comparison of the values of mterfaclal area m cocurrent downward flow of gas and hquld with those obtamed m upward flow revealed very httle difference Volumetric as well as true hqmd side mass transfer coefficients m downflow were found to be several times lower than m upflow Only m the smallest 10
Liquid-side mass transfer coefficient for gas slugs rising in liquids
โ Scribed by M.T. Sena Esteves; J.R.F. Guedes De Carvalho
- Publisher
- Elsevier Science
- Year
- 1993
- Tongue
- English
- Weight
- 852 KB
- Volume
- 48
- Category
- Article
- ISSN
- 0009-2509
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โฆ Synopsis
The present work reports a series of' experimental measurements of liquid-side mass transfer coefficient for slugs rising in liquids with viscosities in the range 0.9 x IO-'-0.14 Pas. Three column diameters were used (19,32 and 52 mm) and slugs with values of L/D up to 38 were studied. The data obtained compare well with the theoretical predictions of van Heuven and Beck and they show the limited range of applicability of the empirical equations of Filla and Niranjan et rrl. The data reported for slugs rising in water in the 52 mm i.d. column clearly suggest that transition .O turbulent film flow occurs at a value of r/D of about 1 I, the mass transfer in the turbulent portion being well predicted by correlations developed for wetted wall columns. A simple asymptotic expression for the evaluation of mass transfer coefficients in long slugs (i.e. slugs alongside which fully developed film flow is observed over a large portion of the total length) in viscous liquids was also developed and it is seen to compare very well with the experimental data.
๐ SIMILAR VOLUMES
## NOTATION vibrational amplitude of ultrasonic horn, m velocity of sound in water, m/s cavitation number as defined in Fig. 2 vibrational frequency of an oscillating bubble or ultrasonic horn, Hz energy intensity as defined in eq. ( 2), W/m2 fluid pressure further downstream of the throttled valv
Mass transfer coefficients in gas and liquid have been obtained for the case of cocurrent gas-liquid flow through a vertical tube 6 mm id. by absorbing sulphur dioxide into sodium hydroxide solution and carbon dioxide into sodium carbonate-sodium bicarbonate solution respectively. The liquid side ma