디올레핀류 화합물의 선택적 수소화 반응을 위한 수식된니켈-알루미나계 촉매와 그 제조방법
    81.
    发明公开
    디올레핀류 화합물의 선택적 수소화 반응을 위한 수식된니켈-알루미나계 촉매와 그 제조방법 失效
    用于选择性加氢二烯的改性镍 - 镍氧化物催化剂及其制备方法

    公开(公告)号:KR1020020061434A

    公开(公告)日:2002-07-24

    申请号:KR1020010002734

    申请日:2001-01-17

    Abstract: PURPOSE: The modified nickel-alumina catalyst for selective hydrogenation of diolefins of the present invention is manufactured by surface modifying gamma-alumina support with one element selected from zirconium, lanthanum and tin, and then it is further supported by nickel. CONSTITUTION: In a modified nickel-alumina catalyst for selective hydrogenation of diolefins that is manufactured by surface modifying gamma-alumina support with one element selected from zirconium, lanthanum and tin, and then it is further supported by nickel, the present invention is characterized in that gamma-alumina support is supported by one element selected from zirconium, lanthanum and tin in an amount of 0.2 to 10 wt.% and nickel in an amount of 0.5 to 10 wt.%, based on the weight of the gamma-alumina support. Before the modified nickel-alumina catalyst is used to convert diolefins to corresponding mono olefins through selective hydrogenation reaction, the modified nickel-alumina catalyst should undergo reduction stage at 400-500deg.C and pretreatment at 300-450deg.C in H2S gas atmosphere.

    Abstract translation: 目的:本发明二烯烃选择性氢化的改性镍 - 氧化铝催化剂是通过用选自锆,镧和锡的一种元素表面改性γ-氧化铝载体,然后进一步由镍负载制备的。 构成:在通过用选自锆,镧和锡的一种元素表面改性γ-氧化铝载体制备的二烯烃选择性氢化的改性镍 - 氧化铝催化剂中,然后进一步由镍负载,本发明的特征在于 该γ-氧化铝载体由选自锆,镧和锡的一种元素以0.2至10重量%的量负载,镍的量为0.5至10重量%,基于γ-氧化铝载体的重量 。 在通过选择性氢化反应将改性镍 - 氧化铝催化剂用于将二烯烃转化为相应的单烯烃之前,改性镍 - 氧化铝催化剂应在400-500℃下进行还原阶段,并在H 2 S气体气氛中在300-450℃下进行预处理。

    휘발성 유기염소화합물 제거용 산화촉매
    82.
    发明公开
    휘발성 유기염소화합물 제거용 산화촉매 失效
    用于去除氯化挥发性有机化合物的多功能氧化催化剂

    公开(公告)号:KR1020020060002A

    公开(公告)日:2002-07-16

    申请号:KR1020010001198

    申请日:2001-01-09

    CPC classification number: B01J27/053 B01J29/126 B01J29/146 B01J29/48

    Abstract: PURPOSE: Provided is a multifunctional oxidation catalysts, which can remove chlorinated volatile organic compounds at low temperatures of 20 to 220°C as well as minimize generation of another forms of chlorinated volatile organic compounds after reaction. CONSTITUTION: The present invention is characterized in that sulfated metal oxide support is impregnated with (i) as active species, 0.5-2.0 wt.% of one novel metal selected from Pt, Pd, Ir and Rh; (ii) as subsidiary active species, Cu 2.0-10.0 wt.%, Ni 0.1-1.0 wt.%. The sulfated metal oxide support is selected from zirconia, titania and ceria containing SO4 in an amount of 0.3 to 2.3 wt.%. And a porous molecular sieve material is used as support, together with the sulfated metal oxide support within the range of less than 50%. The porous molecular sieve material, such as protonic zeolite or ammonium zeolite, is selected from BEA, MFI, MOR and FAU zeolite with a Si/Al ratio within the range of 10 to 100.

