Catalyst for dehydrogenating aromatic with carbon dioxide
    4.
    发明授权
    Catalyst for dehydrogenating aromatic with carbon dioxide 失效
    用二氧化碳使芳香族脱氢的催化剂

    公开(公告)号:US6037511A

    公开(公告)日:2000-03-14

    申请号:US265359

    申请日:1999-03-10

    CPC classification number: C07C5/322 C07C5/3332 C07C2523/745 Y02P20/582

    Abstract: The invention herein relates to a catalyst for enhancing the conversion of the dehydrogenation reaction of aromatic hydrocarbons such as ethylbenzene under a flow of carbon dioxide, which is expressed by the following formula I, wherein a catalyst in which an active component of iron oxides is highly dispersed onto a zeolite, activated charcoal, .gamma.-alumina or silica carrier. Further, the invention relates to a dehydrogenation method of aromatic hydrocarbons by means of using said catalyst:(Fe.sup.II.sub.x Fe.sup.III.sub.y O.sub.z)/S (I)wherein S denotes a zeolite, activated charcoal, .gamma.-alumina or silica carrier, and the initial state of iron oxide is as follows:x=0.1-2 x+y=3and z=(2x+3y)/2As compared to the case in which the reaction is carried out without carbon dioxide, the invention herein is characterized by the significant enhancement of the activity of the dehydrogenation reaction of aromatic hydrocarbons in conjunction with the catalytic stability under a flow of carbon dioxide in the reaction temperature range of 500.about.700.degree. C. In particular, the invention provides a method of enhancing the dehydrogenation activity, wherein a catalyst is used, in which having a carrier such as a zeolite, active carbon, .gamma.-alumina or silica is loaded with iron oxides containing a high concentration of Fe(II) species.

    Abstract translation: 本发明涉及一种催化剂,其用于增强在二氧化碳流下的芳烃如乙苯的脱氢反应的转化,其由下式I表示,其中,其中氧化铁的活性组分是高度的 分散在沸石,活性炭,γ-氧化铝或二氧化硅载体上。 此外,本发明涉及通过使用所述催化剂的芳烃的脱氢方法:(FeIIxFeIIIyOz)/ S(I)其中S表示沸石,活性炭,γ-氧化铝或二氧化硅载体,以及氧化铁的初始状态 如下:与没有二氧化碳进行反应的情况相比,x = 0.1-2×+ y = 3和z =(2x + 3y)/ 2As),本发明的特征在于活性的显着提高 的芳烃的脱氢反应以及在二氧化碳流动下在700℃的反应温度范围内的催化稳定性。特别地,本发明提供一种提高脱氢活性的方法,其中使用催化剂 ,其中具有诸如沸石,活性炭,γ-氧化铝或二氧化硅的载体载有含有高浓度Fe(II)物质的氧化铁。

    Catalyst for dehydrogenating aromatic hydrocarbons with carbon dioxide
    5.
    发明授权
    Catalyst for dehydrogenating aromatic hydrocarbons with carbon dioxide 失效
    用二氧化碳使芳烃脱氢的催化剂

    公开(公告)号:US6034032A

    公开(公告)日:2000-03-07

    申请号:US163350

    申请日:1998-09-30

    Abstract: The invention herein relates to a catalyst for enhancing the conversion of the dehydrogenation reaction of aromatic hydrocarbons such as ethylbenzene under a flow of carbon dioxide, which is expressed by the following formula I, wherein a catalyst in which an active component of iron oxides is highly dispersed onto a zeolite, activated charcoal, .gamma.-alumina or silica carrier. Further, the invention relates to a dehydrogenation method of aromatic hydrocarbons by means of using said catalyst:(Fe.sup.II.sub.x Fe.sup.III.sub.y O.sub.z)/S (I)wherein S denotes a zeolite, activated charcoal, .gamma.-alumina or silica carrier, and the initial state of iron oxide is as follows:x=0.1-2, x+y=3 and z=(2x+3y)/2As compared to the case in which the reaction is carried out without carbon dioxide, the invention herein is characterized by the significant enhancement of the activity of the dehydrogenation reaction of aromatic hydrocarbons in conjunction with the catalytic stability under a flow of carbon dioxide in the reaction temperature range of 500.about.700.degree. C. In particular, the invention provides a method of enhancing the dehydrogenation activity, wherein a catalyst is used, in which having a carrier such as a zeolite, active carbon, .gamma.-alumina or silica is loaded with iron oxides containing a high concentration of Fe(II) species.

