Evaporation maps for non-ideal ternary mixtures. (14th April 2015)

• Record Type: Journal Article
• Authors: Dillon, Paul; Cronin, Kevin; Byrne, Edmond P.
• Is Part Of: Chemical engineering science. Volume 126(2015)
• Page Start: 641
• Page End: 659
• Publication Date: 2015-04-14
• Subjects: Evaporation -- Drying -- Solvent mixtures -- Multicomponent mass transfer -- Bifurcations; Chemical engineering -- Periodicals; Génie chimique -- Périodiques; Chemical engineering; Periodicals; Electronic journals; 660
• DOI: 10.1016/j.ces.2014.12.035
• Languages: English
• ISSNs: 0009-2509

Abstract

Abstract: Evaporation maps are a convenient way of representing the dynamic composition of evaporating liquid mixtures. Specifically, these maps represent the residual composition of evaporating ternary non-ideal mixtures over the full range of composition, and are analogous to the commonly used residue curve maps of simple distillation processes. The evaporation process considered here involves gas-phase limited evaporation from a liquid or wetted-solid surface, over which a gas flows at known conditions. Evaporation may occur into a pure inert gas, or into one pre-loaded with a known fraction of one or more of the ternary components. The model developed here uses an exact solution to the Maxwell–Stefan equations for mass transfer in the gas film, with a lumped approach applied to the liquid phase. Solutions to the evaporation model take the form of trajectories in temperature–composition space, which are then projected onto a ternary diagram to form the map. Efficient Newton-based methods are used to calculate the composition and temperature of pseudo-azeotropes in the mixture, and to calculate the wet-bulb temperature at a given composition. A numerical continuation method is used for tracking the bifurcations which occur in the evaporation maps, where the composition of one component of the pre-loaded gas is the bifurcation parameter. The bifurcation diagrams can in principle be used to determine the required gas composition to produce a specific terminal pseudo-azeotrope composition. Provided the gas-phase limited assumption applies, such analysis is applicable to applications such as drying of solvent-based coatings and tray-drying of granulated pharmaceutical products. Abstract : Highlights: Evaporation maps are presented as a novel way of showing composition of residual liquid during gas-phase-limited evaporation and drying. Numerical methods for calculation of wet-bulb temperature and azeotrope location for ternary mixtures are developed. Bifurcation analyses are used to track location of "pseudo-azeotropes" with varying gas composition. Approach may be applied to processes involving evaporation and drying of solvent mixtures, such as evaporation of coating-films and tray-drying of pharmaceutical granulations.