Abstract
The electrocatalytic oxidation degradation kinetics of oxalic acid in a cylindrical electrochemical reactor with Ti/IrO2-Ta2O5 as an anode was studied. The relation between instantaneous current efficiency and organic concentration in bulk was established based on the two paths for direct electrochemical oxidations, and the theoretical model was verified by experiments. The experimental resultswere reasonably consistent with the established kinetic model. Furthermore, the competition between the two paths was explored with the modelparameter analysis.
Graphical Abstract
Keywords
electrochemical oxidation, Ti/IrO2-Ta2O5, anode, oxalic acid, theoretical model
Publication Date
2013-08-28
Online Available Date
2013-03-24
Revised Date
2013-03-19
Received Date
2012-12-25
Recommended Citation
Jing SU, Hai-bo LIN, Hong XU, Wei-min HUANG, Ya-peng HE.
Electrocatalytic Oxidation Degradation Kinetics of Oxalic Acid in a Cylindrical Electrochemical Reactor with Ti/IrO2-Ta2O5 Anode[J]. Journal of Electrochemistry,
2013
,
19(4): 293-299.
DOI: 10.61558/2993-074X.2114
Available at:
https://jelectrochem.xmu.edu.cn/journal/vol19/iss4/1
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