Biodegradation of phenol in a continuous process: comparative study of stirred tank and fluidized-bed bioreactors.
The paper presents the main results obtained from the study of the biodegradation process of phenol by a pure culture of Pseudomonas putida ATCC 17484. The experimental work was carried out in two different systems: a stirred tank where cells grew as a suspended culture and a fluidized bed where cells were immobilized within calcium alginate gel beads. The influence of the hydraulic residence time (HRT) and organic loading rate on the removal efficiency of phenol was determined for both bioreactors. Also, the stability of the fluidized-bed bioreactor (FBB) in terms of its ability to withstand sudden phenol overdoses is also reported. Experimental values indicated that both bioreactors showed high phenol degradation efficiencies, higher than 90%, even for a phenol loading rate in the influent as high as 4 g phenol/l day. The FBB showed better performance than the suspended-culture bioreactor due to its better control and because it could operate with lower HRT.
González
G
G
Department of Chemical Engineering, University of Valladolid, 47011 Valladolid, Spain. gerardo@siq.iq.cie.uva.es
Herrera
M G
MG
García
M T
MT
Peña
M M
MM
D000464:Alginates / Q000378:metabolism; D001673:Biodegradation, Environmental; D019149:Bioreactors; D018914:Cells, Immobilized / Q000378:metabolism; D020723:Glucuronic Acid; D006603:Hexuronic Acids; D007700:Kinetics; D019800:Phenol / Q000378:metabolism*; D016958:Pseudomonas putida / Q000166:cytology / Q000378:metabolism*; D013997:Time Factors
D000464:Alginates; D006603:Hexuronic Acids; D019800:Phenol; D020723:Glucuronic Acid