Determination of mass transfer coefficients in agitated gas—liquid reactors by instantaneous rection
✍ Scribed by D. Ridgway; R.N. Sharma; T.R. Hanley
- Publisher
- Elsevier Science
- Year
- 1989
- Tongue
- English
- Weight
- 779 KB
- Volume
- 44
- Category
- Article
- ISSN
- 0009-2509
No coin nor oath required. For personal study only.
✦ Synopsis
A model was developed for the determination of volumetric mass transfer coefficients which combines penetration theory with instantaneous reaction. The two major criteria to be met are that the reaction is instantaneous compared to the diffusion and that the gas-film resistance is negligible. By maintaining the concentrations of the two reactants in the proper ratio, the first of these criteria can be met, while the second is met based on literature values for the gas-side mass transfer coefficient. The model was experimentally verified using a reaction between ozone and indigo disulfonate.
Additionally, a dual technique is introduced which uses a reacting system followed by a dynamic absorption.
After the liquidphase reactant is depleted, the accumulation of the absorbing gas is tracked. The two methods can then be compared under identical mixing conditions.
📜 SIMILAR VOLUMES
## Abstract There are a large number of correlations given in literature for the prediction of volume‐related liquid‐side mass transfer coefficients in mechanically agitated gas‐liquid contactors. Significant disagreement can be observed concerning the proposed correlations, so that no single corre
method is described for evaluating the gas-liquid mass transfer coefficient k,a in agitated vessels from transient-response measurements. It involves cbncentration measurements at several places in the liquid phase and an axial dispersion model for the gas phase. Results are presented showing the di