Pulsed field gradient (PFG) NMR measurements have been conducted to measure self-diffusion coefficients of gases within porous media. Analysis of these microscopic data with the use of a previously developed long-range diffusion model has enabled us to accurately predict breakthrough curves for transport through packed-bed adsorption columns, and the length of unused bed (LUB). This methodology enables the evaluation of mass-transfer coefficients without the complications associated with transient sorption experiments, that is, heat effects, and thereby offers a reasonable alternative to conventional breakthrough experimentation for the evaluation of mass-transfer coefficients, and LUB for large-scale unit operations. © 2004 American Institute of Chemical EngineersAIChE J, 50: 589 -595, 2004
IntroductionThe dynamics of gas adsorption within a packed-bed adsorbent column are dictated by gas-solid phase equilibria, heat transfer, mass transfer, and their mutual coupling. Any transient sorption experiment involves the generation of heat because of the heat of adsorption, and, consequently, a temporary desorption of gas from the solid surface because of the increase of the sample temperature. The swing in temperature in turn directly affects gas diffusion rates. Separating and quantifying these three aspects of adsorption has been the focus of continued research efforts of adsorption scientists (Ruthven, 1984). Consequently, new experimental techniques that enable the decoupling of heat and mass transfer from equilibrium measurements are continuously being sought after as are theoretical insights which enable large-scale adsorption behavior to be predicted from microscopic measurements (Eic et al., 1988;Sircar et al., 1999;Rynders et al., 1997). Because equilibrium and thermal properties can be easily obtained by performing volumetric or gravimetric isotherm experiments at various temperatures and by micro-calorimetric methods, we focus in this work on defining mass-transfer rates within porous media from lab scale quantities of material, and on applying that information to anticipate large-scale breakthrough behavior.The diffusion coefficient of gases in microporous adsorbent materials is among the most important parameters describing mass transfer through adsorbent beds because diffusion rates often control cycle times, and influence the design of industrial separation processes. Mass transfer through commercial zeolites, which are typically formed by extruding (or pressing) a crystalline powder with a binder into pellets, is generally governed by the rate of macropore diffusion (Kärger et al., 1992).Mass-transfer coefficients of gases in a porous media for industrial gas separation unit operations are traditionally assessed by performing large-scale, transient experiments, such as breakthrough tests, which require large amounts of adsorbent and gas. Furthermore, the data analysis of these experiments is complicated because heat, mass, and equilibrium are coupled, transient, and must be considered explicitly. T...