Combined adsorption-permeation membrane process for the removal of chromium (III) ions from contaminated water

Abstract The objective of this work is the examination of the combined adsorption–permeation process for the removal of trivalent chromium from the aqueous phase. Two types of supported membranes are developed on the top surface of an asymmetric α-Al 2 O 3 tubular ceramic substrate by the sol–gel method: the first one was made of γ-Al 2 O 3 while the second one of γ-Al 2 O 3 or TiO 2 . The synthesized membranes are subsequently adapted to an ultrafiltration unit operating in a continuous cross flow mode, and are investigated for the removal of Cr(III) from the aqueous phase. The adsorption capacity of γ-Al 2 O 3 and TiO 2 is examined in single batch experiments at different pH values and it is found that maximum chromium removal is observed for TiO 2 , at pH = 5. It appears that the adsorption capacity for TiO 2 is not affected by the adsorbent dosage. The combined adsorption–permeation process is then studied in the membrane ultrafiltration unit for the treatment of a 0.5 mg L −1 solution; negligible chromium effluent concentration was measured, for both types of membranes, the one with the TiO 2 layer appearing to have a higher efficiency. The examination of membrane surface by SEM and TEM revealed the formation of a chromium layer, that was attributed to the membrane layer acidic sites. FT-IR studies showed that the membrane with the highest chromium removal capacity presented a high percentage of strong Bronsted acidic sites.