1988
DOI: 10.1021/ie00083a031
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A characterization of diffusion distillation for azeotropic separation

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Cited by 10 publications
(7 citation statements)
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“…This is expected since the vapour pressure and diffusivity are proportional to vaporization temperature raised to power n, where n is more than unity. 8 For a given vaporization temperature, total molar flux is higher for helium and lower for argon, compared with air. The ratio of molar fluxes of water to ethanol at azeotropic composition decreases with increase in vaporization temperature for each inert gas and this ratio is higher for argon and lower for helium compared with air at a given vaporization temperature.…”
Section: Resultsmentioning
confidence: 99%
“…This is expected since the vapour pressure and diffusivity are proportional to vaporization temperature raised to power n, where n is more than unity. 8 For a given vaporization temperature, total molar flux is higher for helium and lower for argon, compared with air. The ratio of molar fluxes of water to ethanol at azeotropic composition decreases with increase in vaporization temperature for each inert gas and this ratio is higher for argon and lower for helium compared with air at a given vaporization temperature.…”
Section: Resultsmentioning
confidence: 99%
“…The product of selectivity and total molar flux is proportional to the enrichment, defined for the separation of binary mixture in an integral diffusion distillation column by McDowell and Davis 6. For a given flow rate of 2.58 × 10 −3 m 3 h −1 , experimental and theoretical values of the product of selectivity and total molar flux is plotted against $x_{1}^{v}$ in Fig.…”
Section: Resultsmentioning
confidence: 99%
“…They have shown how the energy consumption in the entire plant can be minimized. McDowell and Davis6 extended the investigation and the description of process behaviour along the length of an integral column via computer simulation. They presented a model of a diffusion distillation column which shows an improvement over the model of Fullarton and Schlunder 3.…”
Section: Introductionmentioning
confidence: 99%
“…where dx1vdl is change in mole fraction of ethanol in a differential height dl on the vaporization side, termed enrichment …”
Section: Modelingmentioning
confidence: 99%
“…where dx v 1 dl is change in mole fraction of ethanol in a differential height dl on the vaporization side, termed enrichment. 21 Similarly, the change in mole fraction of ethanol in a differential height dl on the condensation side is given by…”
Section: Mass Balancementioning
confidence: 99%