2016
DOI: 10.1016/j.memsci.2016.01.010
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Osmotic membrane bioreactor (OMBR) technology for wastewater treatment and reclamation: Advances, challenges, and prospects for the future

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Cited by 229 publications
(118 citation statements)
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“…Mg 2+ and Ca 2+ sources and pH adjustment methods would be required to achieve the initial conditions for the precipitation process, while the performance of these systems could be affected by several parameters. Influent quality, hydraulic load, salinity, membrane fouling (organic, inorganic, or biological fouling) are the most important ones [60,74].…”
Section: Membrane Technologiesmentioning
confidence: 99%
“…Mg 2+ and Ca 2+ sources and pH adjustment methods would be required to achieve the initial conditions for the precipitation process, while the performance of these systems could be affected by several parameters. Influent quality, hydraulic load, salinity, membrane fouling (organic, inorganic, or biological fouling) are the most important ones [60,74].…”
Section: Membrane Technologiesmentioning
confidence: 99%
“…Forward osmosis has recently been implemented in osmotic MBRs (Wang et al, 2016), which show effectiveness in combating membrane fouling. Novel membrane types that are designed to pose minimum fouling propensity is also effective Kharraz et al, 2015;Marbelia et al, 2016).…”
Section: Research Perspectivesmentioning
confidence: 99%
“…For instance, the low SRSF values of SOA, KH 2 PO 4 and MAP are most likely related to their low B parameters (i.e., 0.022, 0.029 and 0.024 kg·m 2 ·h −1 , respectively). A draw solution exhibiting a lower SRSF would be the preferred option for this hybrid MF-FDFO-MBR system since the accumulation of inorganic salt ions in the bioreactor could potentially inhibit the aerobic microbial activity [14]. For that reason, SOA or KH 2 PO 4 would be more suitable for this process.…”
Section: Effect Of Different Types Of Fertilizersmentioning
confidence: 99%
“…The high rejection of FO membrane can therefore provide a better rejection of contaminants and retain a significant portion of suspended solids; which is another advantage of this OMBR system compared to the conventional ones. However, OMBR also has some limitations such as salinity build-up (i.e., accumulation of dissolved salts inside the bioreactor), internal concentration polarization and the energy associated with the draw solution recovery process [13][14][15]. This is due to the combination of high rejection of FO membrane which rejects the salts already present in the bioreactor and those coming from the wastewater feed solution and the reverse transport of salt from the draw solution to the bioreactor passing through the FO membrane [16,17].…”
Section: Introductionmentioning
confidence: 99%