A kinetic model for quantitative evaluation of the effect of hydrogen and osmolarity on hydrogen production by Caldicellulosiruptor saccharolyticus

Biotechnology for Biofuels

Volumn 4, Issue , 2011, Pages

  Ljunggren, Mattias ^a   Willquist, Karin ^a   Zacchi, Guido ^a   Van Niel, Ed W J ^a  

^a LUND UNIVERSITY   (Sweden)

Author keywords

[No Author keywords available]

Indexed keywords

BATCH FERMENTATION; CALDICELLULOSIRUPTOR SACCHAROLYTICUS; EFFECT OF HYDROGEN; EQUILIBRIUM CONCENTRATION; EXPERIMENTAL DATA; EXTREME THERMOPHILE; GROWTH BEHAVIOR; INHIBITORY EFFECT; KINETIC GROWTH; KINETIC MODELS; MASS TRANSFER RATE; MATHEMATICAL EXPRESSIONS; MICROBIAL GROWTH; MODEL PARAMETERS; MONOD KINETIC; OPTIMAL OPERATING CONDITIONS; OSMOLARITY; OVERSATURATION; PRODUCT FORMATION; QUANTITATIVE EVALUATION; SOLUTE CONCENTRATIONS; STRIPPING RATE; SUBSTRATE CONCENTRATIONS;

CONCENTRATION (PROCESS); DISSOLUTION; HYDROGEN; HYDROGEN PRODUCTION; KINETICS; MASS TRANSFER; PRODUCTIVITY;

SUBSTRATES;

CONCENTRATION (COMPOSITION); GROWTH MODELING; HYDROGEN; MASS TRANSFER; MICROBIAL ACTIVITY; NUMERICAL MODEL; QUANTITATIVE ANALYSIS;

CALDICELLULOSIRUPTOR SACCHAROLYTICUS;

EID: 80052665545     PISSN: 17546834     EISSN: None     Source Type: Journal    
DOI: 10.1186/1754-6834-4-31     Document Type: Article

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