2017
DOI: 10.1016/j.watres.2017.08.058
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Hydrolysis of particulate settleable solids (PSS) in activated sludge is determined by the bacteria initially adsorbed in the sewage

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Cited by 24 publications
(9 citation statements)
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“…The remaining particulate carbohydrates might keep hydrolyzing during feeding to the reactor; during a 1-h feeding period, a maximum of 10% of the total carbohydrates could be degraded by the enzymes in the influent. A previous study suggested that the hydrolysis of influent suspended solids would be mainly performed by microorganisms in the influent (Benneouala et al 2017 ). Besides, a recent study on the microbial composition of the wastewater treatment plant of Garmerwolde identified several hydrolyzing microorganisms in the influent (Ali et al 2019 ).…”
Section: Discussionmentioning
confidence: 99%
“…The remaining particulate carbohydrates might keep hydrolyzing during feeding to the reactor; during a 1-h feeding period, a maximum of 10% of the total carbohydrates could be degraded by the enzymes in the influent. A previous study suggested that the hydrolysis of influent suspended solids would be mainly performed by microorganisms in the influent (Benneouala et al 2017 ). Besides, a recent study on the microbial composition of the wastewater treatment plant of Garmerwolde identified several hydrolyzing microorganisms in the influent (Ali et al 2019 ).…”
Section: Discussionmentioning
confidence: 99%
“…On the contrary, the high proportions of non-diffusible X B in the influent of R3 and R4 hampered the granulation process. Several phenomena lead to the conclusion that hydrolysis is only partial during anaerobic plug-flow feeding: (1) WW particles are often large, from several μm up to 1–2 mm (Levine et al., 1985; Dimock and Morgenroth, 2006), (2) hydrolysis is a very slow process (Benneouala et al., 2017; Morgenroth et al., 2002; Jabari et al., 2016), and (3) the anaerobic feeding duration of 1–2 h typically applied in AGS systems is insufficient to provide full hydrolysis of X B (Wagner et al., 2015; Jabari et al., 2016). Therefore partial anaerobic conversion of X B is unavoidable and results in a high availability of substrate during the subsequent aerobic phase, which in turn supports the growth of OHO (Wagner et al., 2015).…”
Section: Discussionmentioning
confidence: 99%
“…Importantly, particulate, colloidal COD and soluble macromolecules constitute a large proportion of the organics pool in biological wastewater treatment (Figure S19), hydrolysis, and acidogenic fermentation of such organics can increase the availability of rbCOD or VFAs for PAOs but they are usually the overall rate-limiting steps. 53 Given the slow growth of HFB in non-EBPR plants, their immigration from the influent microflora is the major determinant for improved phosphorus removal by intensifying their cooperation with PAOs. It should be noted that the much higher sludge concentrations of MBRs over conventional activated sludge processes would also play a role in generating anaerobic pockets within the sludge, promoting the activity of these HFB.…”
Section: ■ Discussionmentioning
confidence: 99%
“…In addition, the long SRT of sewer biofilm communities could lead to the improvement of hydrolysis/fermentation . Moreover, Benneouala et al found that hydrolysis/fermentation process appeared to be more governed by the bacteria initially adsorbed in the influent wastewater than by the activated sludge community . Overall, the influent microflora played a key role in the hydrolysis/fermentation process in the downstream sludge community.…”
Section: Discussionmentioning
confidence: 99%