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Streptomyces are filamentous bacteria which are widely used industrially for the production of therapeutic biomolecules, especially antibiotics. Bioreactor operating conditions may impact the physiological response of Streptomyces especially agitation and aeration as they influence hydromechanical stress, oxygen and nutrient transfer. The understanding of the coupling between physiological response and bioreactor hydrodynamics lies on a simultaneous description of the flow and transfers encountered by the bacteria and of the microbial response in terms of growth, consumption, morphology, production or intracellular signals. This article reviews the experimental and numerical works dedicated to the study of the coupling between bioreactor hydrodynamics and antibiotics producing Streptomyces. In a first part, the description of hydrodynamics used in these works is presented and then the main relations used. In a second part, the assumptions made in these works are discussed and put into emphasize. Lastly, the various Streptomyces physiological responses observed are detailed and compared.

Mesenchymal stem cells (MSC) are known to be a valuable cell source for tissue engineering and regenerative medicine. However, one of the main limiting steps in their clinical use is the amplification step. MSC expansion on microcarriers has emerged during the last few years, fulfilling the lack of classical T-flasks expansion. Even if the therapeutic potential of MSC as aggregates has been recently highlighted, cell aggregation during expansion has to be avoided. Thus, MSC culture on microcarriers has still to be improved, notably concerning cell aggregation prevention. The aim of this study was to limit cell aggregation during MSC expansion on Cytodex-1®, by evaluating the impact of several culture parameters. First, MSC cultures were performed at different agitation rates (0, 25, and 75 rpm) and different initial cell densities (25 and 50×10(6) cell g(-1) Cytodex-1®). Then, the MSC aggregates were put into contact with additional available surfaces (T-flask, fresh and used Cytodex-1®) at different times (before and after cell aggregation). The results showed that cell aggregation was partly induced by agitation and prevented in static cultures. Moreover, cell aggregation was dependent on cell density and correlated with a decrease in the total cell number. It was however shown that the aggregated organization could be dissociated when in contact with additional surfaces such as T-flasks or fresh Cytodex-1® carriers. Finally, cell aggregation could be successfully limited in spinner flask by adding fresh Cytodex-1® carriers before its onset. Those results indicated that MSC expansion on agitated Cytodex-1® microcarriers could be performed without cell aggregation, avoiding a decrease in total cell number.

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The present study aims at investigating the passage of a gas bubble at a plan liquid-liquid interface both experimentally by using a high-speed video camera and numerically through the volume-of-fluid (VOF) approach. A Newtonian silicone oil was used for the light phase while two different liquids, a Newtonian Emkarox (HV45) solution and a non-Newtonian poly(acryl amide) (PAAm) solution, were employed as the heavy phase. The passage of a gas bubble, generated from a submerged orifice, was followed during its rise in each liquid phase and in particular at the liquid-liquid interface. The original curve of the bubble's position vs time gave interesting insight into the dynamic behavior of the interface. Experimental results show the effect of the bubble size as well as the rheological properties of the heavy phase on the bubble's retention time at the liquid-liquid interface. The preliminary numerical results obtained by the VOF approach are in qualitative agreement with the experimental data.