    Abstract translation: 目的:提供一种多功能氧化催化剂,可在20〜220℃的低温下除去氯化挥发性有机化合物,并使反应后产生其他形式的氯化挥发性有机化合物最小化。 构成:本发明的特征在于硫酸化金属氧化物载体浸渍有(i)作为活性物质,选自Pt,Pd,Ir和Rh的一种新型金属为0.5-2.0重量% (ii)作为辅助活性物质,Cu 2.0-10.0重量%,Ni 0.1-1.0重量%。 硫酸化金属氧化物载体选自氧化锆,二氧化钛和含有SO 3的二氧化铈,其量为0.3至2.3重量%。 使用多孔分子筛材料作为载体,硫酸化金属氧化物载体在小于50%的范围内。 多孔分子筛材料,例如质子沸石或铵沸石,选自BEA,MFI,MOR和FAU沸石,Si / Al比在10至100的范围内。

    휘발성 유기화합물 제거용 하니컴형 일체식 촉매의 제조방법
    83.
    发明授权
    휘발성 유기화합물 제거용 하니컴형 일체식 촉매의 제조방법 失效
    一种制备蜂窝状整体式催化剂的方法

    公开(公告)号:KR100336967B1

    公开(公告)日:2002-05-17

    申请号:KR1019990045621

    申请日:1999-10-20

    Abstract: 본발명은휘발성유기화합물제거용하니컴형일체식촉매의제조방법에관한것으로서, 더욱상세하게는팔라듐이온(Pd)과전이금속이온을함유한금속염을제올라이트와같은다공성담체에담지시켜서만들어진촉매분말을소정의바인더와배합하여슬러리형태로제조한후, 이를하니컴형담체표면에습윤코팅하여제조한것으로화학산업의생산과정에서발생하는배가스중의휘발성유기화합물을저온완전연소시켜제거하는데유용한하니컴형일체식촉매의제조방법에관한것이다.

    휘발성 유기화합물 제거용 하니컴형 일체식 촉매
    84.
    发明授权
    휘발성 유기화합물 제거용 하니컴형 일체식 촉매 失效
    用于去除VOC的蜂窝型整体式催化剂

    公开(公告)号:KR100336963B1

    公开(公告)日:2002-05-17

    申请号:KR1020010003268

    申请日:2001-01-19

    Abstract: 본발명은휘발성유기화합물제거용하니컴형일체식촉매에관한것으로서, 더욱상세하게는팔라듐이온(Pd)과전이금속이온을함유한금속염을제올라이트와같은다공성담체에담지시켜서만들어진촉매분말을소정의바인더와배합하여슬러리형태로제조한후, 이를하니컴형담체표면에습윤코팅하여제조한것으로화학산업의생산과정에서발생하는배가스중의휘발성유기화합물을저온완전연소시켜제거하는데유용한하니컴형일체식촉매에관한것이다.

    수소와 산소에 의한 직접적 수산화 방향족 화합물의 제조방법
    85.
    发明公开
    수소와 산소에 의한 직접적 수산화 방향족 화합물의 제조방법 失效
    用氢氧化合物制备羟基芳族化合物的方法

    公开(公告)号:KR1020000001930A

    公开(公告)日:2000-01-15

    申请号:KR1019980022415

    申请日:1998-06-15

    CPC classification number: C07C37/58 Y02P20/52 C07C39/04

    Abstract: PURPOSE: Title compounds are directly prepared by hydrogen and oxygen, not using perhydroxide in the presence of binary catalyst. CONSTITUTION: Title compounds are prepared by hydrogen and oxygen at -10- 60°C, atmospheric pressure in the presence of binary catalyst comprising zeolite catalyst including VIII-B transition metals and alkyl anthraquinone derivatives and zeolite catalyst containing the transition metal having tetrahedron coordinated structures. Thus, 15 ml benzene and 15 ml acetic acid are mixed in the velocity of 16 ml/min of hydrogen and oxygen at 60°C for 5 hours to give a phenol.

