期刊
BIOPROCESS AND BIOSYSTEMS ENGINEERING
卷 34, 期 1, 页码 45-56出版社
SPRINGER
DOI: 10.1007/s00449-010-0445-3
关键词
Biodegradation; Immobilised cells; Pulsed plate bioreactor; Modelling; Biofilms
A novel bioreactor called pulsed plate bioreactor (PPBR) with cell immobilised glass particles in the interplate spaces was used for continuous aerobic biodegradation of phenol present in wastewater. A mathematical model consisting of mass balance equations and accounting for simultaneous external film mass transfer, internal diffusion and reaction is presented to describe the steady-state degradation of phenol by Nocardia hydrocarbonoxydans (Nch.) in this bioreactor. The growth of Nch. on phenol was found to follow Haldane substrate inhibition model. The biokinetic parameters at a temperature of 30 +/- A 1 A degrees C and pH at 7.0 +/- A 0.1 are mu (m) = 0.5397 h(-1), K (S) = 6.445 mg/L and K (I) = 855.7 mg/L. The mathematical model was able to predict the reactor performance, with a maximum error of 2% between the predicted and experimental percentage degradations of phenol. The biofilm internal diffusion rate was found to be the slowest step in biodegradation of phenol in a PPBR.
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