2009
DOI: 10.1016/j.cej.2008.05.007
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Modelling a full scale UASB reactor using a COD global balance approach and state observers

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Cited by 21 publications
(10 citation statements)
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“…COD removal was 46.5 ± 0.41% and LCFA (mainly consisting of palmitic acid and oleic acid) was also consumed about 63.2% (Tables 6, and 7). The acidogenic bacteria in the first step consume the organic substrate and produce volatile fatty acids and CO 2 [11,26]. Wijekoon et al [27] reported the VFA profile variation in the two-stage thermophilic anaerobic membrane bioreactor.…”
Section: The Comparison Of One-stage and Two-stage Anaerobic Digestionmentioning
confidence: 98%
“…COD removal was 46.5 ± 0.41% and LCFA (mainly consisting of palmitic acid and oleic acid) was also consumed about 63.2% (Tables 6, and 7). The acidogenic bacteria in the first step consume the organic substrate and produce volatile fatty acids and CO 2 [11,26]. Wijekoon et al [27] reported the VFA profile variation in the two-stage thermophilic anaerobic membrane bioreactor.…”
Section: The Comparison Of One-stage and Two-stage Anaerobic Digestionmentioning
confidence: 98%
“…These authors assumed that in the first step, the acidogenic bacteria consume the organic substrate and produce volatile fatty acids and CO 2 (and more bacteria) and next, methanogenic population consumes these acids and produce methane and more microorganisms. The biomass growth obtained by these authors for this reactor gave values as low as 0.01 d -1 [22].…”
Section: Kinetic Evaluationmentioning
confidence: 99%
“…where: The following assumptions were made to obtain equation [2]: (1) A similar approach for separating the hydrolytic-acidogenic and methanogenic steps was developed by López and Borzacconi [22] to simulate an anaerobic digestion process in a full-scale upflow anaerobic sludge blanket reactor. These authors assumed that in the first step, the acidogenic bacteria consume the organic substrate and produce volatile fatty acids and CO 2 (and more bacteria) and next, methanogenic population consumes these acids and produce methane and more microorganisms.…”
Section: Kinetic Evaluationmentioning
confidence: 99%
“…Anaerobic Digestion Model Alternatives. A simpler model than ADM1 is the anaerobic system model identified as AM2, and this model was calibrated for a UASB reactor treating malting plant effluent by evaluating a COD mass balance to find the resulting stoichiometric coefficients (López and Borzacconi, 2009 Teissier's kinetic equations (Narayanan, 2009). The author observed that the model presents great flexibility and adequately predicts performance as shown by experimental values obtained and compared to model output.…”
Section: Anaerobic Digestion Modelmentioning
confidence: 99%