Nanofiltration of a German groundwater of high hardness and NOM content: performance and costs |
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Authors: | A Gorenflo D Velázquez-Padrón FH Frimmel |
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Affiliation: | Engler-Bunte-Institut, Water Chemistry, Universität Karlsruhe, Engler-Bunte-Ring 1, D-76131 Karlsruhe, Germany Tel. +49 (721) 6082593; Fax + 49 (721) 6087051 |
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Abstract: | Nanofiltration of conventionally pretreated groundwater with elevated hardness and content of NOM (Ca2+: 115 mg/L; Mg2+: 12 mg/L; DOC = 2.9 mg/L) was carried out in a German water treatment plant of the public works of Mainz. For the investigated water the employed membrane (NF200B, Filmtec/DOW) showed almost complete rejection (>95%) of NOM, determined by measuring DOC, UVA (254 nm) and AOX- and THM-formation potential. Due to the high concentration of SO42− and presumably due to complexation of Ca2+ with humic substances the rejection of Ca2+ and Mg2+ was unexpectedly high (>74% and >86%, respectively) compared to a pure CaCl2 solution (R(CaCl2) <45%). Within an operation period of 4 weeks no significant fouling occurred (flux decline <2%). This was mainly due to the pre-treatment of the raw water (deferrization, demanganization, rapid sand filtration). The operating costs for a nanofiltration plant were calculated to about € 0.23/m3 at a permeate output of 20,000 m3/d which means an increase of the price for drinking water approximately 9%. By blending the permeate and the conventionally treated water at a ratio to yield a DOC concentration in the blend of 1 mg/L, the additional costs for nanofiltration would come to € 0.11/m3. |
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Keywords: | AOX-/THM-formation potential Cost modeling Drinking water Fouling Gel chromatography with DOC detection Membrane filtration Softening |
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