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    • 3. 发明授权
    • Membrane process for the production of hydrogen peroxide by non-hazardous direct oxidation of hydrogen by oxygen using a novel hydrophobic composite Pd-membrane catalyst
    • 使用新的疏水复合Pd膜催化剂通过氧的非危险的直接氧化氧气生产过氧化氢的膜工艺
    • US06432376B1
    • 2002-08-13
    • US09655970
    • 2000-09-05
    • Vasant Ramchandra ChoudharySubhash Dwarkanath SansareAbaji Govind Gaikwad
    • Vasant Ramchandra ChoudharySubhash Dwarkanath SansareAbaji Govind Gaikwad
    • C01B1501
    • B01J31/06B01J23/44B01J35/065B01J2231/70C01B3/501C01B15/029C01B2203/041C01B2203/0495
    • The above objects are achieved by providing a novel process for the production of hydrogen peroxide, by the non-hazardous direct oxidation of hydrogen by oxygen to hydrogen peroxide, without the formation of an explosive H2 and O2 gas mixture, using a novel tubular hydrophobic composite Pd-membrane catalyst, represented by a formula: HPM (c)/SOMF (b)/MxPd1−x(a)/IPM Wherein: IPM is an inorganic porous membrane, permeable to all gases and vapors, in a form of tube having a thickness of at least 0.5 mm and internal diameter of at least 0.6 cm; Mx Pd1−x is a metal alloy, permeable only to hydrogen gas, deposited on the inner side of IPM; Pd is a palladium metal; M is a metal selected from copper, silver, gold, noble metals other than palladium, or a mixture of two or more thereof; x is a mole fraction of the metal M in the metal alloy (MxPd1−x) in the range from about 0.03 to about 0.6; (a) is a weight of the metal alloy per unit area of IPM in the range from about 5.0 g.m−2 to about 500 g.m−2; SOMF is a surface oxidized thin metal film comprising palladium which is permeable only to hydrogen, deposited on the metal alloy (Mx Pd1−x); (b) is a thickness of SOMF in the range from about 0.05 &mgr;m to about 5.0 &mgr;m; HPM is a hydrophobic polymer membrane permeable to hydrogen and oxygen gases and also to vapors of water and hydrogen peroxide but not to liquid water or aqueous solution; and (c) is a weight of the HPM per unit area of SOMF in the range from about 0.2 g.m−2 to about 40 g.m−2.
    • 上述目的通过提供一种用于生产过氧化氢的新方法,通过将氧气由氧气直接氧化成过氧化氢,而不形成爆炸性的H 2和O 2气体混合物,使用新的管状疏水性复合物 Pd膜催化剂,由下式表示:其中:IPM是一种无机多孔膜,可渗透所有气体和蒸汽,其形式为管,其厚度至少为0.5mm,内径为至少0.6cm; Mx Pd1-x是一种金属合金,只能渗透氢气,沉积在IPM的内侧; Pd是钯金属; M是选自铜,银,金,钯以外的贵金属或其两种以上的混合物的金属; x是金属合金(MxPd1-x)中的金属M在约0.03至约0.6的范围内的摩尔分数; (a)是每单位面积IPM的金属合金的重量在约5.0g.m-2至约500g.m-2的范围内; SOMF是沉积在金属合金(Mx Pd1-x)上的,仅透氢的钯的表面氧化薄金属膜; (b)是约0.05μm至约5.0μm范围内的SOMF的厚度; HPM是一种对氢气和氧气可透过的疏水性聚合物膜,也是水和过氧化氢的蒸气,而不是液态水或水溶液; 和(c)是每单位面积的SOMF的HPM的重量在约0.2g.m-2至约40g.m-2的范围内。
    • 6. 发明授权
    • Method for production of hydrogen peroxide with improved yield and selectivity by direct oxidation of hydrogen over palladium containing catalyst
    • 通过在含钯催化剂上直接氧化氢而提高产率和选择性的过氧化氢生产方法
    • US07288240B2
    • 2007-10-30
    • US11167573
    • 2005-06-27
    • Vasant Ramchandra ChoudharyChancal SamantaPrabhas Jana
    • Vasant Ramchandra ChoudharyChancal SamantaPrabhas Jana
    • C01B15/029B01J27/13
    • C01B15/029
    • A method for improving drastically both the selectivity and yield of hydrogen peroxide in the direct oxidation of hydrogen to hydrogen peroxide over a solid catalyst comprising palladium, which comprises: i) depositing on the solid catalyst at least two halogen containing compounds, one compound essentially comprising bromine and second compound essentially comprising fluorine with the bromine to palladium and fluorine to palladium atom ratios in the range from 0.02 to 20 and from 0.01 to 50, respectively; ii) decomposing the halo compounds deposited on the solid catalyst by calcination at a temperature above 200° C. under inert, reducing or oxidizing gas atmosphere or under vacuum; and iii) contacting the solid catalyst obtained from step (ii) with a gas mixture consisting of hydrogen and oxygen or air or O2 enriched air in an aqueous reaction medium, comprising a mineral acid at the following reaction conditions: concentration of mineral acid in the reaction medium above 0.001 mol/dm3, concentration of the solid catalyst in the reaction medium above 0.01 g/dm3, H2/O2 mole ratio in the gas mixture in the range from 0.01 to 10, flow rate of the gas mixture in the range from 50 cm3/g catalyst/h to 50,000 cm3/g catalyst/h, gas pressure at least 0.9 atm, and temperature below 100° C. and contact period of the reaction medium at least 0.01 h, is disclosed.
