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    • 22. 发明公开
    • 허니컴 촉매의 제조 방법
    • 蜂窝状催化剂的制备方法
    • KR1020130000891A
    • 2013-01-03
    • KR1020110061696
    • 2011-06-24
    • 주식회사 나노
    • 신동우유상희정기봉박삼식
    • B01J35/04B01J23/30B01J37/02B01J37/08
    • B01J37/0215B01J23/30B01J35/04B01J37/08
    • PURPOSE: A producing method of a honeycomb catalyst is provided to reduce production cost and to improve denitrification efficiency by forming and extruding catalytic clay to form a honeycomb molded body and by uniformly coating a co-catalyst solution containing a tungsten precursor on the honeycomb molded body using a dip coating process. CONSTITUTION: A producing method of a honeycomb catalyst includes the following steps: raw materials for a catalyst are mixed with a solvent to form a catalyst composition(S1); the catalyst composition is kneaded to form a catalytic clay(S2); the catalytic clay is extrusion-molded into a honeycomb molded body(S3); and the honeycomb molded body is coated with a co-catalyst solution(S4). The tungsten precursor includes at least one selected from a group including ammonium metatungstate, ammonium paratungstate, and tungstic acid. The raw materials for the catalyst include a carrier and catalyst activating components. The carrier includes titanium dioxide. The catalyst activating components are selected from one or more metals with denitrification activity, oxides of the metals, salts of the metals, or a mixture of the same. [Reference numerals] (AA) Start; (BB) End; (S1) Forming a catalyst composition by mixing raw materials for a catalyst with a solvent; (S2) Forming catalytic clay by kneading the catalyst composition; (S3) Extrusion-molding the catalytic clay into a honeycomb molded body; (S4) Coating the honeycomb molded body with a co-catalyst solution; (S5) Forming a honeycomb catalyst by plasticization
    • 目的:提供一种蜂窝状催化剂的制造方法,通过形成和挤出催化剂粘土来形成蜂窝成型体,并且在蜂窝成型体上均匀地涂布含有钨前体的助催化剂溶液,从而降低生产成本,提高脱氮效率 使用浸涂工艺。 构成:蜂窝状催化剂的制造方法包括以下步骤:将催化剂原料与溶剂混合,形成催化剂组合物(S1); 将催化剂组合物捏合以形成催化粘土(S2); 将催化性粘土挤出成型为蜂窝成型体(S3); 并且蜂窝成型体涂有助催化剂溶液(S4)。 钨前体包括选自偏钨酸铵,仲钨酸铵和钨酸中的至少一种。 催化剂的原料包括载体和催化剂活化组分。 载体包括二氧化钛。 催化剂活化组分选自具有脱氮活性的一种或多种金属,金属的氧化物,金属的盐或其混合物。 (附图标记)(AA)开始; (BB)结束; (S1)通过将催化剂的原料与溶剂混合形成催化剂组合物; (S2)捏合催化剂组合物形成催化剂粘土; (S3)将催化性粘土挤出成型为蜂窝成型体; (S4)用助催化剂溶液涂布蜂窝成型体; (S5)通过增塑形成蜂窝催化剂
    • 23. 发明公开
    • 탈질효율 측정 방법 및 탈질효율 측정 장치
    • 测量SCR转换效率的方法和装置
    • KR1020120107551A
    • 2012-10-04
    • KR1020110025111
    • 2011-03-22
    • 주식회사 나노
    • 신동우박삼식유상희천혜연
    • G01N31/10F01N3/20F01N11/00B01D53/94
    • Y02T10/47G01N31/10B01J19/0053B01J19/1812
    • PURPOSE: A denitrification efficiency measuring method and an apparatus for the same are provided to secure reliable measured results and to shorten the time required for measurement. CONSTITUTION: A denitrification efficiency measuring method includes the following: at least two exhaust gases are firstly mixed(S100); the mixed exhaust gases are pre-heated at a temperature more than or equal to 200 deg. C(S110); the mixed exhaust gases are secondly mixed with reducing gas(S120); the gas mixture is reacted with a reducing catalyst(S130); and reacted gas is analyzed to measure the efficiency of the reducing catalyst(S140). [Reference numerals] (AA) Start; (BB) End; (S100) Primarily mixing at least two exhaust gases; (S110) Pre-heating the mixed exhaust gases; (S120) Secondarily mixing the mixed exhaust gases with reducing agent gas; (S130) Reacting the mixed gases with a reducing catalyst; (S140) Measuring the efficiency of the reducing catalyst by analyzing reactive gas
    • 目的:提供脱氮效率测定方法及其设备,以确保可靠的测量结果并缩短测量所需的时间。 构成:脱氮效率测定方法包括:首先混合至少两种废气(S100); 混合废气在大于或等于200度的温度下被预热。 C(S110); 混合废气二次与还原气体混合(S120); 气体混合物与还原催化剂反应(S130); 并分析反应气体以测量还原催化剂的效率(S140)。 (附图标记)(AA)开始; (BB)结束; (S100)主要混合至少两种废气; (S110)预混合排气; (S120)二次混合废气与还原剂气体混合; (S130)用还原催化剂反应混合气体; (S140)通过分析反应气体来测定还原催化剂的效率
    • 25. 发明公开
    • 고체윤활제를 함유하는 고온 내마모성 그리이스 조성물
    • 润滑脂组合物具有严酷的温度条件和包含固体润滑剂的耐磨性
    • KR1020020075958A
    • 2002-10-09
    • KR1020010015654
    • 2001-03-26
    • 주식회사 나노
    • 신동우윤대현
    • C10M125/22
    • PURPOSE: Provided is a grease composition having wearing resistance under severe temperature condition, particularly ultra high or ultra low temperature and containing a solid lubricant. CONSTITUTION: The grease composition contains 60 to 99 wt.% of grease and 0.1 to 40 wt.% of solid lubricant having a diameter of 1 to 50 micrometer, which is particularly a dichalcogenide solid lubricant and is produced by mixing at least a transition metal selected from the group consisting of tungsten(W), molybdenum(Mo), niobium(Nb), thallium(Ta), titanium(Ti), vanadium(V) and chromium(Cr) with at least a group 6A metal selected from the group consisting of sulfur(S), selenium(Se) and tellurium (Te) in a mole ratio of 1:2.2 to 1:3.0, and heating the mixture at 800 to 1000 deg. C for 2 hours or less.
