Advanced Membrane Bioreactors for Wastewater Treatment

A special issue of Membranes (ISSN 2077-0375). This special issue belongs to the section "Membrane Processing and Engineering".

Deadline for manuscript submissions: closed (20 February 2022) | Viewed by 14215

Special Issue Editors


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Guest Editor
European Institute of Membranes, IEM, University of Montpellier, CNRS, ENSCM, 34090 Montpellier, France
Interests: high-level removal of micropollutants and resource recovery for wastewater reuse application; energy production from anaerobic digestion of organic content of domestic wastewaters; insights into the complexity of dissolved and colloidal organic matter origin; fate and behavior in biological processes (aerobic and anaerobic) combined to membrane separation
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Guest Editor
Department of chemical engineering, IUT GON, France UR ABTE (Aliments Bioprocédés Toxicologie Environnements) EcoTEA, University of Caen Normandy, Caen, France
Interests: membrane separation; membrane bioreactors; anaerobic digestion; modelling; wastewater treatment
Special Issues, Collections and Topics in MDPI journals

Special Issue Information

Dear Colleagues,

MBR is an efficient technology for industrial and domestic wastewater treatment which combine membrane filtration system and activated sludge biological treatment. MBR technology seems to be a good choice as most of the solids including bacteria will completely be eliminated through membrane separation which enables the final effluent to be directly discharge to the surface water or more easily post-treated for wastewater reuse applications. Major limitations for the widespread application of Membrane Bioreactors (MBR) is membrane fouling and energy consumption. Membrane fouling reduces plant productivity, shortens membrane lifetime, increases energy consumption and the need for chemical cleaning.

This Special Issue on “Advanced Membrane Bioreactors for Wastewater Treatment” of the journal Membranes seeks contributions to assess the state-of-the-art and future developments in the field of advanced membrane bioreactors. Topics include, but are not limited to fouling characterization, new fouling mitigation strategies (quorum quenching, mechanical cleaning processes,…), Anaerobic MBR, Biofilm MBR, new membrane materials for MBR, gravity driven MBR, hybrid MBR, micro-pollutants issues, theory, modelling, design, management and applications of advanced membrane bioreactors. Authors are invited to submit their latest results; both original papers and reviews are welcome.

Dr. Geoffroy Lesage
Dr. Amine Charfi
Guest Editors

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Keywords

  • Membrane bioreactors
  • Low-energy wastewater treatment
  • Wastewater reuse
  • Fouling
  • Ultrafiltration

Published Papers (5 papers)

