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Bubble coalescence behaviour in biological media
Authors:I Adler  H Buchholz  J Voigt  R Wittler  K Schügerl
Institution:(1) Institut für Technische Chemie der Universität Hannover, Callinstr. 3, D-3000 Hannover, Federal Republic of Germany
Abstract:Summary Volumetric mass transfer coefficients (kLa) were measured by a steady state method in a twin bubble column to characterize the coalescence behaviour of the medium. Employing Hansenula polymorpha cultivation broths, kLa values were compared with those measured in model media in the presence and absence of antifoam agents. The ratio of the volumetric mass transfer coefficient in the system investigated to that in water, 
$${\text{m  =  k}}_{\text{L}} {\text{a/(k}}_{\text{L}} {\text{a)H}}_{\text{2}} {\text{O}}$$
, was employed to characterize the cultivation medium.Symbols a Specific gas/liquid interfacial area with regard to the liquid volume in reactor - de Dynamical equilibrium bubble diameter - dH Perforated plate hole diameter - dp Primary bubble diameter - dS Sauter bubble diameter - Fv Liquid feed rate - H Bubbling layer height - kL Gas/liquid mass transfer coefficient - kLa Volumetric mass transfer coefficient - m kLa/(kLa)r coalescence index - mcorr Corrected coalescence index Eq. (3)] - OTR Oxygen transfer rate - PO Dissolved O2-partial pressure in BS2 - P1 Dissolved O2-partial pressure in BS1 - PO PO/PS relative oxygen saturation in BS2 - P1 P1/PS relative oxygen saturation in BS1 - PS Saturation dissolved oxygen partial pressure - Rc dnB/dt coalescence rate - S Substrate concentration - tF Time since the beginning of the cultivation - X Biomass concentration - V1 Liquid volume in BS1 - wSG Superficial gas velocity in BS1 - isinG Gas holdup in BS1 - pgr1 V1/Fv mean liquid residence time in BS1 - BS1 O2 absorber column - BS2 O2 desorber column - D Desmophen (antifoam agent) - NS Nutrient salt solution (Table 1)
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