2006
DOI: 10.1590/s1516-89132006000500018
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Simple models for the continuous aerobic biodegradation of phenol in a packed bed reactor

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Cited by 12 publications
(9 citation statements)
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References 20 publications
(16 reference statements)
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“…The model presented by Gerrard et al (2006) was used to model the bioconversion of Cr(VI) in a packed bed reactor [36]. The design equation for packed bed reactor with plug flow is given as:…”
Section: Kinetics Studies For Column Experimentsmentioning
confidence: 99%
“…The model presented by Gerrard et al (2006) was used to model the bioconversion of Cr(VI) in a packed bed reactor [36]. The design equation for packed bed reactor with plug flow is given as:…”
Section: Kinetics Studies For Column Experimentsmentioning
confidence: 99%
“…Under aerobic conditions, phenol may be converted by the bacterial biomass to carbon dioxide; other intermediates such as benzoate, catechol, cis-cismuconate, ␤-ketoadipate, succinate and acetate are known to be formed during the biodegradation process [12]. P. putida has been studied by many researchers in free and immobilized forms, using different types of bioreactors [2,[13][14][15][16][17][18][19][20][21][22][23].…”
Section: Introductionmentioning
confidence: 99%
“…The Monod model was also well fitted to the experimental data to determined choose of parameters (R²=0.995), and consequently, it is recommendable not to discard the hypothesis of growth limitation due to substrate limitation. Monod model was also gave the best fit to the experimental data in studies by Gerard et al (2006). It is important to detach that biologic processes are extremely complexes, and they have numberless variables interfering in the process.…”
Section: Simplified Model For Biomass Growthmentioning
confidence: 84%