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Research

24 pages, 3911 KiB  
Article
Hollow-Fiber Membrane Contactor for Biogas Recovery from Real Anaerobic Membrane Bioreactor Permeate
by Qazi Sohaib, Carla Kalakech, Christophe Charmette, Jim Cartier, Geoffroy Lesage and Jean-Pierre Mericq
Membranes 2022, 12(2), 112; https://doi.org/10.3390/membranes12020112 - 19 Jan 2022
Cited by 11 | Viewed by 2908
Abstract
This study demonstrates the application of hollow-fiber membrane contactors (HFMCs) for the recovery of biogas from the ultrafiltration permeate of an anaerobic membrane bioreactor (AnMBR) and synthetic effluents of pure and mixed CH4 and CO2. The developed membrane degassing setup [...] Read more.
This study demonstrates the application of hollow-fiber membrane contactors (HFMCs) for the recovery of biogas from the ultrafiltration permeate of an anaerobic membrane bioreactor (AnMBR) and synthetic effluents of pure and mixed CH4 and CO2. The developed membrane degassing setup was coupled with a pilot-scale AnMBR fed with synthetic domestic effluent working at 25 °C. The membrane degassing unit was able to recover 93% of the total dissolved CH4 and 83% of the dissolved CO2 in the first two hours of permeate recirculation. The initial recovery rates were very high (0.21 mg CH4 L−1 min−1 and 8.43 mg CO2 L−1 min−1) and the membrane was able to achieve a degassing efficiency of 95.7% for CH4 and 76.2% for CO2, at a gas to liquid ratio of 1. A higher mass transfer coefficient of CH4 was found in all experimental and theoretical evaluations compared to CO2. This could also be confirmed from the higher transmembrane mass transport resistance to CO2 rather than CH4 found in this work. A strong dependency of the selective gas transport on the gas and liquid side hydrodynamics was observed. An increase in the liquid flow rate and gas flow rate favored CH4 transport and CO2 transport, respectively, over each component. The results confirmed the effectiveness of the collective AnMBR and membrane degassing setup for biogas recovery. Still, additional work is required to improve the membrane contactor’s performance for biogas recovery during long-term operation. Full article
(This article belongs to the Special Issue Advanced Membrane Bioreactors for Wastewater Treatment)
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16 pages, 2058 KiB  
Article
Effect of Different Influent Conditions on Biomass Production and Nutrient Removal by Aeration Microalgae Membrane Bioreactor (ICFB-MMBR) System for Mariculture Wastewater Treatment
by Yi Ding, Shiyuan Wang, Hang Ma, Binyu Ma, Zhansheng Guo, Hong You, Junxue Mei, Xuguang Hou, Zhenlin Liang and Zhipeng Li
Membranes 2021, 11(11), 874; https://doi.org/10.3390/membranes11110874 - 14 Nov 2021
Cited by 5 | Viewed by 2220
Abstract
The nutrient removal and biomass production of the internal circulating fluidized bed microalgae membrane bioreactor (ICFB-MMBR) was studied under different cultivation modes, influent TOC, influent pH, and influent N/P. Platymonas helgolandica tsingtaoensis was used as the biological source. The growth of P. helgolandica [...] Read more.
The nutrient removal and biomass production of the internal circulating fluidized bed microalgae membrane bioreactor (ICFB-MMBR) was studied under different cultivation modes, influent TOC, influent pH, and influent N/P. Platymonas helgolandica tsingtaoensis was used as the biological source. The growth of P. helgolandica tsingtaoensis and the removal efficiency of pollutants in the mixotrophy culture mode were improved compared with other culture modes. With the increased influent TOC, the average growth rate of P. helgolandica tsingtaoensis increased, and ammonia nitrogen and total phosphorus removal rate were improved. The P. helgolandica tsingtaoensis growth rate and nutrient removal efficiencies at the influent pH of 8 were the best among the different influent pH values. As the influent N/P ratio increased from 5 to 20, the P. helgolandica tsingtaoensis growth rate and pollutant removal rate increased gradually. When the influent N/P ratio was higher than 20, the P. helgolandica tsingtaoensis growth rate and pollutant removal rate tended to be stable and did not significantly change with the increase of influent N/P ratio. At the proper influent conditions, the high P. helgolandica tsingtaoensis biomass and nutrient removal efficiency could be obtained in the microalgae membrane bioreactor, which could provide a theoretical basis for the application of the system for wastewater treatment. Full article
(This article belongs to the Special Issue Advanced Membrane Bioreactors for Wastewater Treatment)
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22 pages, 14458 KiB  
Article
Assessment of an Integrated and Sustainable Multistage System for the Treatment of Poultry Slaughterhouse Wastewater
by Phumeza Akhona Dyosile, Cebisa Mdladla, Mahomet Njoya, Moses Basitere, Seteno Karabo Obed Ntwampe and Ephraim Kaskote
Membranes 2021, 11(8), 582; https://doi.org/10.3390/membranes11080582 - 30 Jul 2021
Cited by 4 | Viewed by 2642
Abstract
This paper assesses the performance of an integrated multistage laboratory-scale plant, for the treatment of poultry slaughterhouse wastewater (PSW). The system was comprised of an eco-flush dosed bio-physico pre-treatment unit for fats, oil, and grease (FOG) hydrolysis prior to the PSW being fed [...] Read more.
