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Substrate inhibition
kinetics of phenol degradation by binary mixed culture of
Pseudomonas aeruginosa and Pseudomonas fluorescence
from steady state and wash- out data
S. E. Agarry1*,
B. O. Solomon2,3 and S. K. Layokun2
1Biochemical
Engineering Research Unit, Department of Chemical
Engineering, Ladoke Akintola University of Technology,
Ogbomoso, Nigeria.
2Biochemical
Engineering Research Laboratory, Obafemi Awolowo University,
Ile-Ife, Nigeria.
3National
Biotechnology Development Agency, Abuja, Nigeria.
*Corresponding author. E-mail:
sam_agarry@yahoo.com.
Nomenclature: CTR,
Carbon dioxide transfer rate (mg/L/h); D, dilution
rate (h-1); ,
half-saturation constant (mg/L);
,
inhibition constant (mg/L); OTR, oxygen transfer rate
(mg/L/h);
,
specific phenol (substrate) consumption rate (mg/mg/h);
,
maximum specific phenol (substrate) consumption rate
(mg/mg/h); S, Cs, substrate concentration
(mg/L); µmax maximum specific growth
rate (h-1); X, biomass concentration
(mg/L).
Accepted
19 September, 2008 |
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Steady states of a continuous culture with an inhibitory
substrate were used to estimate kinetic parameters under
substrate limitation (chemo stat operation). Mixed cultures
of an indigenous Pseudomonas fluorescence and Pseudomonas
aeruginosa were grown in continuous culture on phenol as
the sole source of carbon and energy at dilution rates of
0.01 – 0.20 h-1. Using different dilution rates
several steady states were investigated and the specific
phenol consumption rates were calculated. In addition,
phenol degradation was investigated by increasing the
dilution rate above the critical dilution rate (washout
cultivation). The results showed that the phenol degradation
by mixed culture of P. fluorescence and P. aeruginosa
can be described by simple substrate inhibition kinetics
under substrate limitation but cannot be described by simple
substrate inhibition kinetics under washout cultivation. The
phenol consumption rate (degradation rate) increased with
increase in dilution rate. Fitting of the steady state data
from continuous cultivation to six inhibition models
resulted in the best fit for Haldane, Yano and Koga, Aiba et
al. and Teissier models, respectively. The rsmax
value of 0.322 mg/mg/h obtained from these model equations
was comparable to the experimentally calculated rsmax
value of 0.342 mg/mg/h obtained under washout cultivation.
Key words: Continuous cultivation, washout cultivation, steady state,
substrate inhibition, bioreactor, primary culture, secondary
culture, kinetic parameters, mixed culture.
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