Forward osmosis membrane fouling and cleaning for wastewater reuse

被引:31
|
作者
Yu, Youngbeom [1 ]
Lee, Seockheon [2 ]
Maeng, Sung Kyu [3 ]
机构
[1] Korea Water Resources Corp, K Water Res Inst, 462-1 Jeonmin Dong, Daejeon 05730, South Korea
[2] Korea Inst Sci & Technol, Ctr Water Resource Cycle, Hwarangno14 Gil 5, Seoul 136791, South Korea
[3] Sejong Univ, Dept Civil & Environm Engn, 98 Gunja Dong, Seoul 143747, South Korea
来源
关键词
air-scouring; cross-flow velocity; forward osmosis; membrane fouling; osmotic backwashing; spacer; AMMONIA-CARBON DIOXIDE; REVERSE-OSMOSIS; NANOFILTRATION MEMBRANES; ORGANIC-MATTER; CONTACTOR PROCESSES; PROCESS PERFORMANCE; PHYSICAL ASPECTS; PART I; MECHANISMS; PRETREATMENT;
D O I
10.2166/wrd.2016.023
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Membrane fouling properties and different physical cleaning methods for forward osmosis (FO) and reverse osmosis (RO) laboratory-scale filtration systems were investigated. The membrane fouling, with respect to flux reduction, was lower in FO than in RO when testing an activated sludge effluent. Cross-flow velocity, air-scouring, osmotic backwashing and effect of a spacer were compared to determine the most effective cleaning method for FO. After a long period of fouling with activated sludge, the flux was fully recovered in a short period of osmotic backwashing compared with cleaning by changing cross-flow velocity and air-scouring. In this study, the osmotic backwashing was found to be the most efficient way to clean the FO membrane. The amount of RNA recovered from FO membranes was about twice that for RO membranes; biofouling could be more significant in FO than in RO. However, the membrane fouling in FO was lower than that in RO. The spacer increased the flux in FO with activated sludge liquor suspended solids of 2,500 mg/L, and there were effects of spacer on performance of FO-MBR membrane fouling. However, further studies are required to determine how the spacer geometry influences on the performance of the FO membrane.
引用
收藏
页码:111 / 120
页数:10
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