Improved modelling of the unsteady-state behaviour of an immobilized-cell, fluidized-bed bioreactor for phenol biodegradation

Canadian Journal of Chemical Engineering

Volumn 80, Issue 2, 2002, Pages 239-252

  Onysko, Kira A ^a   Robinson, Campbell W ^a   Budman, Hector M ^a  

^a UNIVERSITY OF WATERLOO   (Canada)

Author keywords

Biofilm; Dynamic model; Immobilized cell fluidized bed bioreactor; Phenol degradation; Pseudomonas putida Q5

Indexed keywords

BACTERIA; BIODEGRADATION; BIOFILMS; CELL IMMOBILIZATION; CHEMICAL REACTORS; FLUIDIZED BEDS; PHENOLS; REACTION KINETICS;

BIOFILM THICKNESS; PSYCHROTROPHIC BACTERIUM;

CHEMICAL ENGINEERING;

PHENOL;

BIOREACTOR; FLUIDIZED BED; INSTABILITY; MODELING; REACTOR;

ARTICLE; BACTERIAL GROWTH; BACTERIUM CULTURE; BIODEGRADATION; BIOFILM; BIOMASS; BIOREACTOR; CONCENTRATION (PARAMETERS); DYNAMIC MODEL; FLUIDIZED BED REACTOR; GROWTH INHIBITION; GROWTH RATE; GROWTH RATE SUPPRESSION FACTOR; IMMOBILIZED CELL FLUIDIZED BED BIOREACTOR; IMMOBILIZED CELL REACTOR; MODEL; NONHUMAN; PREDICTION; PSEUDOMONAS PUTIDA; PSEUDOMONAS PUTIDA Q5; SIMULATION; STEADY STATE; THICKNESS; UNSTEADY STATE;

EID: 0036552109     PISSN: 00084034     EISSN: None     Source Type: Journal    
DOI: 10.1002/cjce.5450800209     Document Type: Article

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