Influence of relaxation modes on membrane fouling in submerged membrane bioreactor for domestic wastewater treatment

被引:53
作者
Habib, Rasikh [1 ]
Asif, Muhammad Bilal [1 ,2 ]
Iftekhar, Sidra [1 ,3 ]
Khan, Zahiruddin [4 ]
Gurung, Khum [3 ]
Srivastava, Varsha [3 ]
Sillanpaa, Mika [3 ,5 ]
机构
[1] Univ Engn & Technol, Dept Environm Engn, Taxila 47050, Pakistan
[2] Univ Wollongong UOW, Sch Civil Min & Environm Engn, Strateg Water Infrastruct Lab, Wollongong, NSW 2522, Australia
[3] Lappeenranta Univ Technol, Sch Engn Sci, Lab Green Chem, Sammonkatu 12, FI-50130 Mikkeli, Finland
[4] Govt Punjab, Punjab Saaf Pani Co, Lahore 54000, Pakistan
[5] Florida Int Univ, Dept Civil & Environm Engn, Miami, FL 33174 USA
关键词
Fouling resistances; Membrane fouling rate; Relaxation modes; Soluble microbial products; Submerged membrane bioreactor; NUTRIENT REMOVAL; MBR; OPERATION; PERFORMANCE; REVERSIBILITY; SUBSTANCES; PARAMETERS; QUALITY; SURFACE; CAKE;
D O I
10.1016/j.chemosphere.2017.04.048
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Relaxation and backwashing have become an integral part of membrane bioreactor (MBR) operations for fouling control. This study was carried out on real municipal wastewater to evaluate the influence of different operational strategies on membrane fouling at equivalent water yield. Four relaxation modes (MBR10+0, MBR10+1, MBR10.+1.5 and MBR10+2) were tested to analyze membrane fouling behavior. For the optimization of relaxation modes, fouling rate in terms of trans-membrane pressure, hydraulic resistances and characteristics of fouling fractions were analyzed. It has been observed that cake layer resistance was minimum in MBR10-1.5 but pore blockage resistance was increased in all relaxation modes. Moreover, high instantaneous flux contributed significantly to fouling rate at the initial stage of MBR operations. Relaxation modes were also efficient in removing irreversible fouling to some extent. Under all relaxation modes, COD removal efficiency ranged from 92 to 96.5%. Ammonium and TP removal were on the lower side due to the short solids and hydraulic retention time. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:19 / 25
页数:7
相关论文
共 50 条
[1]   Evaluation of fouling deposition, fouling reversibility and energy consumption of submerged hollow fiber membrane systems with periodic backwash [J].
Akhondi, Ebrahim ;
Wicaksana, Filicia ;
Fane, Anthony Gordon .
JOURNAL OF MEMBRANE SCIENCE, 2014, 452 :319-331
[2]  
[Anonymous], 2005, Standard methods for the examination of water and waste- water
[3]  
[Anonymous], 1991, WASTEWATER ENG TREAT
[4]   The role of EPS in the foaming and fouling for a MBR operated in intermittent aeration conditions [J].
Campo, Riccardo ;
Capodici, Marco ;
Di Bella, Gaetano ;
Torregrossa, Michele .
BIOCHEMICAL ENGINEERING JOURNAL, 2017, 118 :41-52
[5]   Fouling transients in nominally sub-critical flux operation of a membrane bioreactor [J].
Cho, BD ;
Fane, AG .
JOURNAL OF MEMBRANE SCIENCE, 2002, 209 (02) :391-403
[6]   Effect of organic loading on the performance of MBR for advanced treatment and water reuse [J].
Cho, Yoon-Ho ;
Sibag, Mark L. ;
Eusebio, Ramon Christian ;
Kim, Han-Seung .
DESALINATION AND WATER TREATMENT, 2011, 33 (1-3) :224-230
[7]   A comparison study on membrane fouling in a sponge-submerged membrane bioreactor and a conventional membrane bioreactor [J].
Deng, Lijuan ;
Guo, Wenshan ;
Ngo, Huu Hao ;
Zhang, Jian ;
Liang, Shuang ;
Xia, Siqing ;
Zhang, Zhiqiang ;
Li, Jianxin .
BIORESOURCE TECHNOLOGY, 2014, 165 :69-74
[8]   A COLORIMETRIC METHOD FOR THE DETERMINATION OF SUGARS [J].
DUBOIS, M ;
GILLES, K ;
HAMILTON, JK ;
REBERS, PA ;
SMITH, F .
NATURE, 1951, 168 (4265) :167-167
[9]   The impact of different operating conditions on membrane fouling and EPS production [J].
Dvorak, Lukas ;
Gomez, Marcel ;
Dvorakova, Marketa ;
Ruzickova, Iveta ;
Wanner, Jiri .
BIORESOURCE TECHNOLOGY, 2011, 102 (13) :6870-6875
[10]   Effects of aeration parameters on effluent quality and membrane fouling in a submerged membrane bioreactor using Box-Behnken response surface methodology [J].
Fu, Hai-Yan ;
Xu, Peng-Cheng ;
Huang, Guo-He ;
Chai, Tian ;
Hou, Ming ;
Gao, Pan-Feng .
DESALINATION, 2012, 302 :33-42