합성가스로부터 메탄올을 제조하는 촉매 및 이의 제조방법
    21.
    发明授权
    합성가스로부터 메탄올을 제조하는 촉매 및 이의 제조방법 有权
    合成气制甲醇的催化剂及其制备

    公开(公告)号:KR101823623B1

    公开(公告)日:2018-01-31

    申请号:KR1020150156852

    申请日:2015-11-09

    CPC classification number: Y02P20/52

    Abstract: 본발명은메탄올제조용촉매및 이의제조방법에관한것으로, 더욱상세하게는공침방법에의하여만들어지는촉매에있어서공침조건을제어하여촉매를제조하는방법으로, 복잡한원료를사용하거나제조단계를거치지않고, 메탄올수율을향상시킬수 있는촉매를제조할수 있고, 이를이용하여저온, 저압의액상반응을통하여효율적으로메탄올을합성할수 있다.

    Abstract translation: 而不通过去本发明,并且更具体地,涉及控制共沉淀条件在通过共沉淀方法制得的催化剂,以产生催化剂的方法,一个复杂的用的原料或制造用于制备催化剂及其甲醇的方法的制造工序的, 可以制备可以提高甲醇收率的催化剂,并且可以使用该催化剂在低温低压下通过液相反应有效地合成甲醇。

    슬러리 기포탑 반응기의 온도 제어 시스템
    22.
    发明授权
    슬러리 기포탑 반응기의 온도 제어 시스템 有权
    浆液鼓泡塔反应器温度控制系统

    公开(公告)号:KR101605818B1

    公开(公告)日:2016-03-24

    申请号:KR1020140050985

    申请日:2014-04-28

    CPC classification number: Y02E50/32

    Abstract: 본발명은슬러리기포탑반응기의온도제어시스템및 방법에관한것으로, 석탄합성가스를슬러리에함유된촉매와피셔-트롭쉬(Fischer-Tropsch; FT) 반응에의해합성연료를생성할때 발생하는반응열을효과적으로제어하기위한것이다. 본발명에따르면, 온도제어장치는슬러리기포탑반응기의가동초기에는가열된오일을슬러리기포탑반응기의냉각관으로순환시켜슬러리기포탑반응기의내부온도를 FT 반응온도까지상승시킨다. 그리고 FT 반응이시작되면, 온도제어장치는슬러리기포탑반응기의온도보다는낮은온도의오일을냉각관으로순환시켜슬러리기포탑반응기에서발생되는열을제거한다.

    슬러리 기포탑 반응기의 온도 제어 시스템
    23.
    发明公开
    슬러리 기포탑 반응기의 온도 제어 시스템 有权
    用于控制浆料泡沫反应器温度的装置和方法

    公开(公告)号:KR1020150124549A

    公开(公告)日:2015-11-06

    申请号:KR1020140050985

    申请日:2014-04-28

    CPC classification number: Y02E50/32 C10K3/02 C10G2/00 C10G5/00 C10J3/20

    Abstract: 본발명은슬러리기포탑반응기의온도제어장치및 방법에관한것으로, 석탄합성가스를슬러리에함유된촉매와피셔-트롭쉬(Fischer-Tropsch; FT) 반응에의해합성연료를생성할때 발생하는반응열을효과적으로제어하기위한것이다. 본발명에따르면, 온도제어장치는슬러리기포탑반응기의가동초기에는가열된오일을슬러리기포탑반응기의냉각관으로순환시켜슬러리기포탑반응기의내부온도를 FT 반응온도까지상승시킨다. 그리고 FT 반응이시작되면, 온도제어장치는슬러리기포탑반응기의온도보다는낮은온도의오일을냉각관으로순환시켜슬러리기포탑반응기에서발생되는열을제거한다.

