Enhancement of gas-liquid mass transfer by a dispersed second liquid phae
β Scribed by W.J. Bruining; G.E.H. Joosten; A.A.C.M. Beenackers; H. Hofman
- Publisher
- Elsevier Science
- Year
- 1986
- Tongue
- English
- Weight
- 489 KB
- Volume
- 41
- Category
- Article
- ISSN
- 0009-2509
No coin nor oath required. For personal study only.
β¦ Synopsis
From experiments in a stirred cell contsctor with flat gaeliquid interface, it is shown that the rate of xnsss transfer of oxygen into an aqueous solution can he enhanced by the presence of small amount8 (0.5-l ~01%) of a dispersed organic phase (e.g. hexadecane, decane, decanol or cyclohexane), provided that the droplet diameter is in the order of or smaller than the tilm thickness (D/k=) and the solubility of oxygen in the organic phase is larger than in water. A simple model is proposed that predicts the experimentally observed enhancement factors with reasonable accuracy.
π SIMILAR VOLUMES
Mass transfer behaviour of gas-liquid dispersions is usually characterized by the volumetric mass transfer coefficient &a. For its experimental determination various methods exist which can be grouped inro stationary and instationary (dynamic) methods. Very often volumetric mass transfer coefficient
Shorter Communications N, molar flux of i with respect to stationary coordinate reference frame N, mixture total molar flux p total system pressure [PI modal matrix of [DI distance coordinate along diffusion path gas constant time temperature diffusion velocity of species i in mixture molar average
D e p a r t m e n t of C h e m i c a l Engineering University of N o t r e Dame, N a t r e Dome, Indiana 46556 Rates of mass transfer during drop formation and coalescence were investigated for three dispersed phase-controlled liquid systems, one binary (ethyl acetate-water) and two ternary (acetic
Bubble break-up, gas holdup, and the gas-liquid volumetric mass transfer coefficient are studied in a bubble column reactor with simultaneous injection of a gas and liquid through a T-junction nozzle. The theoretical dependence of bubble break-up and the volumetric mass transfer coefficient on liqui