Optimization of Inocula Conditions for Enhanced Biosurfactant Production by Bacillus subtilis SPB1, in Submerged Culture, Using Box–Behnken Design

2012 ◽  
Vol 5 (2) ◽  
pp. 92-98 ◽  
Author(s):  
Ines Mnif ◽  
Semia Ellouze-Chaabouni ◽  
Dhouha Ghribi
2014 ◽  
Vol 57 (2) ◽  
pp. 295-301 ◽  
Author(s):  
Marylane de Sousa ◽  
Iuri Torquato Dantas ◽  
Anne Kamilly Nogueira Felix ◽  
Hosiberto Batista de Sant'Ana ◽  
Vânia Maria Maciel Melo ◽  
...  

2011 ◽  
Vol 86 (2) ◽  
pp. 384-389 ◽  
Author(s):  
T. Roldán-Carrillo ◽  
X. Martínez-García ◽  
I. Zapata-Peñasco ◽  
G. Castorena-Cortés ◽  
J. Reyes-Avila ◽  
...  

Author(s):  
R. R. Fonseca ◽  
A. J. R. Silva ◽  
F. P. De Franca ◽  
V. L. Cardoso ◽  
E. F. C. Sérvulo

2021 ◽  
Vol 0 (0) ◽  
Author(s):  
Bahareh Moshtagh ◽  
Kelly Hawboldt ◽  
Baiyu Zhang

Abstract Costs associated with production of favorable biologically produced surfactants continue to be a significant obstacle to large scale application. Using industrial wastes and by-products as substrate and optimization of cultural conditions are two strategies of producing biosurfactants with a reasonable price. Also, modeling the biosurfactant production bioprocess improves the commercial design and monitoring of biomass growth, biosurfactant production, and substrate utilization. In this study, the indigenous Bacillus subtilis N3-1P strain and a local brewery waste as the carbon source were used to produce a biosurfactant. The batch cultivation was performed under the optimum conditions. Models describing the biomass growth, biosurfactant production, and substrate utilization were developed by fitting the experimental data to the logistic, Contois and Luedeking-Piret models using MATLAB software and regression analysis. The kinetic parameters including the maximum specific growth rates (µ max), the Contois constant (K), parameters of the Luedeking-Piret modelswere calculated. Yields including Y X/S , and Y P/X were found to be 0.143 gX/gS, and 0.188 gP/gX, respectively. The experimental and predicted model showed good agreement. The developed models are a key step in designing reactors for scale up of biosurfactant production.


Fuel ◽  
2013 ◽  
Vol 111 ◽  
pp. 259-268 ◽  
Author(s):  
Jorge F.B. Pereira ◽  
Eduardo J. Gudiña ◽  
Rita Costa ◽  
Rui Vitorino ◽  
José A. Teixeira ◽  
...  

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