The influence of non-ideal vapor–liquid equilibrium on the evaporation of ethanol/iso-octane droplets

[Display omitted] The present work investigates the differences between ideal and non-ideal vapor–liquid equilibria (VLE) and their effect on vaporization for multicomponent hydrocarbon fuels, which are representative for combustion and gasification. For this purpose, a parametric study is performed...

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Veröffentlicht in:International journal of heat and mass transfer 2013-09, Vol.64, p.547-558
Hauptverfasser: Bader, A., Keller, P., Hasse, C.
Format: Artikel
Sprache:eng
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Zusammenfassung:[Display omitted] The present work investigates the differences between ideal and non-ideal vapor–liquid equilibria (VLE) and their effect on vaporization for multicomponent hydrocarbon fuels, which are representative for combustion and gasification. For this purpose, a parametric study is performed for examining non-ideal VLE behavior within a pressure range from 0.5 to 20.0bar and an ambient temperature range from 0°C to 600°C, which are typical vaporization conditions in technical systems. The VLE results are then applied in a 0D single-droplet evaporation model, which can be considered a base model for most CFD applications. The droplet life time and the evaporation rates of the individual liquid components are studied for ideal and non-ideal VLE by varying the pressure, the temperature and the particle Reynolds number. A detailed analysis of the transient processes is performed in binary and ternary diagrams and a separation factor is introduced as a quantitative means of measuring for the effective relative volatility of the species. The observed differences suggest that non-ideal VLE have a significant impact on the droplet evaporation characteristics for complex hydrocarbon mixtures.
ISSN:0017-9310
1879-2189
DOI:10.1016/j.ijheatmasstransfer.2013.04.056