A novel loosely structured nanofiltration membrane bioreactor for wastewater treatment: Process performance and membrane fouling

被引:22
|
作者
Cao, Lei [1 ]
Zhang, Yufeng [1 ,2 ,3 ,5 ]
Ni, Lei [1 ]
Feng, Xianshe [4 ]
机构
[1] Tiangong Univ, Sch Mat Sci & Engn, State Key Lab Separat Membranes & Membrane Proc, Tianjin 300387, Peoples R China
[2] Tianjin Chengjian Univ, Sch Environm & Municipal Engn, Tianjin Key Lab Aquat Sci & Technol, Tianjin 300384, Peoples R China
[3] Tianjin Chengjian Univ, Joint Res Ctr Protect Infrastructure Technol & Env, Dept Environm & Municipal Engn, Tianjin 300384, Peoples R China
[4] Univ Waterloo, Dept Chem Engn, Waterloo, ON N2L 3G1, Canada
[5] Tiangong Univ, Sch Mat Sci & Engn, State Key Lab Separat Membranes & Membrane Proc, 399 Binshui Xi Rd, Tianjin 300387, Peoples R China
基金
国家高技术研究发展计划(863计划);
关键词
NF-MBR; Loose NF membrane; Critical flux; Transmembrane pressure; Biofouling layer; DISSOLVED ORGANIC-MATTER; HOLLOW-FIBER MEMBRANES; NF-MBR; LANDFILL LEACHATE; CAKE LAYER; HYBRID; REMOVAL; FLUX; TECHNOLOGY; BIOFILM;
D O I
10.1016/j.memsci.2021.120128
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A novel nanofiltration membrane bioreactor (NF-MBR) was constructed by integrating a loosely structured nanofiltration hollow fiber membrane into an aerobic activated sludge system. In order to verify the feasibility of loose NF membrane bioreactor, parallel experiments of conventional ultrafiltration membrane bioreactor (UF-MBR) and NF-MBR were conducted to investigate process performances, membrane fouling characteristics. The loose NF membrane showed a relatively high permeability at a level of around 10 L m(-2) h(-1) bar(-1) (flux of 2.0 L m(-2) h(-1)) under low operation pressure (10-30 KPa). The results showed that NF-MBR achieved a higher removal efficiency of chemical oxygen demand (CODCr) and dissolved organic carbon (DOC) due to high rejection of loose NF membrane for biopolymers and part of the humic substances. During long term operation in NF-MBR, loose NF membrane displayed low salt rejection, resulting in no obvious salts accumulation in bioreactor in comparison with UF-MBR. The average rising rates in TMP for the NF-MBR was 0.16 KPa/day, which was twice lower than that of UF-MBR. The results of fouling mechanism showed that reversible cake fouling was dominant for both NF and UF membranes, while the relatively small pore size of the NF membrane mitigated irreversible pore blockage. Further biofouling layer analysis demonstrated that humic substances, polysaccharides and proteins were the main organic foulants. The results of energy consumption revealed that NF-MBR had comparable total energy consumption compared with UF-MBR. The outcomes of this study show the feasibility of loose NF membrane bioreactor to provide a great potential as an advanced process for wastewater treatment.
引用
收藏
页数:16
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