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Flux decline in crossflow microfiltration and ultrafiltration: experimental verification of fouling dynamics
Institution:1. School of Nuclear Science and Engineering, Shanghai Jiao Tong University, Shanghai 200240, China;2. China Nuclear Power Technology Research Institute, Shenzhen 518026, China;3. Institute of Fusion and Reactor Technologies (IFRT), Karlsruhe Institute of Technologies (KIT), Karlsruhe 76131, Germany;1. State Key Laboratory of Coal Combustion, Huazhong University of Science and Technology, Luoyu Road 1037, Wuhan 430074, China;2. Dongfang Electric Corporation Limited, Shuhan Road 333, Chengdu 610036, China;1. Department of Chemical and Biomolecular Engineering, National University of Singapore, 4 Engineering Drive 4, Singapore 117585, Singapore;2. Department of Electrical and Computer Engineering, National University of Singapore, 4 Engineering Drive 3, Singapore 117583, Singapore;3. Water Desalination & Reuse (WDR) Center, King Abdullah University of Science and Technology, Thuwal 23955-6900, Saudi Arabia
Abstract:The theory of fouling dynamics in crossflow membrane filtration is compared with ultrafiltration experiments with suspensions of 0.12 μm silica colloids. It has been experimentally verified that colloidal fouling in crossflow filtration is a dynamics process from non-equilibrium to equilibrium and that the steady state flux is the limiting flux. With the cake concentration cg identified from an independent experiment and the specific cake resistance calculated by Carman–Kozeny equation, the time-dependent flux and the time to reach steady state in the experiments of this study are correctly predicted with the theory of fouling dynamics.
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