The addition of the chelating polymer polyacrylic acid (PAA) to assist in the removal of manganese from groundwater by membranes was investigated using membranes with different pore sizes under various operating conditions. Negligible manganese removal was achieved with the UF and NF membranes at acidic pH values, but removals exceeding 90% could be achieved at elevated pH (pH 9), presumably due to the formation of manganese hydroxides. Mn removal increased substantially when PAA was added to the feed solution, due to chelation of Mn by the PAA and rejection of the chelates by the membranes. The chelate could be broken at acidic pH, releasing free PAA that could then be separated from the Mn ions and reused. Smaller PAA molecules were lost in the first regeneration cycle, but negligible PAA was lost in subsequent cycles. In the systems with PAA, nitrate ions were rejected more efficiently than in the PAA-free systems, presumably because of electrical repulsion between nitrate ions and PAA sorbed on the membrane surface. With increasing PAA dose, the volumetric flux first decreased and then increased; the latter result was accompanied by a change in the physical-chemical form of the polymers, as indicated by an increase in turbidity.
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Research Article|
March 01 2005
Removal of manganese from water using combined chelation/membrane separation systems
S.-C. Han;
S.-C. Han
*Department of Environmental Engineering, Kyungpook National University, Daegu 702-701, Korea
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K.-H. Choo;
K.-H. Choo
*Department of Environmental Engineering, Kyungpook National University, Daegu 702-701, Korea
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S.-J. Choi;
S.-J. Choi
*Department of Environmental Engineering, Kyungpook National University, Daegu 702-701, Korea
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M.M. Benjamin
**Department of Civil and Environmental Engineering, University of Washington, Seattle, WA 98195, USA
E-mail: chookh@knu.ac.kr
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Water Sci Technol (2005) 51 (6-7): 349–355.
Citation
S.-C. Han, K.-H. Choo, S.-J. Choi, M.M. Benjamin; Removal of manganese from water using combined chelation/membrane separation systems. Water Sci Technol 1 March 2005; 51 (6-7): 349–355. doi: https://doi.org/10.2166/wst.2005.0656
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