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    • 34. 发明申请
    • Spray Process for Selective Oxidation
    • 选择氧化喷涂工艺
    • US20120022287A1
    • 2012-01-26
    • US13258159
    • 2010-03-23
    • Bala SubramaniamDaryle H. BuschFenghul Niu
    • Bala SubramaniamDaryle H. BuschFenghul Niu
    • C07C51/265
    • C07C51/255B01J4/002B01J10/007B01J2219/00006B01J2219/00063B01J2219/00065B01J2219/00162C07C51/265C07C63/00
    • Oxidation process can include: introducing small droplets of liquid reaction mixture having oxidizable reactant, catalyst, and solvent into a reaction zone containing oxygen and diluent gas; and oxidizing the reactant with the oxygen at a suitable reaction temperature and a suitable reaction pressure to produce an oxidized product. The liquid reaction mixture can have an aromatic feedstock having an oxidizable substituent as the oxidizable reactant. The oxidized product can include an aromatic compound having at least one carboxylic acid. For example, the aromatic feedstock can include a benzene ring having at least one oxidizable alkyl substituent, furan hetero-ring having at least one oxidizable alkyl substituent, a naphthalene poly-ring having at least one oxidizable alkyl substituent, derivatives thereof, and mixtures thereof.
    • 氧化过程可以包括:将具有可氧化反应物,催化剂和溶剂的小液滴的液体反应混合物引入含有氧气和稀释气体的反应区; 并在合适的反应温度和合适的反应压力下用氧氧化反应物以产生氧化产物。 液体反应混合物可具有具有可氧化取代基的芳族原料作为可氧化反应物。 氧化产物可以包括具有至少一个羧酸的芳族化合物。 例如,芳族原料可以包括具有至少一个可氧化烷基取代基的苯环,具有至少一个可氧化烷基取代基的呋喃异环,具有至少一个可氧化烷基取代基的萘多环,其衍生物及其混合物 。
    • 35. 发明申请
    • POLYOL HYDROGENOLYSIS BY IN-SITU GENERATED HYDROGEN
    • 多元醇氢原位生成氢
    • US20110004029A1
    • 2011-01-06
    • US12796245
    • 2010-06-08
    • Raghunath V. ChaudhariDebdut S. RoyBala Subramaniam
    • Raghunath V. ChaudhariDebdut S. RoyBala Subramaniam
    • C07C29/60B01J23/42B01J23/46B01J31/02
    • B01J23/462B01J21/04B01J21/18B01J23/6567B01J35/0006C07C29/60C07C31/205
    • A catalyst composition/system can include: a platinum catalyst metal (Pt) and/or rhenium catalyst metal (Re) on a first support; and a ruthenium catalyst metal (Ru) and/or rhenium catalyst metal (Re) on a second support or a platinum catalyst metal (Pt) and a ruthenium catalyst metal (Ru) and/or a rhenium catalyst metal (Re) on the same support. The Pt:Ru, Re:Pt and/or Re:Ru weight ratio can be between about 1:4 and about 4:1. The support can be alumina, carbon, silica, a zeolite, TiO2, ZrO2 or another suitable material. The first and second support can be on the same support structure or on different support structures. In one option, the first and second supports can be positioned such that the Pt and/or Re are capable of catalyzing a dehydrogenation and/or reforming reaction that produces hydrogen and the Ru and/or Re are capable of catalyzing a hydrogenolysis reaction.
    • 催化剂组合物/体系可以包括:在第一载体上的铂催化剂金属(Pt)和/或铼催化剂金属(Re); 以及在第二载体上的铂催化剂金属(Pt)和钌催化剂金属(Ru)和/或铼催化剂金属(Re)上的钌催化剂金属(Ru)和/或铼催化剂金属(Re) 支持。 Pt:Ru,Re:Pt和/或Re:Ru重量比可以在约1:4至约4:1之间。 载体可以是氧化铝,碳,二氧化硅,沸石,TiO 2,ZrO 2或其它合适的材料。 第一和第二支撑件可以在相同的支撑结构上或不同的支撑结构上。 在一个选择中,可以将第一和第二载体定位成使得Pt和/或Re能够催化产生氢的脱氢和/或重整反应,并且Ru和/或Re能够催化氢解反应。