Evaluation of a Hybrid Moving Bed Biofilm Membrane Bioreactor and a Direct Contact Membrane Distillation System for Purification of Industrial Wastewater

被引:1
|
作者
Alharthi, Mamdouh S. [1 ]
Bamaga, Omar [2 ]
Abulkhair, Hani [1 ,2 ]
Organji, Husam [2 ]
Shaiban, Amer [2 ]
Macedonio, Francesca [3 ]
Criscuoli, Alessandra [3 ]
Drioli, Enrico [3 ]
Wang, Zhaohui [4 ]
Cui, Zhaoliang [4 ]
Jin, Wanqin [4 ]
Albeirutty, Mohammed [1 ,2 ]
机构
[1] King Abdulaziz Univ, Dept Mech Engn, POB 80200, Jeddah 21589, Saudi Arabia
[2] King Abdulaziz Univ, Ctr Excellence Desalinat Technol, POB 80200, Jeddah 21589, Saudi Arabia
[3] Natl Res Council Italy CNR ITM, Inst Membrane Technol, Via P Bucci 17-C, I-87036 Arcavacata Di Rende, Italy
[4] Nanjing Tech Univ, Coll Chem Engn, State Key Lab Mat Oriented Chem Engn, Nanjing 211816, Peoples R China
关键词
industrial wastewater; moving bed biofilm reactor; membrane bioreactor; membrane distillation; hybrid process; SALINITY; TECHNOLOGIES; PERFORMANCE; DRIVERS; REUSE; MBR;
D O I
10.3390/membranes13010016
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
Integrated wastewater treatment processes are accepted as the best option for sustainable and unrestricted onsite water reuse. In this study, moving bed biofilm reactor (MBBR), membrane bioreactor (MBR), and direct contact membrane distillation (DCMD) treatment steps were integrated successively to obtain the combined advantages of these processes for industrial wastewater treatment. The MBBR step acts as the first step in the biological treatment and also mitigates foulant load on the MBR. Similarly, MBR acts as the second step in the biological treatment and serves as a pretreatment prior to the DCMD step. The latter acts as a final treatment to produce high-quality water. A laboratory scale integrated MBBR/MBR/DCMD experimental system was used for assessing the treatment efficiency of primary treated (PTIWW) and secondary treated (STIWW) industrial wastewater in terms of permeate water flux, effluent quality, and membrane fouling. The removal efficiency of total dissolved solids (TDS) and effluent permeate flux of the three-step process (MBBR/MBR/DCMD) were better than the two-step (MBR/DCMD) process. In the three-step process, the average removal efficiency of TDS was 99.85% and 98.16% when treating STIWW and PTIWW, respectively. While in the case of the two-step process, the average removal efficiency of TDS was 93.83% when treating STIWW. Similar trends were observed for effluent permeate flux values which were found, in the case of the three-step process, 62.6% higher than the two-step process, when treating STIWW in both cases. Moreover, the comparison of the quality of the effluents obtained with the analysed configurations with that obtained by Jeddah Industrial Wastewater Treatment Plant proved the higher performance of the proposed membrane processes.
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页数:17
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