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Sensitivity of distillation column design to uncertainties in vapor-liquid equilibrium information

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dc.contributor.author Peridis, S en
dc.contributor.author Magoulas, K en
dc.contributor.author Tassios, D en
dc.date.accessioned 2014-03-01T01:09:32Z
dc.date.available 2014-03-01T01:09:32Z
dc.date.issued 1993 en
dc.identifier.issn 0149-6395 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/11062
dc.subject Distillation Columns en
dc.subject Vapor Liquid Equilibrium en
dc.subject.classification Chemistry, Multidisciplinary en
dc.subject.classification Engineering, Chemical en
dc.subject.other Liquids en
dc.subject.other Phase equilibria en
dc.subject.other Vapors en
dc.subject.other Column design en
dc.subject.other Design sensitivity en
dc.subject.other Uncertainties en
dc.subject.other Vapor liquid equilibrium en
dc.subject.other Distillation columns en
dc.title Sensitivity of distillation column design to uncertainties in vapor-liquid equilibrium information en
heal.type journalArticle en
heal.identifier.primary 10.1080/01496399308019040 en
heal.identifier.secondary http://dx.doi.org/10.1080/01496399308019040 en
heal.language English en
heal.publicationDate 1993 en
heal.abstract The sensitivity of distillation column design [number of stages (N) and reflux ratio (R)] to changes in the mean relative volatility (alpha) across the column is examined to demonstrate the effect that uncertainties in the required vapor-liquid equilibrium (VLE) information has on N and R. The results, presented in graphic form for different levels of alpha, provide the design engineer with a simple method of establishing the required degree of accuracy in the VLE information used for a given separation. The sensitivity increases, as expected, with decreasing values of alpha, becoming very pronounced for difficult separations, but it is significant even for easier ones. Thus, for alpha = 1.1, a 2% reduction in alpha leads to a 80% increase in N or an over 120% increase in R, while for alpha = 1.5 the corresponding increases are about 20 and 25%, respectively. The dependence of this sensitivity on design parameters, such as the ratio of the key components in the feed, feed thermal condition, etc., is also examined. The effect of the sources of uncertainty in the VLE information: the values of the interaction coefficient and, on occasion, of the critical properties and acentric factor, is then demonstrated with two examples. en
heal.publisher MARCEL DEKKER INC en
heal.journalName Separation Science and Technology en
dc.identifier.doi 10.1080/01496399308019040 en
dc.identifier.isi ISI:A1993LH31100007 en
dc.identifier.volume 28 en
dc.identifier.issue 9 en
dc.identifier.spage 1753 en
dc.identifier.epage 1767 en


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