Two-Phase Flow in Chromatographic Processes - Experimental and Theoretical Analysis Franziska Ortner and Marco Mazzotti Institute of Process Engineering, ETH Zurich, CH-8092 Zurich, Switzerland [email protected] Motivation Model Equations and Assumptions Interaction of adsorbing components can result in a Experimental evidence of LLPS considerable enrichment in the liquid phase. As a consequence, these components can exceed their solubility limits, and phase separation occurs within the chromatographic column. Liquid-liquid phase separation (LLPS) has been observed for the system phenetole (PNT), 4-tert-Butylphenol (TBP) in the solvent methanol:water 63:37 (v:v) and on a Zorbax 300SB-C18 column[1]. Standard chromatographic models only consider a single convective phase, and thus fail to describe a spontaneous phase split, as well as hydrodynamic effects and adsorption behavior in the presence of multiple convective phases[1,2]. In this contribution, we develop a model accounting for the mentioned effects, and apply it to the experimental system PNT, methanol and water with the adsorbent Zorbax 300SB-C18. Characterization of System Properties Thermodynamic equilibrium between liquid phases Component mass balances Assumptions Variable porosity Volume additivity Thermodyn. equ. between liquid phases Thermodyn. equ. between liquid phases and adsorbed phase see below Hydrodynamic behavior Hydrodynamic behavior • Pressure drop described by extended Darcy’s law: • Neglecting pressure difference of phases due to interfacial tensions Fractional flow[3] with wetting phase w and nonwetting phase nw: equal velocities (simplified approach) different velocities Liquid-liquid equilibria: experimental data and fitted UNIQUAC model • PNT almost completely immiscible with water Experimental UNIQUAC model • Miscibility increases with increasing methanol content • Accurate description with UNIQUAC model • Fitted parameter values: Simulated Profiles Different velocities • Concentration and flow profiles are not identical Comparison with equal velocities Significant differences visible concerning: •Concentration levels (Ci profile) • Differences depend on the determined fractional flow function •Elution times of transitions (Ci and Fi profile) •Types of transitions (Ci and Fi profile) Adsorption behavior Adsorption isotherms based on activities Adsorption isotherms based on concentration Adsorption Flow profile Desorption Adsorption Desorption experimentally accessible • Determined by breakthrough experiments in the soluble region at different solvent ratios (mass fraction of methanol in solvent) experimentally not accessible Concentration profile Validation Experiments UNIQUAC model • Transforming liquid phase concentrations to activities with the established UNIQUAC model, the experimental adsorption data falls on one curve • Description by an anti-Langmuir isotherm, being a function of liquid phase activities Two-phase flow • Displacement of two phases in thermodyn. equ.: decoupling of hydrodynamic effects from adsorption effects Experimental conditions Experimental pressure and flow profiles Experimental conditions quantitative agreement qualitative agreement • All initial and feed states are single phase states, but immiscible → high chance of two-phase flow within the column • Entire chromatographic cycles (adsorption and desorption steps) considered • Quantitative description by model accounting for different velocities. Validation experiments • Relative permeabilities determined from pressure and outlet flow profiles based on mass balance and equilibrium theory equations[4] Relative permeability functions • Displacement of a pure solvent mixture (initial states A) by a mixture of PNT with methanol (feed states B). Adsorption Desorption Adsorption A1 - B1 Desorption A2 – B2 Fractional flow functions References: [1] Jermann, S. et al. J. Chrom. A, 1425 (2015), 116-28 [2] Ortner, F. et al. Ind. Eng. Chem. Res., 54 (2015), 11420−37 [3] Buckley S., Leverett M., Trans. AIME, 146 (1942), 107-16 [4] Marle, C. M. (1981), Multiphase Flow in Porous Media, Gulf Publishing, Houston
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