Multiphase Bioreactor Design

(avery) #1

with vwp the slip-velocity between water and gel bead, and vwo the slip-velocity between
water and organic phase. The droplet diameter is calculated with the equation of Kumar
and Hartland


with , and
The rise velocity of a single droplet is calculated with Vignes’ equation:


with


The mass transfer coefficient is calculated with the equation of Newman (1931).

t represents the contact time and is equal to: t=Htε 0 /Ud
The mass balances are made dimensionless by dividing with the initial substrate
concentration, the bead diameter, and with DS/R^2. The resulting dimensionless parameters


are: dimensionless length inside the bead z=r/R, dimensionless concentration ,
and a dimensionless time Fo=Dst/R^2.
The resulting mass balances with the implementation of the transfer flux relations are:


Multiphase bioreactor design 384    
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