Modelling and simulation of steady-state phenol degradation in a pulsed plate bioreactor with immobilised cells of Nocardia hydrocarbonoxydans
| dc.contributor.author | Shetty K, V.S. | |
| dc.contributor.author | Verma, D.K. | |
| dc.contributor.author | Srinikethan, G. | |
| dc.date.accessioned | 2026-02-05T09:36:04Z | |
| dc.date.issued | 2011 | |
| dc.description.abstract | 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 ± 1 °C and pH at 7.0 ± 0.1 are ? <inf>m</inf> = 0.5397 h -1, K <inf>S</inf> = 6.445 mg/L and K <inf>I</inf> = 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. © 2010 Springer-Verlag. | |
| dc.identifier.citation | Bioprocess and Biosystems Engineering, 2011, 34, 1, pp. 45-56 | |
| dc.identifier.issn | 16157591 | |
| dc.identifier.uri | https://doi.org/10.1007/s00449-010-0445-3 | |
| dc.identifier.uri | https://idr.nitk.ac.in/handle/123456789/27354 | |
| dc.subject | Aerobic biodegradation | |
| dc.subject | Bio-kinetic parameters | |
| dc.subject | Degradation of phenols | |
| dc.subject | Glass particles | |
| dc.subject | Haldane | |
| dc.subject | Immobilised Cells | |
| dc.subject | Internal diffusion | |
| dc.subject | Mass balance equations | |
| dc.subject | Maximum error | |
| dc.subject | Modelling | |
| dc.subject | Modelling and simulations | |
| dc.subject | Nocardia | |
| dc.subject | Phenol degradation | |
| dc.subject | Pulsed plate bioreactor | |
| dc.subject | Reactor performance | |
| dc.subject | Substrate inhibition | |
| dc.subject | Biofilms | |
| dc.subject | Biofilters | |
| dc.subject | Biological water treatment | |
| dc.subject | Bioreactors | |
| dc.subject | Cell culture | |
| dc.subject | Cells | |
| dc.subject | Degradation | |
| dc.subject | Mathematical models | |
| dc.subject | Microbiology | |
| dc.subject | Phenols | |
| dc.subject | Wastewater | |
| dc.subject | Biodegradation | |
| dc.subject | phenol | |
| dc.subject | aerobic metabolism | |
| dc.subject | article | |
| dc.subject | bacterial cell | |
| dc.subject | bacterial growth | |
| dc.subject | bacterial kinetics | |
| dc.subject | bacterial metabolism | |
| dc.subject | biodegradation | |
| dc.subject | biofilm | |
| dc.subject | controlled study | |
| dc.subject | immobilized cell reactor | |
| dc.subject | mathematical model | |
| dc.subject | Nocardia hydrocarbonoxydans | |
| dc.subject | nonhuman | |
| dc.subject | priority journal | |
| dc.subject | reactor monitoring | |
| dc.subject | steady state | |
| dc.subject | Algorithms | |
| dc.subject | Biodegradation, Environmental | |
| dc.subject | Cells, Immobilized | |
| dc.subject | Computer Simulation | |
| dc.subject | Diffusion | |
| dc.subject | Kinetics | |
| dc.subject | Models, Biological | |
| dc.subject | Phenol | |
| dc.subject | Temperature | |
| dc.subject | Waste Disposal, Fluid | |
| dc.subject | Pseudonocardia hydrocarbonoxydans | |
| dc.title | Modelling and simulation of steady-state phenol degradation in a pulsed plate bioreactor with immobilised cells of Nocardia hydrocarbonoxydans |
