2013
DOI: 10.1016/j.cej.2013.01.098
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Biological nutrient removal in a continuous anaerobic–aerobic–anoxic process treating synthetic domestic wastewater

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Cited by 78 publications
(20 citation statements)
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“…At DO concentrations of 2 and 3.5 mg/l, the TN removal efficiency was increased with decreasing COD/N ratio which confirms the high capacity of this system for nitrogen removal. Table 9 compares the performance of this innovative system with other bioreactors applied for the simultaneous nutrients removal [13,14,23,25,[44][45][46][47][48]. It is clearly found from Table 9, single bioreactors with CFID regime shows more capability to remove CNP from wastewater relative to the other proposed single bioreactors.…”
Section: Effect Of Cod/n Ratiomentioning
confidence: 98%
“…At DO concentrations of 2 and 3.5 mg/l, the TN removal efficiency was increased with decreasing COD/N ratio which confirms the high capacity of this system for nitrogen removal. Table 9 compares the performance of this innovative system with other bioreactors applied for the simultaneous nutrients removal [13,14,23,25,[44][45][46][47][48]. It is clearly found from Table 9, single bioreactors with CFID regime shows more capability to remove CNP from wastewater relative to the other proposed single bioreactors.…”
Section: Effect Of Cod/n Ratiomentioning
confidence: 98%
“…The non-aeration cycle must be long enough to allow the process to enter into an anaerobic stage which promotes Enhance Biological Phosphorous Removal (EBPR) [23,24], in which Polyphosphate Accumulating Organisms (PAO) consume organic matter by transforming it into polyhidroxyalcalanoates (PHA) and release phosphorous into the reactor. It will be subsequently A value lower than this threshold points to a low oxygen consumption rate, which means that there is a low organic matter concentration in the reactor.…”
Section: Aeration Controlmentioning
confidence: 99%
“…Complete removal of total Kjeldahl Nitrogen (TKN) is practically unachievable in the WWTP's having a preanaerobic system, wherein the anaerobic reactor is positioned behind the aerobic reactor and the mixed liquor involving nitrate is recirculated to the aerobic reactor from the secondary clarifier. The nitrate recirculation rate needs to be intensified, so as to improve the TKN removal efficiency, which steers to higher power consumption and dissolved oxygen (DO) return from the aerobic reactor (Liu et al 2013).…”
Section: Description Of Wwtp and Data Analysismentioning
confidence: 99%
“…Nitrogen mainly occurs in wastewater in the TKN form. After biological wastewater treatment, TKN mostly appears as oxidized nitrite (Liu et al 2013).…”
Section: Introductionmentioning
confidence: 99%