The inactivation of HO was studied in a continuous flow electro-Fenton reactor. Ion exchange resin was used to provide iron support, and H2O2 was produced in situ by cathodic reduction of oxygen. In order to study the electro-Fenton efficiency, three treatments were run; treatment A: without electric current and without iron promoter, treatment B: applying a potential difference of -4V but without iron promoter; and treatment C: applying the aforementioned potential difference and with iron promoter. Treatment A represents the retention capacity of the system given by sorption capacity of involved materials, while B represents the electrochemical oxidation effect, and finally C represents the electro-Fenton effect. HO determination was carried out in the influent and effluent, as well as in the internal materials of the reactor; Fe (II)-ionic exchange resin, cathode (graphite cloth), activated carbon packed reactor, anode (graphite cloth) and Na-ionic exchange resin.
It was possible to retain between 96.59% and 98.33% of HO admitted to the reactor, the higher inactivation was observed in treatment C (See Figure 1). The percentage of total HO, represents the amounts of HO both viable and non-viable. The percentage of viable HO was determined by trypan blue staining and incubation to verify HO viability. A low presence of viable HO could be observed in treatments B and C, while treatment C with electro-Fenton conditions produces hydroxyl radicals that have a high oxidizing potential which affects the layers of the HO.
Control treatments A and B, compared to treatment C, presented higher percentages distribution for both total and viable HO, demonstrating that inactivation of HO is possible through the electro-Fenton process. The decrease in viable HO for treatments C with conditions suitable for electro-Fenton can serve as qualitative evidence that the Fenton reaction is taking place.