1983
DOI: 10.1002/aic.690290119
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Vapor‐liquid equilibrium constants at infinite dilution determined by a gas stripping method: Ethane, propane, n‐butane, n‐pentane in the methane‐n‐decane system

Abstract: A new apparatus to measure partition coefficients K: at infinite dilution up to 200 lo5 Pa and 423 K is described. Measurements of the systems: (1) methane-ethane-ndecane and methane-propane-n-decane at 294.25 K; and (2) methane-n-butane-ndecane at 344.25 K illustrate the reproducibility and good agreement with literature data. In addition, new data were obtained for the system methane-n- SCOPEVapor-liquid distribution ratio of light hydrocarbons between a gas phase made of methane and a liquid phase composed… Show more

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Cited by 20 publications
(4 citation statements)
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“…Actually, 6 of them are γ ∞ A(B) if their solvents are of one component. The deviations of these measurements, analyzed as in Legret et al (1983), are not larger than 4%. They were caused mainly by errors in detection of the desorption rates A of the solute concentration.…”
Section: Resultsmentioning
confidence: 90%
“…Actually, 6 of them are γ ∞ A(B) if their solvents are of one component. The deviations of these measurements, analyzed as in Legret et al (1983), are not larger than 4%. They were caused mainly by errors in detection of the desorption rates A of the solute concentration.…”
Section: Resultsmentioning
confidence: 90%
“…Barber et al (1991) made use of the quadrupole mass spectrometer directly coupled to the apparatus to analyze the effluent stream of the SCF carbon tetrafluoride -solid carbon tetrachloride system, providing a method of on-line analysis. The gas stripping method developed for pressures up to 20 MPa by Legret et al(1983) can also be considered as a particular variant of the saturation method. The technique enables rapid accumulation of data on partitioning of solvents at infinite dilution in systems of the type nonvolatile solute -volatile solvent.…”
Section: Examplesmentioning
confidence: 99%
“…The reproducibility is usually in the 1 to 2% region. Recently, the method has been extended to cover VLE in multicomponent systems, 238 should prove valuable in a variety of industrial applications involving systems composed of light and heavy hydrocarbons, for instance in pipeline design or tertiary oil recovery.…”
Section: A Recent Designs Of Apparatusmentioning
confidence: 99%