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Membrane fouling prevention in crossflow microfiltration by the use of electric fields
Affiliation:1. Aix-Marseille University, CNRS, LP3 Laboratory, UMR 7341, 13288 Marseille, France;2. Aix-Marseille University, CNRS, MADIREL Laboratory, UMR 7246, 13397 Marseille, France;3. Aix-Marseille University, CNRS, ICR UMR7273, CROPS, Centre Saint-Jérôme, F-13397 Marseille Cedex 20, France;4. FR CNRS 3459, Réseau sur le Stockage Electrochimique de l’Energie (RS2E), Paris, France;5. FR CNRS 3104, ALISTORE-ERI, France;1. Faculty of Civil and Transportation Engineering, Guangdong University of Technology, Guangzhou 510006, China;2. State Key Laboratory of Pollution Control and Resource Reuse, School of Environmental Science and Engineering, Tongji University, Shanghai 200092, China;1. Department of Chemical Engineering, College of Engineering, Jazan University, Jazan 11451, Saudi Arabia;2. Chemistry Department, Faculty of Science, Cairo University, Giza, Egypt;3. Engineering Mathematics and Physics Department, Faculty of Engineering, Mansoura University, El-Mansoura, Egypt;4. Department of Chemistry, College of Science, King Saud University, Riyadh 11451, Saudi Arabia;5. Department of Mathematics and Physics Engineering, Faculty of Engineering at Mataria, Helwan University, Cairo 11718, Egypt;1. Service de dermatologie-vénérologie, CHU Ibn Rochd, 1, rue Lahcen-Elaarjoun, quartier des hôpitaux, 20000 Casablanca, Maroc;2. Service de pédiatrie 5, hôpital d’enfants, CHU Ibn Rochd, 6, rue Lahssen-Elaarjoun, quartier des hôpitaux, 20000 Casablanca, Maroc
Abstract:From an analysis of fluid velocity and electric field profiles the trajectory of particles through crossflow microfiltration units has been calculated. A tubular geometry filter leads to the most effective use of electrical power, when it is used as an aid to prevent membrane fouling. Results for plate, tubular and mutitube filters are given. Some experimental data from a tubular filter are presented, which demonstrate typical effects of the important parameters.
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