By T.K. Ghose ,A. Fiechter, N.Blakebrough
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Additional resources for Advances in Biochemical Engineering, Volume 008: Mass Transfer in Biotechnology
The effects o f a s on the mass transfer rate must also be considered but these are difficult to analyze because morphological properties influence theological properties and also introduce questions requiring consideration of "pore" diffusion. Space does not permit a discussion of this topic and hence the reader is referred to other reviews [ 1 1 9 122] for background information and further references. However, we should note here that the complex interactions between a s (or morphology), theological properties, and mass transfer coefficients have received almost no serious consideration at either the experimental or the theoretical level.
30. Diffusion model for three phase interphase mass transfer where KL is the mass transfer coefficient for this interphase transport process, a G is the surface area of the gas phase (bubbles), C~, is the maximum concentration of the solute (the concentration of A when the liquid is saturated with A at the prevailing partial pressure of A in the gas phase), and CA is the actual concentration of A in the liquid phase. To a good approximation we can say • o MAG =MAL = ~, CAs" (57) Eqs. (50), (51), (56), and (57) may be combined to give k,C~ rA- kl 1 + K~aG + kl (58) k[as [Note that kL in Eq.
The power law index) would not change drastically. The large dilution required probably would result in yield and productivity losses which would outweigh gains resulting from better mixing. The results of initial small-scale experiments ( 1 - 5 1) performed in the author's laboratory substantiate this contention in the case of xanthan . 2. 1. General Considerations There have been many reported studies of laboratory and small-scale continuous fermen.