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Feasibility of electro-osmotic belt filter dewatering technology at pilot scale

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dc.contributor.author Snyman, HG
dc.contributor.author Forssman, P
dc.contributor.author Kafaar, A
dc.contributor.author Smollen, M
dc.date.accessioned 2007-06-12T08:11:51Z
dc.date.available 2007-06-12T08:11:51Z
dc.date.issued 2000
dc.identifier.citation Snyman, HG, et al. 2000. Feasibility of electro-osmotic belt filter dewatering technology at pilot scale. Water Science and Technology, vol. 41(8), pp 137-144 en
dc.identifier.issn 0273-1223
dc.identifier.uri http://hdl.handle.net/10204/597
dc.description Copyright: 2000 IWA Publishing en
dc.description.abstract Sewage sludge is typically dewatered using drying beds, belt filter presses or centrifuges. Mechanical dewatering of sludge is costly in terms of capital and running costs, especially the flocculent. In an attempt to address the need for more cost-effective dewatering technologies, electro-osmotic belt filtering was developed by Smollen and Kafaar in 1995. The mechanical equipment resembles a belt filter press but the belts are stainless steel, woven belts, which act as the electrodes. In this study, the feasibility of the technology was tested at pilot scale using waste activated-, anaerobically digested- and dissolved air flotation sludge. The parameters which were investigated include the applied voltage, polyelectrolyte usage and sludge feed rate. Applied voltage of between 15 and 15 volts increased the dewatering significantly in the waste activated- and anaerobically digested sludge. Applying a voltage in dissolved air flotation sludge could not enhance the efficiency of dewatering, unless stored to de-air. The technology was found as sensitive to polyelectrolyte dosages as belt presses. The performance of the electro-osmotic belt filter was sensitive to feed rate, but performed well with non-thickened waste activated sludge (0.61% solids), resulting in cake solids above 20%. en
dc.language.iso en en
dc.publisher IWA Publishing en
dc.subject Belt filter en
dc.subject Sewage sludge en
dc.subject Dewatering en
dc.subject Electro-osmosis en
dc.subject Wastewater sludge en
dc.title Feasibility of electro-osmotic belt filter dewatering technology at pilot scale en
dc.type Article en
dc.identifier.apacitation Snyman, H., Forssman, P., Kafaar, A., & Smollen, M. (2000). Feasibility of electro-osmotic belt filter dewatering technology at pilot scale. http://hdl.handle.net/10204/597 en_ZA
dc.identifier.chicagocitation Snyman, HG, P Forssman, A Kafaar, and M Smollen "Feasibility of electro-osmotic belt filter dewatering technology at pilot scale." (2000) http://hdl.handle.net/10204/597 en_ZA
dc.identifier.vancouvercitation Snyman H, Forssman P, Kafaar A, Smollen M. Feasibility of electro-osmotic belt filter dewatering technology at pilot scale. 2000; http://hdl.handle.net/10204/597. en_ZA
dc.identifier.ris TY - Article AU - Snyman, HG AU - Forssman, P AU - Kafaar, A AU - Smollen, M AB - Sewage sludge is typically dewatered using drying beds, belt filter presses or centrifuges. Mechanical dewatering of sludge is costly in terms of capital and running costs, especially the flocculent. In an attempt to address the need for more cost-effective dewatering technologies, electro-osmotic belt filtering was developed by Smollen and Kafaar in 1995. The mechanical equipment resembles a belt filter press but the belts are stainless steel, woven belts, which act as the electrodes. In this study, the feasibility of the technology was tested at pilot scale using waste activated-, anaerobically digested- and dissolved air flotation sludge. The parameters which were investigated include the applied voltage, polyelectrolyte usage and sludge feed rate. Applied voltage of between 15 and 15 volts increased the dewatering significantly in the waste activated- and anaerobically digested sludge. Applying a voltage in dissolved air flotation sludge could not enhance the efficiency of dewatering, unless stored to de-air. The technology was found as sensitive to polyelectrolyte dosages as belt presses. The performance of the electro-osmotic belt filter was sensitive to feed rate, but performed well with non-thickened waste activated sludge (0.61% solids), resulting in cake solids above 20%. DA - 2000 DB - ResearchSpace DP - CSIR KW - Belt filter KW - Sewage sludge KW - Dewatering KW - Electro-osmosis KW - Wastewater sludge LK - https://researchspace.csir.co.za PY - 2000 SM - 0273-1223 T1 - Feasibility of electro-osmotic belt filter dewatering technology at pilot scale TI - Feasibility of electro-osmotic belt filter dewatering technology at pilot scale UR - http://hdl.handle.net/10204/597 ER - en_ZA


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