Abstract
This work gives a useful insight of hydrodynamic aspects within single-species biofilm reactor with metal structured packing and proposes an original methodology based on high energy X-ray tomography to characterize liquid and biofilm distribution. It has been observed that efficiency of initial liquid distribution controls the biofilm distribution within the packing. This parameter mainly depends on the liquid distributor design. The local liquid velocity within the packing element, depending of the recirculation flow rate, the structural properties of the packing and the bed void fraction distribution, have an effect on initial cell attachment and subsequent biofilm growth. However, once started the process efficiency depends mainly on the biofilm spreading on the packing, affecting further liquid distribution. The liquid flow rate is involved in a physicochemical effect leading to foam formation. The latter decreases surfactin recovery in the liquid phase and provokes biofilm detachment of the packing. Thus, the best surfactin yield production, up to 300mg/L, occurs for a liquid load of 17.6L/m2min supplied by a multiple point source distributor. From a technical point of view, these operating conditions are particularly interesting since foam formation is completely suppressed.
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