    Abstract translation: 本发明涉及一种用于控制浆液泡沫塔式反应器的温度的装置和方法。 当合成燃料由煤合成气体和浆料中所含的催化剂之间的费 - 托(FT)反应生成时,可以有效地控制产生的反应热。 根据本发明,在浆液泡沫塔式反应器的初始操作期间,该装置将加热的油循环到浆料泡沫塔式反应器的冷却管,使得浆料气泡塔式反应器的内部温度升高至FT 反应温度。 然后,当FT反应开始时,该装置将具有比浆液泡沫塔式反应器的温度低的温度的油循环到冷却管,从而从浆料泡沫塔反应器中产生的热量被去除。

    적층형 유동상 축전식 탈이온화장치
    24.
    发明授权
    적층형 유동상 축전식 탈이온화장치 有权
    堆叠型流动电容式除电装置

    公开(公告)号:KR101282794B1

    公开(公告)日:2013-07-05

    申请号:KR1020120002171

    申请日:2012-01-06

    CPC classification number: C02F1/4691

    Abstract: PURPOSE: A laminated-type fluidized-bed battery-powered deionizer is provided to contribute to bulk desalinization, wastewater treatment, energy storage and commercialization of an energy generator as the laminated-type fluidized-bed battery-powered deionizer provides a module that is more compact than an independent unit-cell parallel connection composition for FCDi capacity expansion. CONSTITUTION: A laminated-type fluidized-bed battery-powered deionizer comprises a unit cell (101) on which one or more is laminated; an upper board (110) which is arranged at the top of the unit cell laminated; and a lower board (170) which is arranged at the bottom of the unit cell laminated. The unit cell contains an active anode fluid path, a active cathode fluid path and an electrolyte fluid path. A couple of anode tubes (111,176) connected respectively to the left end and the right end of the active cathode path are installed in one or two among the upper board and the lower board. A couple of cathode tubes (114,173) respectively connected to the left end and the right end of an anode active substance liquid path are installed one or more directions among the upper plate of the lower plate and a couple of electrolyte pipe (115,172) respectively connected to the left end and the right end of an electrolyte active material liquid path are installed on one direction or both directions among the upper plate and the lower plate. An anode terminal (128) is connected to the anode active material liquid path and a cathode terminal (168) is connected to the cathode active material liquid path.

    Abstract translation: 目的:提供层压型流化床电池供电的去离子器,用于能量发生器的散装脱盐,废水处理,能量储存和商业化,因为层压型流化床电池供电的去离子器提供更多的模块 比独立的单元并联组合紧凑,用于FCDi容量扩展。 构成:层压型流化床电池供电去离子器包括其上层压有一个或多个的单元电池(101); 布置在单元电池顶部的上板(110)层叠; 以及布置在单元电池底部的下板(170)。 单元电池包含活性阳极流体路径,活性阴极流体路径和电解质流体路径。 分别连接到活性阴极通道的左端和右端的一对阳极管(111,176)安装在上板和下板中的一个或两个中。 分别连接到阳极活性物质液体通道的左端和右端的一对阴极管(114,173)在下板的上板之间安装一个或多个方向,并且分别连接一对电解液管(115,172) 在上板和下板之间的一个方向或两个方向上安装电解液活性物质液体通道的左端和右端。 阳极端子(128)连接到负极活性物质液体路径,阴极端子(168)连接到阴极活性物质液体路径。

    수소저장용 Ti-V-Cr-Mn-Mg계 합금 및 그 제조방법
    25.
    发明公开
    수소저장용 Ti-V-Cr-Mn-Mg계 합금 및 그 제조방법 失效
    用于氢储存的TI-V-CR-MN-MG合金及其制备方法

    公开(公告)号:KR1020100116477A

    公开(公告)日:2010-11-01

    申请号:KR1020090035219

    申请日:2009-04-22

    CPC classification number: C22C30/00 C22C27/06 C22C2202/04 C22F1/18 Y02E60/327

    Abstract: PURPOSE: Ti-V-Cr-Mn-Mg alloy for hydrogen storage and a preparation method thereof are provided to occlude more hydrogen by substituting a part of V element with Mn and adding Mg in BCC solid solutions for hydrogen storage. CONSTITUTION: Ti-V-Cr-Mn-Mg alloy for hydrogen storage comprises Ti 33~35 weight%, V 20~27 weight%, Cr 37~39 weight%, Mn 1~8 weight%, and Mg 1~5 weight%. The Ti-V-Cr-Mn-Mg alloy is obtained by substituting a part of V element with Mn and adding Mg in BCC solid solutions for hydrogen storage, wherein Ti, V, Cr, and Mn are ball-milled and Mg is embedded. The hydrogen occluding rate of the Ti-V-Cr-Mn-Mg alloy at the room temperature is 3.46~3.64 weight%.