This paper assesses the performance of an integrated multistage laboratory-scale plant, for the treatment of poultry slaughterhouse wastewater (PSW). The system was comprised of an eco-flush dosed bio-physico pre-treatment unit for fats, oil, and grease (FOG) hydrolysis prior to the PSW being fed to a down-flow expanded granular bed reactor (DEGBR), coupled to a membrane bioreactor (DEGBR-MBR). The system’s configuration strategy was developed to achieve optimal PSW treatment by introducing the enzymatic pre-treatment unit for the lipid-rich influent (PSW) in order to treat FOG including odour causing constituents such as H2S known to sour anaerobic digestion (AD) such that the PSW pollutant load is alleviated prior to AD treatment. This was conducted to aid the reduction in clogging and sludge washout in the DEGBR-MBR systems and to achieve the optimum reactor and membrane system performance. A performance for the treatment of PSW after lipid reduction was conducted through a qualitative analysis by assessing the pre- and post-pre-treatment units’ chemical oxygen demand (COD), total suspended solids (TSS), and FOG concentrations across all other units and, in particular, the membrane units. Furthermore, a similar set-up and operating conditions in a comparative study was also performed. The pre-treatment unit’s biodelipidation abilities were characterised by a mean FOG removal of 80% and the TSS and COD removal reached 38 and 56%, respectively. The final acquired removal results on the DEGBR, at an OLR of ~18–45 g COD/L.d, was 87, 93, and 90% for COD, TSS, and FOG, respectively. The total removal efficiency across the pre-treatment-DEGBR-MBR units was 99% for COD, TSS, and FOG. Even at a high OLR, the pre-treatment-DEGBR-MBR train seemed a robust treatment strategy and achieved the effluent quality set requirements for effluent discharge in most countries. Full article
(This article belongs to the Special Issue Advanced Membrane Bioreactors for Wastewater Treatment)
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17 pages, 1964 KiB  
Article
Assessment of an Anaerobic Membrane Bioreactor (AnMBR) Treating Medium-Strength Synthetic Wastewater under Cyclical Membrane Operation
by Ahmet E. Uman, Robert A. Bair and Daniel H. Yeh
Membranes 2021, 11(6), 415; https://doi.org/10.3390/membranes11060415 - 31 May 2021
Cited by 6 | Viewed by 3402
Abstract
A lab-scale (6.2 L) anaerobic membrane bioreactor combined with a tubular, cross-flow, PVDF ultrafiltration membrane was developed and operated to assess the long-term fouling behavior of a cyclically operated anaerobic membrane bioreactor (AnMBR). The AnMBR was operated at 35 ± 1 °C for [...] Read more.
A lab-scale (6.2 L) anaerobic membrane bioreactor combined with a tubular, cross-flow, PVDF ultrafiltration membrane was developed and operated to assess the long-term fouling behavior of a cyclically operated anaerobic membrane bioreactor (AnMBR). The AnMBR was operated at 35 ± 1 °C for 200 days with a synthetic influent of 501 mg·L−1 COD to mimic municipal wastewater. The system exhibited high treatment performance with an average COD removal efficiency of 86.5 ± 6.4% (n = 20) and an average permeate COD concentration of 63.9 ± 31.1 mg·L−1. A clear permeate with an average turbidity of 0.6 ± 0.2 NTU, was achieved. Permeate TN and TP concentrations were 22.7 ± 5.1 mg·L−1 and 6.9 ± 2.0 mg·L−1 corresponding to removal efficiencies of 20.6% and 49.3%, respectively, likely due to membrane rejection of particulate, colloidal, and organic fractions. A stable membrane flux of 4.3 L.m−2.h−1 (LMH) was maintained for 183 days without gas-lift, gas sparge, or chemical cleaning. Cyclical operation with frequent relaxation (60 s for every 30 min of the permeate production run) and periodic permeate backwash (15 s for every 186 min) maintained stable membrane operation with an average TMP of 0.25 bar and a fouling rate of 0.007 kPa/h for the entire operating period. The comparison revealed frequent backwashing and relaxation is a sustainable strategy for operation of the AnMBR. Full article
(This article belongs to the Special Issue Advanced Membrane Bioreactors for Wastewater Treatment)
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15 pages, 2054 KiB  
Article
Development of a Short-Cut Combined Magnetic Coagulation–Sequence Batch Membrane Bioreactor for Swine Wastewater Treatment
by Yanlin Chen, Qianwen Sui, Dawei Yu, Libing Zheng, Meixue Chen, Tharindu Ritigala and Yuansong Wei
Membranes 2021, 11(2), 83; https://doi.org/10.3390/membranes11020083 - 23 Jan 2021
Cited by 12 | Viewed by 2182
Abstract
A high concentration of suspended solids (SS) in swine wastewater reduces the efficiency of the biological treatment process. The current study developed a short-cut combined magnetic coagulation (MC)–sequence batch membrane bioreactor (SMBR) process to treat swine wastewater. Compared with the single SMBR process, [...] Read more.
A high concentration of suspended solids (SS) in swine wastewater reduces the efficiency of the biological treatment process. The current study developed a short-cut combined magnetic coagulation (MC)–sequence batch membrane bioreactor (SMBR) process to treat swine wastewater. Compared with the single SMBR process, the combined process successfully achieved similarly high removal efficiencies of chemical oxygen demand (COD), total nitrogen (TN), ammonium nitrogen (NH4+-N), and total phosphorous (TP) of 96.0%, 97.6%, 99.0%, and 69.1%, respectively, at dosages of 0.5 g/L of poly aluminium chloride (PAC), 2 mg/L of polyacrylamide (PAM), and 1 g/L of magnetic seeds in Stage II, and concentrations of TN, COD, and NH4+-N in effluent can meet the discharge standards for pollutants for livestock and poultry breeding (GB18596-2001, China). The nitrogen removal loading (NRL) was increased from 0.21 to 0.28 kg/(m3·d), and the hydraulic retention time (HRT) was shortened from 5.0 days to 4.3 days. High-throughput sequencing analysis was carried out to investigate microbial community evolution, and the results showed that the relative abundance of ammonia-oxidizing bacteria (AOB) in the SMBR increased from 0.1% without pre-treatment to 1.78% with the pre-treatment of MC. Full article
(This article belongs to the Special Issue Advanced Membrane Bioreactors for Wastewater Treatment)
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