Abstract
Monolithic anion exchanger PolyHIPE media were used for the removal of nitrate anions () from aqueous solutions. Both equilibrium and column
adsorption tests and regeneration tests were carried out. The suitability of the Langmuir adsorption model to the equilibrium data was investigated. The maximum adsorption capacity was 0.215 meq/g as per Langmuir isotherm at 20°C. At a flow rate of 5 ml/min (corresponding flux was 1.0 cm/min) and 150 mg/L nitrate feed concentration, breakthrough capacity and apparent capacity were 1.336 meq
/g resin and 2.842 meq
/g resin, respectively. Column experimental tests were conducted to provide data for theoretical modeling and to verify the system performance of the process. The theoretical column model adopted in this work was found to describe well, the ion-exchange breakthrough characteristics. After reaching equilibrium adsorption capacity, the monoliths were regenerated using 1 N HCl and were subsequently retested. It was found that the regeneration efficiency reduced from 99% after second usage to 95% after the third usage.
Acknowledgment
Research Fund of Ataturk University, Turkey sponsored the PhD studentship of Dr Necla Barlık. Further support was received for Prof Galip Akay from the European Union under the integrated project, POLYCAT (Contract No: CP-IP 246095-2 POLYCAT) when he led the project at Newcastle University.