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    • 1. 发明授权
    • Metal-exchanged carboxylato-alumoxanes and process of making metal-doped alumina
    • 金属交换的羧基铝氧烷和制备金属掺杂氧化铝的方法
    • US06207130B1
    • 2001-03-27
    • US09058587
    • 1998-04-10
    • Aivaras KareivaChuansheng BaiCharles Jeffrey HarlanD. Brent MacQueenAndrew R. BarronRonald L. Cook
    • Aivaras KareivaChuansheng BaiCharles Jeffrey HarlanD. Brent MacQueenAndrew R. BarronRonald L. Cook
    • C01F702
    • C01F7/002B82Y30/00C01F7/04C01F7/16C01F7/30C01F17/0025C01G1/00C01G45/006C01G51/006C01P2002/32C01P2002/34C01P2002/52C01P2002/54C01P2004/64C07F5/069C07F15/025C07F15/045C07F15/065
    • A method has been developed for the solution-based metal exchange of carboxylato-alumoxanes [Al(O)x(OH)y(O2CR)z]n with a wide range of metal cations. Metal-exchanged carboxylato-alumoxanes are new, particularly those in which about 10% to about 50% or more of the Al ions are exchanged for other metal ions. Additionally, the carboxylic acid ligands can be stripped from the boehmite core of metal-exchanged carboxylato-alumoxanes at low temperature leading to the formation of metal-exchanged boebmite particles. These new material phases can be used as intermediates for preparation of mixed metal aluminum oxide materials. Thermolysis of the metal-exchanged carboxylato-alumoxanes or metal-exchanged boehmite particles results in doped aluminas (M/Al2O3), binary (MAlOx), ternary (MM′AlOx) and even more complex metal aluminum oxide compounds, where M and M′ are metal ions other than those of aluminum and are preferably those of Lanthanide metals or transition metals. The method allows preparation of pure phase materials as well as the preparation of metastable metal aluminum oxide phases. The carboxylato-alumoxanes are prepared by the reaction of boehmite (or pseudoboehmite) with carboxylic acids in a suitable solvent. Up to at least half of the aluminum cations in the boehmite lattice of the carboxylato-alumoxanes can be replaced by the reaction of metal acetylacetonates with the carboxylato-alumoxane in a suitable solvent. The metal exchange reaction can also be carried out by reaction with soluble metal salts. Reactions of boehmite with the metal acetylacetonates (or soluble metal salts) do not lead to the metal exchange reaction observed for the carboxylato-alumoxanes.
    • 已经开发了用于宽范围的金属阳离子的羧基 - 铝氧烷[Al(O)x(OH)y(O 2 CR)z] n的基于溶液的金属交换的方法。 金属交换的羧基铝氧烷是新的,特别是其中约10%至约50%或更多的Al离子被交换为其它金属离子的那些。 此外,羧酸配体可以在低温下从金属交换的羧酸 - 铝氧烷的勃姆石芯中汽提,导致形成金属交换的勃姆沸石颗粒。 这些新材料相可以用作制备混合金属氧化铝材料的中间体。 金属交换的羧酸 - 铝氧烷或金属交换的勃姆石颗粒的热解导致掺杂的氧化铝(M / Al 2 O 3),二元(MA 1 O x),三元(MM'AlO x)和甚至更复杂的金属氧化铝化合物,其中M和M' 是除铝以外的金属离子,优选为镧系金属或过渡金属的金属离子。 该方法允许制备纯相材料以及制备亚稳态金属氧化铝相。 羧基铝氧烷通过勃姆石(或假勃姆石)与羧酸在合适溶剂中的反应来制备。 羧酸 - 铝氧烷的勃姆石晶格中的至少一半的铝阳离子可以通过金属乙酰丙酮化物与羧基 - 铝氧烷在合适的溶剂中的反应来代替。 金属交换反应也可以通过与可溶性金属盐反应来进行。 勃姆石与金属乙酰丙酮化物(或可溶性金属盐)的反应不会导致对羧基铝氧烷观察到的金属交换反应。
    • 3. 发明申请
    • Hydrocracker post-treat catalyst for production of low sulfur fuels
    • 用于生产低硫燃料的加氢裂化器后处理催化剂
    • US20070278135A1
    • 2007-12-06
    • US11446251
    • 2006-06-02
    • William J. TracyChuansheng BaiRobert A. BradwayWilliam E. LewisRandolph J. Smiley
    • William J. TracyChuansheng BaiRobert A. BradwayWilliam E. LewisRandolph J. Smiley
    • C10G65/00C10G69/00
    • C10G65/12B01J23/883B01J23/8885B01J31/10C10G45/08
    • A hydrocracking process for converting a petroleum feedstock to higher gravity, lower sulfur products, especially ultra low sulfur road diesel fuel. The process may be operated as a single-stage or two-stage hydrocracking. In each case, a hydrocracking step is followed directly by a post-treat hydrodesulfurization zone using a bulk multimetallic catalyst comprised of at least one Group VIII non-noble metal and at least two Group VIB metals with a ratio of Group VIB metal to Group VIII non-noble metal is from about 10:1 to about 1:10. In the two-stage option with interstage ammonia removal, the initial hydrocracking step may be followed by hydrodesulfurization using the bulk multimetallic catalyst prior to the ammonia removal which is followed by the second hydrocracking step. A final hydrodesulfurization over the bulk multimetallic catalyst may follow. The hydrodesulfurization over the bulk multimetallic catalyst is carried out at a pressure of at least 25 barg and preferably at least 40 barg.
