Publicado 12 números por año
ISSN Imprimir: 1091-028X
ISSN En Línea: 1934-0508
Indexed in
A Study of Gas Liquid Liquid Systems in a Gas-Agitated Extractor with Static Mixer
SINOPSIS
The operational characteristics of a gas−liquid−liquid system in a gas-agitated extractor with static mixer were studied. Experimental measurements of the gas holdup, the holdup of the dispersed phase, and the mass transfer coefficient under varying conditions were obtained out in the extractor using air, water, and kerosene. It was found that the holdup of the dispersed phase and the mass transfer coefficient depend on gas velocity, water velocity, kerosene velocity, and the structure within extractor. The holdup of gas is independent of the water velocity and kerosene velocity.
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Xiong Jieming, Zhang Liping, Effects of Gas-Agitation and Packing on Hydrodynamics and Mass Transfer of Extraction Column, The Canadian Journal of Chemical Engineering, 82, 5, 2008. Crossref