    Abstract translation: 目的:提供用于储氢的Ti-V-Cr-Mn-Mg合金及其制备方法,以通过用Mn取代V元素的一部分并在BCC固溶体中加入Mg来储存氢来封闭更多的氢。 构成:用于储氢的Ti-V-Cr-Mn-Mg合金包括Ti 33〜35重量%,V 20〜27重量%,Cr 37〜39重量%,Mn 1〜8重量%,Mg 1〜5重量% %。 Ti-V-Cr-Mn-Mg合金是通过用Mn取代一部分V元素并在BCC固溶体中加入Mg进行储氢而得到的,其中Ti,V,Cr和Mn是球磨的,Mg嵌入 。 Ti-V-Cr-Mn-Mg合金在室温下的吸氢率为3.46〜3.64重量%。

    고열유속 마이크로다공성 전열표면의 제조방법 및마이크로다공성 전열관.
    26.
    发明公开
    고열유속 마이크로다공성 전열표면의 제조방법 및마이크로다공성 전열관. 有权
    用高热量及其管制造微波传热表面

    公开(公告)号:KR1020090109603A

    公开(公告)日:2009-10-21

    申请号:KR1020080034944

    申请日:2008-04-16

    Abstract: PURPOSE: A manufacturing of micro-porous heat transfer surface with a high heat flux and a micro-porous tube thereof are provided to improve the adhesive force without a post-process of high-temperature plasticity. CONSTITUTION: A base material(21) consecutively transferred by the automatic control jig transferring device(26) is supplied and rotated. Compound powder mixed with pore-forming agent and coating powder is supplied to a hypersonic powder injection device(10). The base material is transferred and rotated with a hypersonic blow nozzle(25). The supplied compound powder is coated on the surface of the base material by accelerating and crashing using compressed gas. A compound powder is coated layer is washed and the pore-forming agent is completely removed.

    Abstract translation: 目的:提供具有高热通量的微孔传热表面和其微孔管的制造,以提高粘合力,而不需要高温可塑性的后处理。 构成:由自动控制夹具传送装置(26)连续传送的基材(21)被供给并旋转。 向超音速粉末注射装置(10)供给与成孔剂和涂层粉末混合的复合粉末。 基体材料用超音速喷嘴(25)转移并旋转。 通过使用压缩气体加速和撞击将所提供的复合粉末涂覆在基材的表面上。 将复合粉末的涂层进行洗涤,并将成孔剂完全除去。

    자립형 셀프서스테이닝 방식의 열교환기타입 모듈형 리포머
    28.
    发明公开
    자립형 셀프서스테이닝 방식의 열교환기타입 모듈형 리포머 审中-实审
    自维持自热换热器其他口模块化改造器

    公开(公告)号:KR1020170137497A

    公开(公告)日:2017-12-13

    申请号:KR1020160069729

    申请日:2016-06-03

    Abstract: 본발명은반응열을공급하기위한열교환기타입의반응열공급기와격오지나심해환경에서의가스를활용한수소생산을위하여고흡열반응을위한열을흡수하기위한촉매층에충전된메탈폼으로설계된수소를생산할수 있는수소생산량변동이가능한자립형셀프서스테이닝방식의열교환기타입의모듈형리포머에관한것으로본 발명은추가적인외부열원공급없이연속적이고안정적으로높은흡열반응을위한반응열을안정적으로공급할수 있어촉매층의반응온도를안정적으로유지할수 있는효과를갖는다.

    Abstract translation: 本发明可以与用于生产利用eseoui气体深海环境氢气,反应热供给的热交换的其它口ohjina的用于反应的供热以产生氢气的尺寸被设计为填充在催化剂床,以吸收热量用于吸热反应的金属泡沫, 本发明涉及一种模块化重整器,其能够连续且稳定地供应用于高吸热反应的反应热而无需提供额外的外部热源, 这样温度可以保持稳定。

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