Yee L., Blanch H.W. Recombinant protein expression in high cell density fed-batch cultures of Escherichia coli. Nat Biotechnol 1992, 10(12):1550-1556.
Loloei A.Z., Daneshp N., Motlagh M.R.J., Vali A.R. Growth rate control in biotechnological fed-batch process using dynamic matrix control. SICE-ICASE International Joint Conference 2006, 3696-3701.
Martiónez A., Ramiórez O.T., Valle F. Effect of growth rate on the production of β-galactosidase from Escherichia coli in Bacillus subtilis using glucose-limited exponentially fedbatch cultures. Enzyme Microb Tech 1998, 22(6):520-526.
Bastin G., Dochain D. On-line Estimation and Adaptive Control of Bioreactors 1990, Elsevier Science, Amsterdam.
Dauner M., Storni T., Sauer U. Bacillus subtilis metabolism and energetic in carbon-limited and excess-carbon chemostat culture. J Bacteriol 2001, 183(24):7308-7317.
Vierheller C., Goel A., Peterson M., Domach M.M., Ataai M.M. Sustained and constitutive high levels of protein production in continuous culture of Bacillus subtilis. Biotechnol Bioeng 1995, 47:520-524.
Zamboni N., Fisher E., Muffler A., Wyss M., Hohmann H.P., Sauer U. Transient expression and flux changes during a shift from high to low riboflavin production in continuous cultures of Bacillus subtilis. Biotechnol Bioeng 2005, 89(2):219-232.
Lee J., Parulekar S.J. Enhanced production of α-amylase in fed-batch cultures of Bacillus subtilis TN 106[pAT5]. Biotechnol Bioeng 1993, 42:1142-1150.
Picó-Marco E., Navarro J.L., Bruno-Barcena J.M. A closed loop exponential feeding law: Invariance and global stability analysis. J Process Control 2006, 16(4):395-402.
Picó-Marco E., Picó J. Partial stability for specific growth rate control in biotechnological fed-batch processes. J Process Control 2003, 1:724-728.
Guez J.S., Chenikher S., Cassar J.P., Jacques P. Setting up and modelling of overflow fed-batch cultures of Bacillus subtilis for the production and continuous removal of lipopeptides. J Biotechnol 2007, 131(1):67-75.
Maget-Dana R., Thimon L., Peypoux F., Ptak M. Surfactin/iturin A interactions may explain the synergistic effect of surfactin on the biological properties of iturin A. Biochimie 1992, 74:1047-1051.
Razafindralambo H., Paquot M., Baniel A., Popineau Y., Hbid C., Jacques P., Thonart P. Foaming properties of surfactin, a lipopeptide biosurfactant from Bacillus subtilis. J Am Oil Chem Soc 1996, 73(1):149-151.
Razafindralambo H., Popineau Y., Deleu M., Hbid C., Jacques P., Thonart P., Paquot M. Foaming properties of lipopeptides produced by Bacillus subtilis: effect of lipid and peptide structural attributes. J Agric Food Chem 1998, 46:911-916.
Cooper D.G., Macdonald C.R., Duff S.J., Kosaric N. Enhanced production of surfactin from Bacillus subtilis by continuous product removal and metal cation additions. Appl Environ Microbiol 1981, 42:408-412.
Davis D.A., Lynch H.C., Varley J. The application of foaming for the recovery of surfactin from B. subtilis ATCC 21332 cultures. Enzyme Microb Technol 2001, 28:346-354.
McIntyre J.J., Bunch A.W., Bull A.T. Vancomycin production is enhanced in chemostat culture with biomass-recycle. Biotechnol Bioeng 1999, 62:576-582.
Harmand J., Rapaport A., Dochain D., Lobry C. Microbial ecology and bioprocess control: opportunities and challenges. J Process Control 2008, 18(9):865-875.
Dochain D. State observation and adaptive linearizing control for distributed parameter (bio)chemical reactors. Int J Adapt Control Signal Process 2001, 15:633-653.
Huang B. Bayesian methods for control loop monitoring and diagnosis. J Process Control 2008, 18(9):829-838.
Dowd J.E., Ezra K.E., Kwok, Piret J.M. Predictive modeling and loose-loop control for perfusion bioreactors. Biochem Eng J 2001, 9:1-9.
Lee J., Lee S.Y., Park S., Middelberg A.P.J. Control of fed-batch fermentations. Biotechnol Adv 1999, 17:29-48.
Gadkar K.G., Doyle F.J., Crowley T.J., Varner J.D. Cybernetic model predictive control of a continuous bioreactor with cell recycle. Biotechnol Prog 2003, 19:1487-1497.
Magyar A., Szederkényi G., Hangos K.M. Globally stabilizing feedback control of process systems in generalized Lotka-Volterra form. J Process Control 2008, 18:80-91.
Morari M., Lee H.J. Model predictive control: past, present and future. Comput Chem Eng 1999, 23:667-682.
Zhu G.Y, Zamamiri A., Henson M.A., HjortsØ M.A. Model predictive control of continuous yeast bioreactors using cell population balance models. Chem Eng Sci 2000, 55:6155-6167.
De Battista H., Picó J., Picó-Marco E. Globally stabilizing control of fed-batch processes with haldane kinetics using growth rate estimation feedback. J Process Control 2006, 16(8):865-875.
Jenzsch M., Simutis R., Eisbrenner G., Stückrath I., Lübbert A. Estimation of biomass concentrations in fermentation processes for recombinant protein production. Bioprocess Biosyst Eng 2006, 29(1):19-27.
Jenzsch M., Simutis R., Luebbert A. Generic model control of the specific growth rate in recombinant Escherichia coli cultivations. J Biotechnol 2006, 122(4):483-493.
Leclère V., Béchet M., Adam A., Guez J.S., Wathelet B., Ongena M., Thonart P., Gancel F., Chollet-Imbert M., Jacques P. Characterization of a constitutive mycosubtilin overproducing Bacillus subtilis strain and its antagonistic activity. Appl Environ Microbiol 2005, 71(8):4577-4584.
Guez J.S., Muller C.H., Danzé P.M., Büchs J., Jacques P. Respiration activity monitoring system (RAMOS), an efficient tool to study the influence of the oxygen transfer rate on the synthesis of lipopeptide by Bacillus subtilis ATCC6633. J Biotechnol 2008, 134(1-2):121-126.