    • 一种用于在包含钯的固体催化剂中将氢气直接氧化成过氧化氢的过氧化氢的选择性和产率大大提高的方法,其包括:i)在固体催化剂上沉积至少两种含卤素的化合物,一种化合物基本上包含 溴和第二化合物,其主要包含氟,溴与钯和氟与钯的比例分别为0.02至20和0.01至50; ii)通过在惰性,还原或氧化气体气氛或真空下在高于200℃的温度下煅烧来分解沉积在固体催化剂上的卤代化合物; 和iii)将由步骤(ii)获得的固体催化剂与由氢气和氧气组成的气体混合物或空气或富含O 2的空气在含水反应介质中接触,所述反应介质在下列反应中包含无机酸 条件:反应介质中无机酸的浓度高于0.001mol / dm 3,反应介质中的固体催化剂浓度高于0.01g / dm 3,H
    • 7. 发明授权
    • Process for preparing hydrogen peroxide
    • US07157071B2
    • 2007-01-02
    • US10879501
    • 2004-06-30
    • Vasant Ramchandra ChoudharyChanchal SamantaPrabhas Jana
    • Vasant Ramchandra ChoudharyChanchal SamantaPrabhas Jana
    • C01B15/01
    • C01B15/01
    • The present invention discloses a process for the production of hydrogen peroxide from hydrazine hydrate or hydrazine salt, represented by a general formula: N2H4.nX, wherein, X is H2O, H2SO4, HNO3, HCl, HBr, HI or CH3COOH; n is 0.5, 1 or 2; N is nitrogen; H is hydrogen; S is sulfur; Cl is chlorine; Br is bromine; and I is iodine, by its liquid phase oxidation with oxygen, using a solid catalyst comprising palladium but with or without halogen promoter, in an aqueous reaction medium with or without comprising a mineral acid and/or halide anions, which comprises: i) contacting the solid catalyst with a hydrazine hydrate or hydrazine salt and oxygen containing gas selected from oxygen, air and oxygen enriched air, in aqueous reaction medium at the following reaction conditions: the concentration of hydrazine hydrate or hydrazine salt in the reaction medium above 0.001 mol/dm3, the concentration of mineral acid in the reaction medium in the range from zero mol/dm3 to 10 mol/dm3, the concentration of halide anions added to the reaction medium in the range from zero mmol/dm3 to 100 mmol/dm3, the concentration of the solid catalyst in the reaction medium in the range from 0.01 g/dm3 to 100 g/dm3, the space velocity of the oxygen containing gas in the range from 100 cm3/g catalyst/h to 100,000 cm3/g catalyst/h, the mass ratio of hydrazine hydrate or hydrazine salt to solid catalyst in the range from 0.01 to 100, the temperature below 100° C., the pressure at least 0.95 atm, and the reaction contact time above 0.02 h; and ii) separating the H2O2 from the reaction mixture.
    • 8. 发明授权
    • Process for the selective esterification of tertiary alcohol by an acid anhydride using a reusable solid catalyst
    • 使用可重复使用的固体催化剂通过酸酐选择性酯化叔醇的方法
    • US06420596B1
    • 2002-07-16
    • US09725642
    • 2000-11-29
    • Vasant Ramchandra ChoudharyKshudiram MantriSuman Kumar Jana
    • Vasant Ramchandra ChoudharyKshudiram MantriSuman Kumar Jana
    • C07C6702
    • C07C67/08C07C69/003C07C69/14C07C69/157C07C69/78
    • This invention provides a process for the selective esterfication of a tertiary alcohol(I) by an acid anhydride(II) to produce corresponding tertiary ester(III) and carboxylic acid(V), using a reusable solid catalyst(IV) comprising one or more halides of indium, gallium, zinc and iron. The process comprises: (i) contacting a mixture of (I) and (II) in the absence or presence of a non aqueous solvent with the fine particles of (IV) in a stirred batch reactor provided with a reflux water condenser at atmospheric pressure at the reaction conditions, such that the mole ratio of (II) to (I) is in the range from about 0.1 to about 10.0; the weight ratio of (IV) to (I+II) is in the range from about 0.005 to about 0.5; the reaction temperature is below about 80° C., and the reaction period is in the range from about 0.1 h to about 50 h; (ii) removing the solid catalyst(IV) from the reaction mixture by filtration; and (iii) reusing the separated solid catalyst for subsequent batch of the process.
    • 本发明提供一种通过酸酐(II)选择性酯化叔醇(I)以产生相应的叔酯(III)和羧酸(V)的方法,使用包含一种或多种的可重复使用的固体催化剂(IV) 铟,镓,锌和铁的卤化物。 该方法包括:(i)在不存在或不存在非水溶剂的情况下,将(I)和(II)的混合物与(IV)的细颗粒在设置有回流水冷凝器的搅拌间歇反应器中在大气压下接触 在反应条件下使得(II)与(I)的摩尔比在约0.1至约10.0的范围内; (IV)至(I + II)的重量比在约0.005至约0.5的范围内; 反应温度低于约80℃,反应时间为约0.1小时至约50小时; (ii)通过过滤从反应混合物中除去固体催化剂(IV); 和(iii)将分离的固体催化剂重新用于后续批次的方法。