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• W2772181736 abstract "In this work, ultrafiltration (UF) is used to remove dissolved and colloidal substances (DCS) from a secondary clarifier effluent from a wastewater treatment plant (WWTP) in a papermaking factory. The approach has been to examine and model the decline in permeate flux resulting from membrane fouling. Effluent from a WWTP at a papermaking factory, previously filtered, was used as feed. UF experiments were carried out in a laboratory-scale plant using a 10 kDa polyethersulfone (PES) UF membrane in a flat sheet module with an active area of 154.8 cm2. The transmembrane pressure (TMP) (1–3 bar) and crossflow rate (1.5–4.5 L/min) were varied during the experiments, at constant temperature (22 ± 0.5 °C). Experimental results from UF tests were expressed in terms of permeate flux (Jp) as a function of time to check modified Hermia’s models adapted to crossflow filtration. The parameters of these models were theoretically estimated. The predicted results were compared with experimental data with a high goodness of fit. The results showed that the phenomenon controlling fouling, under most of the conditions tested, was intermediate blocking (R2 > 0.96). Measurements of particle size distribution and zeta potential near the isoelectric point, showed a substantial reduction in colloidal compounds. Additionally, given that COD was removed down to 110 mg/L, it could be said that UF is suitable for producing water that can be reused in different papermaking processes." @default.
• W2772181736 created "2017-12-22" @default.
• W2772181736 creator A5006306326 @default.
• W2772181736 creator A5018239369 @default.
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• W2772181736 date "2018-02-01" @default.
• W2772181736 modified "2023-10-18" @default.
• W2772181736 title "Modelling approach to an ultrafiltration process for the removal of dissolved and colloidal substances from treated wastewater for reuse in recycled paper manufacturing" @default.
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• W2772181736 doi "https://doi.org/10.1016/j.jwpe.2017.11.017" @default.
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