    Abstract translation: 本发明涉及一种催化剂,其用于增强在二氧化碳流下的芳烃如乙苯的脱氢反应的转化,其由下式I表示,其中,其中氧化铁的活性组分是高度的 分散在沸石,活性炭,γ-氧化铝或二氧化硅载体上。 此外,本发明涉及通过使用所述催化剂的芳烃的脱氢方法:(FeIIxFeIIIyOz)/ S(I)其中S表示沸石,活性炭,γ-氧化铝或二氧化硅载体,以及氧化铁的初始状态 如下:x = 0.1-2,x + y = 3,z =(2x + 3y)/ 2与没有二氧化碳进行反应的情况相比,本发明的特征在于显着增强 的芳烃的脱氢反应的活性与在二氧化碳流动下的催化稳定性在500-6,000℃的反应温度范围内。特别地,本发明提供了一种增强脱氢活性的方法,其中a 使用其中具有载体如沸石,活性炭,γ-氧化铝或二氧化硅的催化剂负载含有高浓度Fe(II)物质的氧化铁。

    Method for preparing noble metal-supported zeolite catalyst for catalytic reduction of nitrogen oxide
    9.
    发明授权
    Method for preparing noble metal-supported zeolite catalyst for catalytic reduction of nitrogen oxide 失效
    制备用于氮氧化物催化还原的贵金属负载的沸石催化剂的方法

    公开(公告)号:US06528031B1

    公开(公告)日:2003-03-04

    申请号:US09476238

    申请日:1999-12-30

    Abstract: The present invention provides a method for preparing a catalyst for the reduction of nitrogen oxides by the use of natural gas as a reducing agent in an excess oxygen atmosphere, which comprises of filling zeolite with an organic compound having molecular weight of 100˜250 prior to loading catalytically active noble metal components on a zeolite. Since the method according to the present invention supports catalytic active noble metal components on a zeolite under the condition that the pores of zeolite are filled with organic compounds, the noble metal component, which is essential for forming highly active NOx reduction catalyst, can be supported precisely on the desired positions of zeolite pores. Therefore, the NOx reduction catalysts prepared by the present invention are very useful for the purification of exhaust gas in an excessive oxygen atmosphere such as gas turbines, boilers or lean-burn automobiles.

    Abstract translation: 本发明提供一种制备用于在过量氧气氛中使用天然气作为还原剂还原氮氧化物的催化剂的方法,其包括在分子量为100〜250之前将沸石与分子量为100〜250的有机化合物进行填充, 在沸石上加载催化活性的贵金属组分。 由于根据本发明的方法在沸石的孔填充有机化合物的条件下在沸石上支持催化活性贵金属组分,因此可以支持对形成高活性NOx还原催化剂至关重要的贵金属组分 精确地在沸石孔的所需位置。 因此,本发明制备的NOx还原催化剂对于在诸如燃气轮机,锅炉或贫燃汽车的过氧气氛中净化废气非常有用。

    Process for preparing hydroxylated aromatics by hydrogen and oxygen
    10.
    发明授权
    Process for preparing hydroxylated aromatics by hydrogen and oxygen 失效
    通过氢气和氧气制备羟基化芳烃的方法

    公开(公告)号:US06191318B1

    公开(公告)日:2001-02-20

    申请号:US09332135

    申请日:1999-06-14

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

    Abstract: The present invention relates to a process for preparing hydroxylated aromatics by using hydrogen and oxygen and more particularly, to a process for preparing hydroxylated aromatics by using hydrogen and oxygen with a two-component heterogeneous catalyst. One component consists of porous catalyst containing one of Group VIII B transition metals such as Pd, Pt, Au and Cu, and hydrogen transfer organic compounds such as anthraquinone. The other component consists of a catalyst containing a transition metal selected from Ti, V, and Sn with tetrahedral coordination geometry. The main advantages of this new catalytic system are to 1) overcome the drawbacks of liquid phase oxidation using conventional homogeneous catalysts, 2) avoid use of expensive hydrogen peroxide as an oxidant, and 3) improve the selectivity of the reaction.

    Abstract translation: 本发明涉及通过使用氢和氧制备羟基化芳族化合物的方法,更具体地说,涉及通过使用氢和氧与双组分多相催化剂制备羟基化芳族化合物的方法。 一种组分由含有ⅧB族过渡金属如Pd,Pt,Au和Cu之一的多孔催化剂和氢转移有机化合物如蒽醌组成。 另一个组分由含有选自Ti,V和Sn的过渡金属和四面体配位几何形状的催化剂组成。 这种新催化体系的主要优点是1)克服使用常规均相催化剂的液相氧化的缺点,2)避免使用昂贵的过氧化氢作为氧化剂,3)提高反应的选择性。

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