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NAMS 2002 Workshop - ICOM 2008

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Nanofiltration and Reverse Osmosis III - Applications – 4<br />

Friday July 18, 11:15 AM-11:45 AM, Maui<br />

Nanofiltration of Ferric and Ferrous Cations in Acidic Solutions<br />

X. Bernat (Speaker), ETSEQ, Universitat Rovira i Virgili, Terragona, Spain<br />

F. Stüber, ETSEQ, Universitat Rovira i Virgili, Terragona, Spain<br />

A. Fortuny, Universitat Politècnica de Catalunya, Barcelona, Spain<br />

C. Bengoa, Universitat Rovira i Virgili, Terragona, Spain<br />

A. Fabregat, ETSEQ, Universitat Rovira i Virgili, Terragona, Spain<br />

J. Font, ETSEQ, Universitat Rovira i Virgili, Terragona, Spain - jose.font@urv.cat<br />

Ferric and ferrous ions are used as catalyst in advanced oxidation processes, in<br />

conjunction with hydrogen peroxide, to accelerate oxidation reactions for partially<br />

mineralizing organic biorefractory substances. Fenton process, Fe/H2O2, is the<br />

most popular technique based in this principle. As a result, homogeneous iron<br />

leaves the oxidation step with the treated wastewater posing potential<br />

environmental and economical problems. Nanofiltration is being studied and<br />

applied as a promising technology to recover multivalent ions and organic<br />

compounds from aqueous polluted streams achieving additionally partial<br />

softening of these waters. Several mechanisms such as charge repulsion<br />

between the membrane and the targeted compound and sieving are involved in<br />

the mechanisms allowing the retention of the targeted ions or compounds. In<br />

addition, several operating variables may affect the efficiency of the separation<br />

process by lowering the permeate fluxes during the operation. The<br />

transmembrane pressure, the pH, the hydrodynamic conditions, the presence of<br />

other species and still others may influence the retention, the permeate rate and<br />

the fouling during the filtration process. In this work, the recovery of ferrous and<br />

ferric ions from aqueous solution by nanofiltration is presented. The experiments<br />

were conducted in a commercial batch stirred filtration cell. The effect of several<br />

operating variables on both the iron retention and the permeate flux were<br />

studied. NF, NF90 and NF270 membranes (manufactured by Dow Filmtec) were<br />

selected for this work as they are commercially available membranes that<br />

possess different isoelectric points and charge densities on their surfaces. The<br />

solutions to be treated were adjusted at pH 2, which is typical pH for effluents<br />

treated by Fenton process. The effect of the transmembrane pressure, the<br />

stirring speed, the presence of NaCl and the iron concentration on the iron<br />

retention and permeate flux decline is illustrated. The results show that low<br />

permeate flux decline was achieved and high Fe (III) retention (up to 99.9%) was<br />

obtained with all the tested membranes, assuring the final quality of the permeate<br />

and the possibility of reusing the retentate in the oxidation reactor. When<br />

comparing Fe (III) and Fe (II) performance, a lower iron charge caused a<br />

decrease of the iron retention due to the poorer charge repulsion phenomena<br />

between the charged membrane surface and the Fe (II) ions. NF90, which is a<br />

specially designed membrane for the recovery of iron, showed the highest Fe (III)

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