The aim of the present study was first to propose non drmensional correlations allowing for calculation and scale up of the gas holdup, lrqurd-side mass transfer coefficient and mechanical power In gas liquid stirred tankswhen such parameters as superficral gas velocrty and stirrIng speed are grven
Mechanisms of nozzle type reactor operation with gas removal
β Scribed by Coker, A. K. ;Jeffreys, G. V. ;Mumford, C. J.
- Book ID
- 104748224
- Publisher
- Springer
- Year
- 1992
- Tongue
- English
- Weight
- 588 KB
- Volume
- 49
- Category
- Article
- ISSN
- 0003-6994
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β¦ Synopsis
A nozzle type reactor with provision for gas removal has been studied for the neutralisation of dodecylbenzene sulphonic acid with sodium carbonate solution. Gas was removed via a central air core so that the product was essentially foam-free. The rate of mixing and the chemical reaction between dodecylbenzene sulphonic acid and sodium carbonate solution, were observed to be much faster than the liquid residence time so complete conversion into the product was achieved within seconds. Some gas bubbles were entrained in the product: however these were negligible compared with the bulk of the gas bubbles expelled at the top of the reactor. The criteria for gas removal was that the time for bubbles to travel to the air core under the prevailing centripetal force was less than the liquid phase residence time in the reactor. Mathematical models were therefore proposed to predict the equilibrium bubble diameter and the time for bubble travel to the core. Predicted times were found to be very much less than the average residence time.
π SIMILAR VOLUMES
A new reactor for biological waste gas treatment was developed to eliminate continuous solvents from waste gases. A trickle-bed reactor was chosen with discontinuous movement of the packed bed and intermittent percolation. The reactor was operated with toluene as the solvent and an optimum average b