2015
DOI: 10.1016/j.watres.2015.08.030
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Effect of particulate organic substrate on aerobic granulation and operating conditions of sequencing batch reactors

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Cited by 98 publications
(54 citation statements)
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References 35 publications
(58 reference statements)
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“…Other authors indicated that to achieve granulation on actual industrial wastewater a longer time is required(Wagner et al, 2015).The granules formation in the present study may have been enhanced by the biofilm detachment present in the effluent of the anaerobic pre-treatment system(Yu et al, 2013). The inactive cells and particulate material in suspension could have acted as aggregation nuclei for granular structure development.Aerobic granules were characterized by a yellow-brownish appearance with a regular and smooth surface.…”
mentioning
confidence: 62%
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“…Other authors indicated that to achieve granulation on actual industrial wastewater a longer time is required(Wagner et al, 2015).The granules formation in the present study may have been enhanced by the biofilm detachment present in the effluent of the anaerobic pre-treatment system(Yu et al, 2013). The inactive cells and particulate material in suspension could have acted as aggregation nuclei for granular structure development.Aerobic granules were characterized by a yellow-brownish appearance with a regular and smooth surface.…”
mentioning
confidence: 62%
“…The rate of SCOD converted into intracellular polymers was not evaluated in this study. Afterwards, another increasing trend was observed (from the 75 th min to 4h) which represents the hydrolysis and uptake of PCOD into TB-EPS storage for further metabolic degradation (Wagner et al, 2015). After 4h, the TB-EPS content started decreasing because bacteria in the absence of external carbon source consumed EPS to produce energy for their metabolism.…”
Section: Eps Variation During the Cyclementioning
confidence: 99%
“…Ultimately, it resulted in reduced COD and nutrient removal efficiency due to limited storage of organic material in the inner part of the granule. Wagner et al ( 2015 ) compared AGS reactors operated with only soluble carbon (acetate and hydrolyzed peptone) and with soluble and particulate carbon (particulate starch). In the presence of particles, the anaerobic phase had to be prolonged to allow for substrate hydrolysis.…”
Section: Process Configurations and Operational Conditions Affectingmentioning
confidence: 99%
“…It is generally assumed that since the rate of anaerobic hydrolysis is relatively low; thus, to benefit from hydrolysis of pCOD the anaerobic condition should be extended (Grady et al, ). However, Wagner et al () reported that in an anaerobic/aerobic granular activated sludge‐SBR system with rbCOD deficiency, extending anaerobic HRT from 1 to 1.5 h did not improve phosphorous removal performance. With regard to activated sludge modeling (Henze et al, ) in ASM1, the rate of anaerobic hydrolysis is zero.…”
Section: Introductionmentioning
confidence: 99%