Bubble free gaseous transfer in bioreactors using perfluorocarbons

In this work the concept of bubble-free oxygenation that was able to ensure oxygen supply and carbon dioxide extraction for a chemostat culture of Escherichia coli was experimentally demonstrated. It was operated at the dilution rate of 0.275 h^–1 under atmospheric pressure and at 35.5 °C. Foralkyl, a commercial perfluorocarbon, added in the influent medium under emulsified form and at 50% volumic fraction, was able to provide 0.17 g O₂/l/h and extract 0.23 g CO₂/l/h for a culture at 0.74 g/l of biomass. This oxygen supply was close to the maximum oxygenation Foralkyl was theoretically able to provide at this pressure when imposing a minimum oxygen concentration of 1 mg/l in the water phase. The quantification of transfer was not done from a direct measurement of oxygen transfer rates because conventional oxygen concentration measurement by membrane polarographic probe in an emulsion was not judged reliable. This evaluation was done by referring to conventional aerated culture whose measurable parameters (biomass and product concentrations) were found unaffected when shifting to the novel oxygenation device.List of Symbols C _LV ^* , C _LV g/l dissolved oxygen concentration in the vector phase at equilibrium and in the reactor - C _LW ^* , C _LW g/l dissolved oxygen concentration in the water phase at equilibrium and in the reactor - C _LWinput , C _LWoutput g/l dissolved oxygen concentrations in aqueous medium in the reactor input and output flow - D h^–1 dilution rate - ^DMM_{o 2}, MM_{co 2} g/mol oxygen and carbon dioxide molar masses - %O_2input, %O_2output oxygen percentages in the reactor input and output flow - %CO_2input, %CO_2output carbon dioxide percentages in the reactor input and output flow - %N _2input %N _2output nitrogen percentages in the reactor input and output flow - Q _G.i ⁿ Q _G.o ⁿ l/h gas flow rates at the reactor input and output at normal conditions (273 K, 1 atm) - Q _L l/h liquid flow rate - Q _LW , Q _LV l/h water and vector flow rates - r_{O 2} g/l/h oxygen consumption rate - r _x g/l/h biomass production rate - r _{CO 2} g/l/h carbon dioxide production rate - V _L l fermentor aqueous volume - V _LW , V _LV l water phase and vector phase volume - V _{O 2}, V _{CO 2}, l/mol oxygen and carbon dioxide molar volume under gaseous form at normal conditions (273 K, 1 atm) - Y _{O 2 x} gO₂/g cell oxygen consumption yield for biomass growth - Y _sx g glucose/g cell glucose consumption yield for biomass growth - vector volumic fraction - h^–1 growth rate This work was totally financed by the European Space Agency.