    Abstract translation: 目的:标题化合物直接由氢和氧制备,在二元催化剂存在下不使用全氢氧化物。 构成:标题化合物是在氢气和氧气的制备下,在-10〜60℃,大气压下,在二元催化剂存在下,包含沸石催化剂,包括VIII-B过渡金属和烷基蒽醌衍生物,以及含有具有四面体配位结构的过渡金属的沸石催化剂 。 因此,将15ml苯和15ml乙酸以16ml / min的氢气和氧气的速度在60℃下混合5小时,得到苯酚。

    고분산 혼합 금속산화물 담지 촉매의 제조방법
    86.
    发明公开
    고분산 혼합 금속산화물 담지 촉매의 제조방법 失效
    生产高分散混合金属氧化物负载型催化剂的方法

    公开(公告)号:KR1019970014833A

    公开(公告)日:1997-04-28

    申请号:KR1019950028862

    申请日:1995-09-05

    Abstract: 본 발명은 성분금속염에 유기산과 디히드록시 알콜 화합물을 첨가하여 얻어진 금속착염용액에 고표면적을 갖는 알루미늄 및 실리콘 함유 담체를 첨가하여 상온에서 액상으로 혼합하고 이를 70~150℃에서 감압증류 및 극초단파를 이용, 건조하여 겔화시킨 후에 300~700℃의 소성온도에서 열처리하여 혼합 금속산화물이 무정형으로 또 고표면적으로 담체에 균일하게 분산되어 있는 하기 식(Ⅰ)으로 표시되는 질소 산화물 제거 및 탄화수소 연소화반응에 촉매활성이 있는 혼합 금속산화물 담지촉매의 제조방법 :
    (A
    a O
    x ·B
    b O
    y )·(C
    c O
    z ·C'
    c' O
    Z' )/S (Ⅰ)
    상기 식에서, A와 B는 란탄계열 금속 또는 알칼리금속 또는 알카리토금속이고, C와 C
    ' 는 제1주기 전이금속 또는 귀금속이고, a, b, c 및 c
    ' 는 양론적으로 0 내지 1의 값을 가지며, a+b=1, c+c
    ' =1이고 또〔a+b〕대 〔c+c
    ' 〕의 비율은 0.1~3.0:1.0의 범위이고, S는 제올라이트, 알루미나, 실리카, 알루미나-실리카 등의 알루미늄 및/또는 실리콘 함유 담체에 관한 것이다.

    이산화탄소로 부터 합성가스의 제조방법
    88.
    发明授权
    이산화탄소로 부터 합성가스의 제조방법 失效
    二氧化碳合成气的制备工艺

    公开(公告)号:KR1019960009892B1

    公开(公告)日:1996-07-24

    申请号:KR1019930016885

    申请日:1993-08-25

    CPC classification number: B01J23/78 C01B3/40 C01B2203/1052 Y02P20/52

    Abstract: Synthetic gas is prepared by continuously reacting carbon dioxide with low grade hydrocarbon or natural gas containing methane and oxygen or steam in a mole ratio of 2:1-5:1 in the presence of a catalyst that comprises nickel, alkali and alkali earth metals supported on silicone such as zeolite, silica, silicate or silica-alumina at 600-1,000deg.C and 0.5-20 atms and a space velocity of 1,000-500,000. The ratio of carbon monoxide to hydrogen in the synthetic gas is 1:2-2:1.

    Abstract translation: 在催化剂存在下,使二氧化碳与含有甲烷和氧气或蒸汽的摩尔比为2:1-5:1的低级烃或天然气连续反应制备合成气体,所述催化剂包含负载的镍,碱和碱土金属 在600-1000℃,0.5-20atms,空间速度为1000-500,000的硅氧烷如沸石,二氧化硅,硅酸盐或二氧化硅 - 氧化铝上。 合成气中一氧化碳与氢的比例为1:2.2:1。

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