2013
DOI: 10.1016/j.rser.2012.11.056
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Energy recovery from wastewaters with high-rate anaerobic digesters

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Cited by 152 publications
(53 citation statements)
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“…Further advantages, possibly improving demand-driven gas production and thereby enhancing the scale of exibility compared to single-stage AD, are that the hydrolysis as rate limiting step ) is decoupled from methanogenesis, thereby enabling a shift of the gas production into times of higher demand, selective production of certain intermediates in the AR by controlling pH and redoxpotential , generally higher process stability and ruggedness against shock loads , operation of the MR at much higher OLRs than CSTRs and the possibility to keep the MR in dormancy (Tauseef et al, 2013).…”
Section: Two-staged Anaerobic Digestionmentioning
confidence: 99%
“…Further advantages, possibly improving demand-driven gas production and thereby enhancing the scale of exibility compared to single-stage AD, are that the hydrolysis as rate limiting step ) is decoupled from methanogenesis, thereby enabling a shift of the gas production into times of higher demand, selective production of certain intermediates in the AR by controlling pH and redoxpotential , generally higher process stability and ruggedness against shock loads , operation of the MR at much higher OLRs than CSTRs and the possibility to keep the MR in dormancy (Tauseef et al, 2013).…”
Section: Two-staged Anaerobic Digestionmentioning
confidence: 99%
“…For example, the amino acids from protein degradation contain a carboxylic group (acid) and an amine group (base) which are able to buffer the pH to near 5 (Fennema et al, 2010). According to Tauseef et al (2013), the recommended alkalinity for biomethanation is between 2,500 and 4,500 mg CaCO3.L -1 .…”
Section: Fermentation Of the Synthetic Effluentmentioning
confidence: 99%
“…In terms of sludge production, for most wastewaters, the net sludge yield from aerobic activated sludge treatment is of the order of 0.5 kg of volatile suspended solid (VSS) per kg COD removed as opposed to less than 0.1 kg VSS per kg COD removed sludge yield from anaerobic treatment [1]. If the two systems are combined, anaerobic and aerobic processes can generate lesser amounts of sludge and the overall cost of waste treatment can be considerably reduced.…”
Section: Combined Anaerobic-aerobic Treatment Systemmentioning
confidence: 99%