4.7 Article

Hybrid SBR-FO system for wastewater treatment and reuse: Operation, fouling and cleaning

期刊

DESALINATION
卷 393, 期 -, 页码 31-38

出版社

ELSEVIER SCIENCE BV
DOI: 10.1016/j.desal.2016.03.015

关键词

Forward osmosis (FO); Sequential batch reactor (SBR); Fouling; Natural organic matter (NOM); Wastewater treatment; Membrane cleaning

资金

  1. King Abdullah University of Science and Technology (KAUST), Saudi Arabia

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Forward osmosis (FO) is a novel membrane separation process that potentially can be used as an energy-saving alternative to conventional membrane processes. A hybrid sequential batch reactor (SBR)-FO process was explored. In this system, a plate and frame FO cell including two flat-sheet FO membranes was submerged in a bioreactor treating synthetic domestic wastewater. The dissolved organic carbon (DOC) removal efficiency of the system was 98.55%. Total nitrogen removal was 62.4%, with nitrate, nitrite and ammonium removals of 58.4%, 96.2% and 88.4%, respectively. Phosphate removal was almost 100%. The 15-hour cycle average water flux of a virgin membrane with air scouring was 2.95 L/m(2).h(-1). Air scouring can help to remove loose foulants from the membrane active layer, thus helping to recover up to 89.5% of the original flux. Chemical cleaning of the fouled active layer of the FO membrane was not as effective as air scouring. Natural organic matter (NOM) characterization methods (liquid chromatography-organic carbon detection (LC-OCD) and 3-D fluorescence excitation emission matrix (FEEM)) show that the FO membrane has a very good performance in rejecting biopolymers, humics and building blocks, but a limited ability in rejecting low molecular weight neutrals. Transparent exopolymer particles (TEP) and other biopolymers might be associated with fouling of the membrane on the support layer. A 1% sodium hypochlorite (NaOCl) cleaning solution was proved to be effective for removing the foulants from the support layer and recovering the original flux. (C) 2016 Elsevier B.V. All rights reserved.

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