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Mass transfer in a membrane aerated biofilm

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Academic year: 2021

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Figure

Table 1 e Parameters of the five experiments reported in this paper (Picard, 2011).
Fig. 2 e Diagrammatic view of the experimental set-up used in the present study. Five cells can be run in parallel.
Fig. 3 e a: The Reynolds number in the gas phase has no influence on the global mass transfer coefficient (K G ) in the range investigated
Fig. 5 e Amount of dry matter found per unit of biofilm volume as a function of the Reynolds number in the liquid phase (Picard, 2011)
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