Ultra- and nanofiltration with high shear CR-filters have been utilized for cleaning of clear filtrates and effluents from the pulp and paper industry. The aim was to find out how different nanofiltration membranes operate at high shear conditions. The filtration efficiency of the membranes was evaluated by measuring flux, retention and fouling at various recovery and pH conditions. High fluxes (∼100 L/(m2h)) for nanofiltration membranes were measured when circulation waters from the paper machine were filtered at neutral conditions. In the filtration of discharge of external activated sludge treatment plants we measured fluxes around 150 L/(m2h) even at a concentration factor of 12. The best NF membranes removed over 80% of the organic carbon and of the conductivity and almost completely eliminated the color. With acidic waters fluxes and retentions were significantly lower. The NF270 membrane from Dow and the Desal-5 membranes from Osmonics had the highest flux and retention properties. However, the Desal-5 membrane lost its retention properties slowly, which restricts its use in the high shear CR-filter. CR-nanofiltration can be used in the pulp and paper industry without feed pre-treatment by ultrafiltration. This increases the attractiveness of high shear CR-nanofiltration.
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Research Article|
August 01 2004
Ultrafiltration and nanofiltration in the pulp and paper industry using cross-rotational (CR) filters
M. Mänttäri;
1Department of Chemical Technology, Lappeenranta University of Technology, Laboratory of Membrane Technology and Technical Polymer Chemistry, P.O. Box 20, FIN-53851, Lappeenranta, Finland
E-mail: [email protected]
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M. Nyström
M. Nyström
1Department of Chemical Technology, Lappeenranta University of Technology, Laboratory of Membrane Technology and Technical Polymer Chemistry, P.O. Box 20, FIN-53851, Lappeenranta, Finland
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Water Sci Technol (2004) 50 (3): 229–238.
Citation
M. Mänttäri, M. Nyström; Ultrafiltration and nanofiltration in the pulp and paper industry using cross-rotational (CR) filters. Water Sci Technol 1 August 2004; 50 (3): 229–238. doi: https://doi.org/10.2166/wst.2004.0200
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