2016
DOI: 10.1016/j.biortech.2016.06.036
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Demonstration of a full-scale plant using an UASB followed by a ceramic MBR for the reclamation of industrial wastewater

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Cited by 47 publications
(8 citation statements)
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“…Expanded granular sludge bed (EGSB) was further developed to enhance substrate-biomass interaction within the treatment system by expanding the sludge bed and increasing hydraulic mixing compared to UASB (Niwa et al 2016;Cuff et al 2018). Although well-established UASB and/or EGSB configurations mostly meet the requirements necessary for anaerobic treatment, unfavourable conditions regarding the disintegration of granules led to the development of AnMBR by coupling membrane technology with anaerobic treatment.…”
Section: Brief Evolution Of Anaerobic Schemes As the Core Of The Biormentioning
confidence: 99%
“…Expanded granular sludge bed (EGSB) was further developed to enhance substrate-biomass interaction within the treatment system by expanding the sludge bed and increasing hydraulic mixing compared to UASB (Niwa et al 2016;Cuff et al 2018). Although well-established UASB and/or EGSB configurations mostly meet the requirements necessary for anaerobic treatment, unfavourable conditions regarding the disintegration of granules led to the development of AnMBR by coupling membrane technology with anaerobic treatment.…”
Section: Brief Evolution Of Anaerobic Schemes As the Core Of The Biormentioning
confidence: 99%
“…Sludge bed-based technologies, such as upflow anaerobic sludge blanket (UASB) reactors, have been widely used for MWT in full-scale WWTPs especially in tropical regions [8][9][10]. The AnMBRs, on the other hand, have been mainly applied for the treatment of high strength industrial wastewater [1,11].…”
Section: Introductionmentioning
confidence: 99%
“…However, the emergence of the new FS ceramic membranes, with a predicted life at least double that of the polymeric membranes and with a purportedly higher operating flux (Niwa et al, 2016), may change the paradigm of MBR membrane selection. Since the membrane replacement component of the OPEX relates to Lm/(J t) (Section 2.2.2), the cost effective ness of a novel candidate membrane compared with the conventional one is simply determined by the ratio of Lm/(J t) for the two materials.…”
Section: Discussionmentioning
confidence: 99%