Mass-transfer rates in a disk-column were studied by vaporizing liquids in a range of counter-current flowing gases. The results of these studies are well correlated by a " relative j, factor," which takes into account the relative velocity of the gas and liquid streams. The importance of the gas-l
Gas-liquid mass transfer in a vibrating disk column
β Scribed by K. Miyanami; K. Tojo; I. Minami; T. Yano
- Publisher
- Elsevier Science
- Year
- 1978
- Tongue
- English
- Weight
- 799 KB
- Volume
- 33
- Category
- Article
- ISSN
- 0009-2509
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β¦ Synopsis
A--Gas-hqmd mass transfer has been studled m a vlbratmg disk column with CO2 gas-water concurrent flow The overall volumetric mass transfer coefficient Ka IS correlated m terms of the gas holdup 4 and the maxlmum power dlssrpatlon P,,,,[cm*/sec'] as follows where d,, and d, are the duuneters of the vlbratmg disk and the column, respectively The bquld phase mass transfer coefficient K In gas-hquld dlsperslons IS almost Independent of the power dlsslpatlon and IS mamjy Influenced by the bubble sue. the coe5iclent IS nearly proportional to the Sauter mean diameter of the bubbles The mass transfer coefficient m the vfbratmg &sk column IS of the same order of magmtude as that for correspondmg bubbk sues m a conventtond stured tank with rotary astation
π SIMILAR VOLUMES
Gas holdups and volumetric mass transfer coefficients (kLa) for oxygen were measured in suspensions of kieselguhr (7 pm), aluminium oxide (8 pm) and activated carbon (5 pm) in water or 0.8 molar sodium sulfate solution. By comparison to previously reported specific interfacial areas (a) determined b
## Abstract Data are reported on the absorption of oxygen by water under countercurrent flow conditions, in a 15βcm diameter reciprocating plate bubble column. Amplitude (half stroke) is set at 12.7βmm and reciprocation frequencies up to 5βHz have been employed. Five different types of plate have b