Impact of rheology on the mass transfer coefficient during the growth phase of Trichoderma reesei in stirred bioreactors

Chemical Engineering Science

Volumn 75, Issue , 2012, Pages 408-417

  Gabelle, J C ^a,b,c,d   Jourdier, E ^a   Licht, R B ^a   Ben Chaabane, F ^a   Henaut, I ^a   Morchain, J ^b,c,d   Augier, F ^a  

^a IFP ENERGIES NOUVELLES   (France)

^b INSA   (France)

^c UMR792 INGÉNIERIE DES SYSTÈMES BIOLOGIQUES ET DES PROCÉDÉS   (France)

^d CNRS   (France)

Author keywords

Bioreactors; Fermentation; Filamentous fungi; Mass transfer; Non Newtonian fluids; Trichoderma reesei

Indexed keywords

BIOMASS CONCENTRATIONS; CELLULASE ENZYME; CONSISTENCY INDEX; COST ESTIMATIONS; CULTURE BROTHS; FILAMENTOUS FUNGI; GAS-LIQUID MASS TRANSFER; GROWTH PHASE; MASS TRANSFER CORRELATION; MODEL FLUIDS; NON-NEWTONIAN FLUIDS; OXYGEN TRANSFER; POWER LAW MODEL; PROCESS OPTIMISATION; SCALE-UP; STIRRED BIOREACTORS; SUBMERGED CULTURES; T. REESEI; TRICHODERMA REESEI;

BIOCONVERSION; BIOLOGICAL WATER TREATMENT; BIOMASS; BIOREACTORS; ECOLOGY; ELASTICITY; ENZYMES; EXPERIMENTS; FERMENTATION; FUNGI; NON NEWTONIAN LIQUIDS; OXYGEN SUPPLY; RHEOLOGY;

MASS TRANSFER;

EID: 84860513208     PISSN: 00092509     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.ces.2012.03.053     Document Type: Article

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