The mass transfer of oxygen between an and water has been studled m a bubble column over wide ranges of hquld and gas velocity An oxygen probe was used to map the steady-state hqmd phase concentration of oxygen throughout the column At any given pomt m the column, the oxygen concentration mcreased w
Oxygen mass transfer into aerated CMC solutions in a bubble column
β Scribed by W.-D. Deckwer; K. Nguyen-Tien; A. Schumpe; Y. Serpemen
- Publisher
- John Wiley and Sons
- Year
- 1982
- Tongue
- English
- Weight
- 714 KB
- Volume
- 24
- Category
- Article
- ISSN
- 0006-3592
No coin nor oath required. For personal study only.
β¦ Synopsis
Abstract
Differing findings on the volumetric mass transfer coefficients k~L~a in CMC solutions in bubble column bioreactors have been reported in the literature. Therefore, oxygen mass transfer was studied again in CMC solutions in a 14βcmβi.d. Γ 270βcmβheight bubble column using different spargers. The k~L~a values were determined along with the dispersion coefficients by fitting the prediction of the axial dispersed plug model with the experimental oxygen concentration profiles in the liquid phase. Surprisingly, the obtained liquid phase dispersion coefficients for CMC solution are higher than one would expect from correlations. The k~L~a data depend largely on the flow regime. In general, they are lower than those reported in the literature. The data for developing slug and established slug flow are dependent on the gas velocity and the effective viscosity of the solution and can br correlated by a simple correlation. This correlation describes k~L~a values measured on fermentation broth of Penicillium chrysogenum with striking agreement.
π SIMILAR VOLUMES
The mass transfer of oxygen between air and water in a recirculating bubble column has been studied, at gas and water superficial velocities of up to 0.23 m SK' and 0.68 m s-l respectively. Experiments show that the assumption of plug flow for the gas phase is reasonable, eliminating a possible sour
Immobilization of pollutant-degrading microorganisms on oxygen-permeable membranes provides a novel method of increasing the oxidation capacity of wastewater treatment bioreactors. Oxygen mass transfer characteristics during continuous-flow steady-state experiments were investigated for biofilms sup
Gas holdups and volumetric mass transfer coefficients (kLa) for oxygen were measured in suspensions of kieselguhr (7 pm), aluminium oxide (8 pm) and activated carbon (5 pm) in water or 0.8 molar sodium sulfate solution. By comparison to previously reported specific interfacial areas (a) determined b