    • 用于将石油原料转化为更高重力,较低硫产物,特别是超低硫道路柴油的加氢裂化方法。 该方法可以作为单级或两级加氢裂化操作。 在每种情况下,加氢裂化步骤直接通过后处理加氢脱硫区,使用由至少一种VIII族非贵金属和至少两种VIB族金属与VIII族的VIB族金属组成的本体多金属催化剂 非贵金属为约10:1至约1:10。 在阶段氨除去的两阶段选择中,初始加氢裂化步骤之后可以在除氨之前使用大量多金属催化剂进行加氢脱硫,其后是第二加氢裂化步骤。 可以遵循大量多金属催化剂的最终加氢脱硫。 本体多金属催化剂上的加氢脱硫在至少25barg,优选至少40barg的压力下进行。
    • 8. 发明授权
    • Catalysts for the selective oxidation of hydrogen sulfide to sulfur
    • 用于将硫化氢选择性氧化成硫的催化剂
    • US6099819A
    • 2000-08-08
    • US234367
    • 1999-01-20
    • Girish SrinivasChuansheng Bai
    • Girish SrinivasChuansheng Bai
    • B01D53/86B01J21/06B01J23/00C01B17/04B01D53/52
    • B01J21/063B01D53/8612B01J23/00C01B17/0465Y10S502/514
    • This invention provides catalysts for the oxidation of hydrogen sulfide. In particular, the invention provides catalysts for the partial oxidation of hydrogen sulfide to elemental sulfur and water. The catalytically active component of the catalyst comprises a mixture of metal oxides containing titanium oxide and one or more metal oxides which can be selected from the group of metal oxides or mixtures of metal oxides of transition metals or lanthanide metals. Preferred metal oxides for combination with TiO.sub.2 in the catalysts of this invention include oxides of V, Cr, Mn, Fe, Co, Ni, Cu, Nb, Mo, Tc, Ru, Rh, Hf, Ta, W, Au, La, Ce, Pr, Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, and Lu. Catalysts which comprise a homogeneous mixture of titanium oxide and niobium (Nb) oxide are also provided. A preferred method for preparing the precursor homogenous mixture of metal hydroxides is by coprecipitation of titanium hydroxide with one or more other selected metal hydroxides. Catalysts of this invention have improved activity and/or selectivity for elemental sulfur production. Further improvements of activity and/or selectivity can be obtained by introducing relatively low amounts (up to about 5 mol %)of a promoter metal oxide (preferably of metals other than titanium and that of the selected second metal oxide) into the homogeneous metal/titanium oxide catalysts of this invention.
    • 本发明提供用于硫化氢氧化的催化剂。 特别地,本发明提供了用于将硫化氢部分氧化成元素硫和水的催化剂。 催化剂的催化活性组分包括含有氧化钛和一种或多种金属氧化物的金属氧化物的混合物,其可以选自金属氧化物或过渡金属或镧系金属的金属氧化物的混合物。 本发明催化剂中与TiO 2组合的优选金属氧化物包括V,Cr,Mn,Fe,Co,Ni,Cu,Nb,Mo,Tc,Ru,Rh,Hf,Ta,W,Au,La, Ce,Pr,Nd,Pm,Sm,Eu,Gd,Tb,Dy,Ho,Er,Tm,Yb和Lu。 还提供了包含氧化钛和铌(Nb)氧化物的均匀混合物的催化剂。 用于制备金属氢氧化物的前体均匀混合物的优选方法是通过氢氧化钛与一种或多种其它选择的金属氢氧化物的共沉淀。 本发明的催化剂具有改善元素硫生产的活性和/或选择性。 活性和/或选择性的进一步改善可以通过将相对低量(最多约5mol%)的助催化剂金属氧化物(优选不同于钛的金属和所选择的第二金属氧化物)引入均质金属/ 本发明的氧化钛催化剂。