When two liquid phases are contacted in a stirred tank reactor, dispersed phase mixing can affect average reaction rate and product selectivity in nonfirst order or mass transfer controlled reactions, as shown theoretically in Part I. This work is concerned with experimental measurement of the dispe
Analysis of dispersed-phase systems: Fresh perspective
โ Scribed by Doraiswami Ramkrishna; Arun Sathyagal; G. Narsimhan
- Book ID
- 102695133
- Publisher
- American Institute of Chemical Engineers
- Year
- 1995
- Tongue
- English
- Weight
- 901 KB
- Volume
- 41
- Category
- Article
- ISSN
- 0001-1541
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โฆ Synopsis
Dispersed-phase systems are analyzed with a fresh perspective where the volume fraction of the dispersed phase is emphasized, not particle numbers as in population balance. Such volume fraction balances are more pertinent to engineering because they deal with the amount of the dispersed phase relative to that of the continuous phase. Although it is easy to make detailed volume fraction balances directly or from population balance, many interesting features are identified here with balance equations in terms of volume fraction, which simply characterize the dispersion process and structure the resulting equation. They lead to equivalent "single-particle" {comprising the entire dispersed phase f processes which can be simulated with great simplicity allowing rapid calculation of quantities associated with the dispersed phase and dispersion. The techniques can solve an inverse problem for mass-transfer coefficients of individual droplets from (simulated) measurements of the bivariate distribution of drop size and concentration of a transferring solute.
Such inverse problem method is important in developing experimental techniques to measure multivariate population distributions such as those of Bae and Tavlarides (1989) and of flow cytometry.
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