2002
DOI: 10.1002/aic.690480606
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Design and analysis of nonequilibrium separation processes

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Cited by 7 publications
(15 citation statements)
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References 21 publications
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“…Sridhar et al 5 begin their analysis of simple batch evaporation in much the same way, as do all others, with the differential material balance for the liquid phase (expressed here in a form slightly different from, but formally equivalent to, that in Sridhar et al 5 )…”
Section: Sridhar Et Al 5 Modelsupporting
confidence: 41%
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“…Sridhar et al 5 begin their analysis of simple batch evaporation in much the same way, as do all others, with the differential material balance for the liquid phase (expressed here in a form slightly different from, but formally equivalent to, that in Sridhar et al 5 )…”
Section: Sridhar Et Al 5 Modelsupporting
confidence: 41%
“…This is the relationship used by Sridhar et al 5 and implies that the molar fluxes have mixed signs (given that the heats of vaporization have the same sign). That is, some components would evaporate, whereas others would be condensing.…”
Section: Sridhar Et Al 5 Modelmentioning
confidence: 44%
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“…In a recent article, a strategy was developed to draw mole fraction curve maps for homogeneous mixtures, using the nonequilibrium model that involves the utilization of mass-transfer models. However, it must be emphasized that these curves were incorrectly referred to as “residue curves”.…”
Section: Introductionmentioning
confidence: 99%
“…Thiel et al (1997a, 1995b) also used residue curve maps for fuel ether systems before formulating a rigorous mass‐transfer model, although the residue curves were still calculated assuming phase equilibrium. Nonequilibrium residue curve maps were recently addressed by Sridhar et al (2002). A comprehensive review of mass‐transfer models used in reactive distillation was published by Taylor and Krishna (2000).…”
Section: Introductionmentioning
confidence: 99%