Journal
JOURNAL OF HAZARDOUS MATERIALS
Volume 144, Issue 3, Pages 634-638Publisher
ELSEVIER SCIENCE BV
DOI: 10.1016/j.jhazmat.2007.01.087
Keywords
chromium recovery; ion exchange; equilibrium; isotherms
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Effluent discharged from the chromium electroplating industry contains a large number of metals, including chromium, copper, nickel, zinc, manganese and lead. The ion exchange process is an alternative technique for application in the treatment of industrial wastewater containing heavy metals and indeed it has proven to be very promising in the removal and recovery of valuable species. The main objective of the present work is to evaluate the performance of commercial ion exchange resins for removing chromium trivalent from industrial effluents, and for this purpose two resins were tested: a chelating exchange resin (Diaion CR11) and a weak cationic resin (Amberlite IRC86). In order to evaluate the sorption capacity of the resins some equilibrium experiments were carried out, being the temperature and pH the main variables considered. The chromium solutions employed in the experiments were synthetic solutions and industrial effluents. In addition, a transient test was also performed as an attempt to understand the kinetic behaviour of the process. (c) 2007 Elsevier B.V. All rights reserved.
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