Anodic oxidation of a direct dye in an electrochemical reactor
- 1 January 1987
- journal article
- research article
- Published by Taylor & Francis in Journal of Environmental Science and Health, Part A
- Vol. 22 (1) , 27-45
- https://doi.org/10.1080/10934528709375331
Abstract
In this work, anodic oxidation of C.I. direct blue 21 was carried out in an electrochemical reactor at a constant temperature of 20°C. The technique was found successful in removing the color of the dye from aqueous solutions containing 0.5 M sodium sulfate. Variables studied were: initial dye concentration, solution flow rate to the reactor, anode area, current density and time duration of anodic oxidation. It was found that the rate of dye removal increased with increasing current density, duration of anodic oxidation and solution flow rate. The mass transfer coefficient was found to increase with increasing reactor current density, decreasing the area of the anode and decreasing the initial dye concentration.This publication has 5 references indexed in Scilit:
- Anodic oxidation of phenol for waste water treatmentThe Canadian Journal of Chemical Engineering, 1981
- Effect of gas evolution on the rate of mass transfer at vertical electrodesElectrochimica Acta, 1972
- The Electrochemical Treatment of Aqueous Effluent StreamsPublished by Springer Nature ,1972
- Electrolytic decomposition of cyanides, phenols and thiocyanates in effluent streams—a literature reviewJournal of Chemical Technology & Biotechnology, 1971
- Electrolytic oxidation of strong cyanide wastesJournal of Chemical Technology & Biotechnology, 1963