1979
DOI: 10.1002/cjce.5450570409
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Liquid‐liquid extraction in laminar slug flow

Abstract: The hydrodynamics of liquid‐liquid slug flow have been studied for several organic components in water, in vertical tubes of diameters between 4.08 and 18.99 mm. Under conditions such that the slug flow is laminar and stable, mass transfer of sparingly soluble organic components (n‐butanol, n‐pentanol and methyl i‐butyl ketone) to water has been measured by observing the shrinkage rates of slugs. The observations are compared with predictions based upon the Higbie penetration model and the calculated velocity … Show more

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Cited by 9 publications
(9 citation statements)
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“…A "free slug" apparatus (Krovvidi (1980)) was also used in some of the experiments. This closely resembled the simple vertical tube arrangement of Baird and Ho (1979) except that the internal diameter of the main tube section was 12.4 mm, rather than the 4 or 6 mm diameters used earlier.…”
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confidence: 52%
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“…A "free slug" apparatus (Krovvidi (1980)) was also used in some of the experiments. This closely resembled the simple vertical tube arrangement of Baird and Ho (1979) except that the internal diameter of the main tube section was 12.4 mm, rather than the 4 or 6 mm diameters used earlier.…”
mentioning
confidence: 52%
“…As discussed by Wallis (1969), a slug of light phase may rise through a denser phase in a vertical tube according to several different flow regimes. This work and its precursor (Baird, Ho (1979)) are concerned with the "capillary regime" in which the interfacial tension greatly restricts the slug velocity. Thus in the case of !I-heptane and water (Ap = 318 kg/m3, a = 43.4 rnN/m) the critical tube diameter for total prcvenrion of plug flow is given by Bretherton's (1961) relationship:…”
Section: Hydrodynamicsmentioning
confidence: 99%
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