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Catalytic wet air oxidation of phenol over platinum and ruthenium catalysts

机译:铂和钌催化剂对苯酚的湿式催化氧化

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Active platinum and ruthenium catalysts have been developed that are also highly selective in catalytic wet air oxidation (CWAO) of phenol. CWAO of phenol was studied using a trickle bed reactor over temperatures 393 and 473 K under total pressure of 5 and 8 MPa at LHV = 0.5-6 h(-1). The initial phenol concentration was ca. 50 mol/m(3) and the initial COD of the solution was ca. 12 kg O-2/m(3). Molar ratio of oxygen to phenol was ca. 38:1. A kinetic analysis of phenol conversion and COD changes has been elaborated based upon lumped reaction network according to which oxidation of phenol proceeds substantially via two routes: (1) directly to carbon dioxide, and (2) through intermediates which are difficult to oxidize over the catalysts studied. Estimates of chemical oxygen demand for the lumped intermediates amount to 64+/-30 g O-2/mol confirming the literature information that these are carboxylic acids, probably with predominant content of acetic acid that is most refractory at CWAO conditions. Power law kinetic equations describe satisfactorily CWAO of phenol over the catalysts of this work. Most activation energies range from 58 to 107 kJ/mol. Reaction orders for phenol range from 0.94 to 2.0 and these for oxygen from 0.22 to 0.85. (C) 2003 Elsevier B.V. All rights reserved. [References: 61]
机译:已经开发了在铂的催化湿空气氧化(CWAO)中也具有高选择性的活性铂和钌催化剂。使用滴流床反应器在LHV = 0.5-6 h(-1)的总压力为5和8 MPa,温度为393和473 K的条件下研究了苯酚的CWAO。最初的苯酚浓度为约。 50 mol / m(3),溶液的初始COD约为。 12 kg O-2 / m(3)。氧气与苯酚的摩尔比为。 38:1。基于集总反应网络,对苯酚转化率和COD变化进行了动力学分析,根据该网络,苯酚的氧化主要通过两种途径进行:(1)直接转化为二氧化碳,(2)通过在氧化过程中难以氧化的中间体研究催化剂。集总中间体的化学需氧量估计为64 +/- 30 g O-2 / mol,这证​​实了文献信息,即羧酸,主要是乙酸含量,在CWAO条件下最难熔。幂律动力学方程式令人满意地描述了这项工作的催化剂上苯酚的CWAO。大多数活化能范围为58至107 kJ / mol。苯酚的反应级数为0.94至2.0,氧的反应级数为0.22至0.85。 (C)2003 Elsevier B.V.保留所有权利。 [参考:61]

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