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A TiO2/Al2O3 catalyst to improve the ozonation of oxalic acid in water

机译:TiO2 / Al2O3催化剂,用于改善水中草酸的臭氧化

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摘要

Removal of oxalic acid from water has been accomplished through TiO2/Al2O3 catalytic ozonation. The combined use of ozone and the titanium catalyst leads to a conspicuous 80% of oxalic acid conversion in 3 h which compares favorably to the hardly 2% reached in the absence of the catalyst at pH 2.5. At the experimental conditions applied, the catalytic process develops under complete carbon mineralization and does not proceed through hydroxyl radical oxidation. The process rate can be described by considering an Eley-Rideal mechanism. Thus, it is proposed that adsorbed oxalic acid reacts directly with ozone in solution, the oxalic acid adsorption stage being the rate-limiting step. This mechanism justifies the experimental kinetic orders found in the range 1 and 0-1 for oxalic acid and ozone, respectively. The apparent activation energy of the catalytic ozonation was also found to be 14 kcal mol(-1). (C) 2003 Elsevier B.V. All rights reserved. [References: 23]
机译:通过TiO2 / Al2O3催化臭氧化作用,可以从水中去除草酸。臭氧和钛催化剂的组合使用可在3小时内产生80%的草酸转化率,这比不使用pH 2.5的催化剂时几乎不转化为2%的草酸转化率高。在所应用的实验条件下,催化过程在完全碳矿化的条件下发展,并且不会通过羟基自由基氧化进行。可以通过考虑Eley-Rideal机制来描述处理速率。因此,提出吸附的草酸与溶液中的臭氧直接反应,草酸的吸附阶段是限速步骤。这种机理证明了草酸和臭氧的实验动力学级数分别在1和0-1范围内。还发现催化臭氧氧化的表观活化能为14 kcal mol(-1)。 (C)2003 Elsevier B.V.保留所有权利。 [参考:23]

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