Application of Coagulation-Membrane Rotation to Improve Ultrafiltration Performance in Drinking Water Treatment

被引:4
|
作者
Yu, Hongjian [1 ]
Huang, Weipeng [1 ]
Liu, Huachen [1 ]
Li, Tian [1 ,2 ,3 ]
Chi, Nianping [4 ]
Chu, Huaqiang [1 ,2 ,3 ]
Dong, Bingzhi [1 ,2 ,3 ]
机构
[1] Tongji Univ, Coll Environm Sci & Engn, Shanghai 200092, Peoples R China
[2] Tongji Univ, Minist Educ, Key Lab Yangtze River Water Environm, Shanghai 200092, Peoples R China
[3] Tongji Univ, State Key Lab Pollut Control & Resource Reuse, Shanghai 200092, Peoples R China
[4] Hunan City Univ, Sch Municipal & Geomat Engn, Yiyang 413000, Peoples R China
基金
上海市自然科学基金;
关键词
membrane rotation; coagulation; UF; dissolved organic matter; membrane fouling control; hydrodynamic shear stress; HOLLOW-FIBER MEMBRANES; FOULING CONTROL; HUMIC SUBSTANCES; PERMEATE FLUX; SHEAR-STRESS; LOW-PRESSURE; FILTRATION; VIBRATION; TRANSVERSE; BEHAVIOR;
D O I
10.3390/membranes11080643
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
The combination of conventional and advanced water treatment is now widely used in drinking water treatment. However, membrane fouling is still the main obstacle to extend its application. In this study, the impact of the combination of coagulation and ultrafiltration (UF) membrane rotation on both fouling control and organic removal of macro (sodium alginate, SA) and micro organic matters (tannic acid, TA) was studied comprehensively to evaluate its applicability in drinking water treatment. The results indicated that membrane rotation could generate shear stress and vortex, thus effectively reducing membrane fouling of both SA and TA solutions, especially for macro SA organics. With additional coagulation, the membrane fouling could be further reduced through the aggregation of mediate and macro organic substances into flocs and elimination by membrane retention. For example, with the membrane rotation speed of 60 r/min, the permeate flux increased by 90% and the organic removal by 35% in SA solution, with 40 mg/L coagulant dosage, with an additional 70% increase of flux and 5% increment of organic removal to 80% obtained. However, too much shear stress could intensify the potential of fiber breakage at the potting, destroying the flocs and resulting in the reduction of permeate flux and deterioration of effluent quality. Finally, the combination of coagulation and membrane rotation would lead to the shaking of the cake layer, which is beneficial for fouling mitigation and prolongation of membrane filtration lifetime. This study provides useful information on applying the combined process of conventional coagulation and the hydrodynamic shear force for drinking water treatment, which can be further explored in the future.
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页数:16
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