    • 目的:提供在严酷的温度条件下,特别是超高温或超低温下具有耐磨性并含有固体润滑剂的润滑脂组合物。 组成:润滑脂组合物含有60至99重量%的润滑脂和0.1至40重量%的直径为1至50微米的固体润滑剂,特别是二硫属化物固体润滑剂,并且通过将至少一种过渡金属 选自由钨(W),钼(Mo),铌(Nb),铊(Ta),钛(Ti),钒(V)和铬(Cr)组成的组, 由硫(S),硒(Se)和碲(Te)组成的组,摩尔比为1:2.2至1:3.0,并将混合物加热至800至1000℃。 C 2小时以下。
    • 26. 发明公开
    • 세라믹스 촉매 담체의 제조 방법
    • 陶瓷催化剂支撑剂的制备方法
    • KR1020020007021A
    • 2002-01-26
    • KR1020000040686
    • 2000-07-14
    • 주식회사 나노
    • 신동우곽해박삼식
    • B01J37/08
    • B01J37/0018B01J37/08
    • PURPOSE: A method for fabricating ceramic catalyst supporter that is applicable to commercial scale with reduced crack is provided. CONSTITUTION: The method comprises the step of (i) dry-mixing 1-10wt.% (based on the weight of raw material) of either methyl cellulose or carboxymethyl cellulose with one raw material selected from the group consisting of zeolite, γ-Al2O3, MnO2, TiO2, V2O3, WO3 and silica glass fiber; (ii) addition of 20-50wt.% water and 2-8wt.% plasticizer, based on the weight of raw material; (iii) aging the mixture under restrict moisture evaporation followed by shaping; (iv) drying the obtained monolithic catalyst in the temperature range 60 to 120deg.C for 5-20hrs; and then (v) heat treatment of the monolithic catalyst in the temperature range 400 to 500deg.C for 3-7hrs. In the second step, additionally, polyoxy ethylene octylene phenylether is added, wherein an amount of water to be added in raw material is 16-30wt.% based on the weight of raw material and an amount of polyoxy ethylene octylene phenylether to be added in raw material is 0.1-2wt.% based on the weight of the water.
    • 目的:提供一种适用于具有减少裂纹的商业规模的陶瓷催化剂载体的制备方法。 方法:该方法包括以下步骤:(i)将一种原料选自沸石,γ-Al 2 O 3,干粉混合1-10重量%(基于原料重量)的甲基纤维素或羧甲基纤维素 ,MnO 2,TiO 2,V 2 O 3,WO 3和石英玻璃纤维; (ii)基于原料的重量加入20-50重量%的水和2-8重量%的增塑剂; (iii)在限制水分蒸发下熟化混合物,然后成型; (iv)将得到的整体催化剂在60〜120℃的温度范围内干燥5-20小时; 然后(v)在400〜500℃的温度范围内对整体式催化剂进行热处理3-7小时。 此外,在第二工序中,添加聚氧乙烯亚辛基苯基醚,其中原料中添加的水的量相对于原料的重量为16〜30重量%,加入的聚氧乙烯亚辛基苯基醚的量为 原料为0.1-2重量%,基于水的重量。
    • 27. 发明公开
    • 아미노산 수용액을 이용한 세라믹스 성형 방법 및 장치
    • 使用氨基酸溶液和装置的陶瓷成型方法
    • KR1020010077621A
    • 2001-08-20
    • KR1020000005529
    • 2000-02-03
    • 주식회사 나노
    • 신동우윤대현박삼식곽해
    • C04B35/00C04B35/632
    • B28C5/006B28B1/14C04B35/632
    • PURPOSE: A ceramics forming method using aqueous amino acid solution is provided which enables to form large-sized ceramics with complicated shapes due to high forming density and forming strength. CONSTITUTION: The forming method comprises the steps of: preparing each slurry by adding ceramic powder, such as, oxide(Al2O3, SiC, Si3N4, etc.) or non-oxide, to 2-10wt.% of amino acid solution and 0.5-1.5wt.% of hardening agent in one(5a) and the other(5b) of a first stirring vessel, respectively, and dispersing each slurry by adding dispersant less than 1wt.%; mixing together at 60-90deg.C in a second stirring vessel; defoaming; casting.
    • 目的:提供一种使用含水氨基酸溶液的陶瓷形成方法,由于其高的成形密度和成形强度,能够形成具有复杂形状的大尺寸陶瓷。 构成:成型方法包括以下步骤:通过将氧化物(Al 2 O 3,SiC,Si 3 N 4等)或非氧化物等陶瓷粉末加入2-10重量%的氨基酸溶液和0.5〜 分别在第一搅拌容器的一个(5a)和另一个(5b)中的硬化剂为1.5重量%,并通过加入小于1重量%的分散剂分散每个浆料; 在60-90℃下在第二搅拌容器中混合; 消泡; 铸件。