权
    레독스 흐름 전지 有权
    氧化还原液流电池

    公开(公告)号:KR101689134B1

    公开(公告)日:2016-12-27

    申请号:KR1020140159812

    申请日:2014-11-17

    Abstract: 본발명은레독스흐름전지에관한것으로, 높은전지전위와높은에너지효율을가지고, 안정적인충방전성능을제공하는레독스흐름전지를제공하기위한것이다. 이러한본 발명은음극부와양극부가세퍼레이터를기준으로구분되도록배치되는스택, 스택에폴리티오펜을포함한전해질을제공하는펌프, 및폴리티오펜을저장하는탱크를포함하는레독스흐름전지를제공한다.

    Abstract translation: 氧化还原液流电池技术领域本发明涉及一种氧化还原液流电池,其目的在于提供具有高电池电位和高能量效率的氧化还原液流电池,并提供稳定的充放电性能。 本发明提供了一种氧化还原液流电池,包括:叠层,被布置成相对于隔板分离负电极单元和正电极单元; 配置为将电解质(包括聚噻吩)供应到所述堆叠的泵; 和储存聚噻吩的储罐。

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