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In this work the products of the oxidation at BDD anode of chloride ions in aqueous solutions were identified during galvanostatic electrolyses performed in a filter-press reactor operating both in batch and continuous mode. A set of experiments were preformed in order to study the effect of operating conditions (current density, residence time, hydrodynamics and chloride concentration) on distribution and concentration of electrolysis by-products. As a comparison experiments were also performed using a commercial DSA anode. A simple mathematical model was formulated, and the model predictions agree with the experimental data in a wide range of experimental conditions. The results of this work showed that at low chloride concentrations electrolysis with BDD anode produce a mixture of powerful oxidant: low current density, high mass transfer conditions and low residence time were found as optimal conditions to maximize the concentration of oxidants and minimize the concentration of chlorates. The proposed reaction mechanism may also justify the controversial effect of chloride ions in wastewater treatments: the electrolysis carried out with BDD anodes and electrolyte containing chloride concentration higher 1 g/L could meet the target of the process only if the active chlorine is effective in oxidation of the pollutant that must be removed

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This paper presents the results of a numerical study of the kinetics of electrochemical oxidation of different organic substances at boron doped diamond (BDD). It is well established that oxidation of organics at BDD anodes takes place in the potential region of oxygen evolution, through reaction steps in which OH radicals are involved: these radicals can react with organic compounds to give more oxidised substances, or with water to give oxygen. Because of the high reactivity of OH radicals these reactions are confined to a thin film adjacent to the electrode surface. A mathematical model was implemented, which accounts for chemical and electrochemical reactions, as well as for the transport phenomena involved in the process: the parameters of the model were derived from experimental data. The model allowed calculation of the trend with time of reactant concentration, reaction intermediates and oxidisable agents: their space profiles in the reactor were also obtained. The numerical predictions of the model were compared with experimental results obtained from galvanostatic electrolyses of different organic compounds: (a) 2,4,6-trihydroxy-1,3,5 triazine also known as cyanuric acid (CA), which is well known to be refractory to oxidation with OH; (b) atrazine (ATR) the most oxidisable precursor of CA, and (c) phenol which is considered as an OH scavenger because of its high reactivity. The agreement between experimental and model predicted data was good in all the examined conditions

The results of an experimental study on electrochemical disinfection of water are presented. Attention was paid to the behaviour of chlorine compounds during electrolysis of water containing chlorides, with particular regard to the selectivity of the process towards the production of oxidising agents. Two reactor configurations were tested: a stirred tank cell and a filter press cell inserted in a hydraulic circuit. Both cells were equipped with boron doped diamond (BDD) anodes. Experiments were performed in batch and continuous mode. The effect of such operating parameters, current density, stirring rate or recirculating flow rate, on the behaviour of the process was investigated. The results at BDD anodes show that low current densities and perfect mixing of the system should be adopted in order to obtain high values of the concentration of oxidising agents avoiding the formation of such undesired by-products as chlorite, chlorate and perchlorate ions. Runs were also performed in which BDD was substituted by a commercial (Ti/RuO2) DSA anode and the results obtained with the two materials are compared