Kapic et al., 2006 - Google Patents
Correlating gas-liquid mass transfer in a stirred-tank reactorKapic et al., 2006
View PDF- Document ID
- 8367120807190012815
- Author
- Kapic A
- Heindel T
- Publication year
- Publication venue
- Chemical Engineering Research and Design
External Links
Snippet
A correlation is developed for the volumetric gas–liquid mass transfer coefficient (kLa) in stirred-tank reactors (STRs) using results from the literature. The volumetric mass transfer coefficient is correlated on the basis of the relative dispersion parameter (N/NCD) for similar …
- 239000007788 liquid 0 title abstract description 40
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Kapic et al. | Correlating gas-liquid mass transfer in a stirred-tank reactor | |
| Bouaifi et al. | Power consumption, mixing time and homogenisation energy in dual-impeller agitated gas–liquid reactors | |
| Moucha et al. | Gas hold-up, mixing time and gas–liquid volumetric mass transfer coefficient of various multiple-impeller configurations: Rushton turbine, pitched blade and techmix impeller and their combinations | |
| Van't Riet | Review of measuring methods and results in nonviscous gas-liquid mass transfer in stirred vessels | |
| Vrábel et al. | Compartment model approach: Mixing in large scale aerated reactors with multiple impellers | |
| Hassan et al. | Stirred‐tank mechanical power requirement and gas holdup in aerated aqueous phases | |
| Nielsen et al. | A novel method of simulating oxygen mass transfer in two‐phase partitioning bioreactors | |
| Gogate et al. | Survey of measurement techniques for gas–liquid mass transfer coefficient in bioreactors | |
| Alves et al. | Experimental and modelling study of gas dispersion in a double turbine stirred tank | |
| Zheng et al. | Improving oxygen transfer efficiency by developing a novel energy-saving impeller | |
| Böhm et al. | Multiphase stirred tank bioreactors–new geometrical concepts and scale‐up approaches | |
| Bashiri et al. | Development of a multiscale model for the design and scale-up of gas/liquid stirred tank reactors | |
| Petříček et al. | Volumetric mass transfer coefficient, power input and gas hold-up in viscous liquid in mechanically agitated fermenters. Measurements and scale-up | |
| Poncin et al. | Hydrodynamics and volumetric gas–liquid mass transfer coefficient of a stirred vessel equipped with a gas-inducing impeller | |
| Labík et al. | Volumetric mass transfer coefficient in viscous liquid in mechanically agitated fermenters. Measurement and correlation | |
| Gao et al. | Void fraction distribution in sparged and boiling reactors with modern impeller configuration | |
| Scargiali et al. | Mass transfer and hydrodynamic characteristics of a high aspect ratio self-ingesting reactor for gas–liquid operations | |
| Pinelli et al. | Some features of a novel gas dispersion impeller in a dual-impeller configuration | |
| Martín et al. | On the contribution of the scales of mixing to the oxygen transfer in stirred tanks | |
| Parthasarathy et al. | Bubble size distribution in a gas sparged vessel agitated by a Rushton turbine | |
| Daub et al. | Maximum stable drop size measurements indicate turbulence attenuation by aeration in a 3 m3 aerated stirred tank | |
| Lueske et al. | Power Draw and Gas‐Liquid Mass Transfer Characteristics of a Stirred‐Tank Reactor with Draft Tube Configuration | |
| Alves et al. | Alternative compartment models of mixing in tall tanks agitated by multi-Rushton turbines | |
| Daub et al. | Measurement of maximum stable drop size in aerated dilute liquid–liquid dispersions in stirred tanks | |
| Kumar et al. | Mass transfer and shear rate in baffled surface aerator |