On the use of the dual-process Langmuir model for correlating unary equilibria and predicting mixed-gas adsorption equilibria.

A new model has been developed for predicting mixed-gas adsorption equilibria from multicomponent gas mixtures based on the dual-process Langmuir (DPL) formulation. It predicts ideal, nonideal, and azeotropic adsorbed solution behavior from a knowledge of only single-component adsorption isotherms and the assertion that each binary pair in the gas mixture correlates in either a perfect positive (PP) or perfect negative (PN) fashion on each of the two Langmuir sites. The strictly PP and strictly PN formulations thus provide a simple means for determining distinct and absolute bounds of the behavior of each binary pair, and the PP or PN behavior can be confirmed by comparing predictions to binary experimental adsorption equilibria or from intuitive knowledge of binary pairwise adsorbate-adsorbent interactions. The extension to ternary and higher-order systems is straightforward on the basis of the pairwise additivity of the binary adsorbent-adsorbate interactions and two rules that logically restrict the combinations of PP and PN behaviors between binary pairs in a multicomponent system. Many ideal and nonideal binary systems and two ternary systems were tested against the DPL model. Each binary adsorbate-adsorbent pair exhibited either PP or PN behavior but nothing in between. This binary information was used successfully to predict ternary adsorption equilibria based on binary pairwise additivity. Overall, predictions from the DPL model were comparable to or significantly better than those from other models in the literature, revealing that its correlative and predictive powers are universally applicable. Because it is loading-explicit, simple to use, and also accurate, the DPL model may be one of the best equilibrium models to use in gas-phase adsorption process simulation.

[1]  J. A. Ritter,et al.  Simulation of gasoline vapor recovery by pressure swing adsorption , 2000 .

[2]  N. Sundaram Equation for adsorption from gas mixtures , 1995 .

[3]  A. Myers Activity coefficients of mixtures adsorbed on heterogeneous surfaces , 1983 .

[4]  T. L. Hill,et al.  Statistical Mechanics of Adsorption. VI. Localized Unimolecular Adsorption on a Heterogeneous Surface , 1949 .

[5]  I. Langmuir THE ADSORPTION OF GASES ON PLANE SURFACES OF GLASS, MICA AND PLATINUM. , 1918 .

[6]  S. Sircar Influence of adsorbate size and adsorbent heterogeneity of IAST , 1995 .

[7]  M. Rao,et al.  Calorimetric Heats of Adsorption and Adsorption Isotherms. 1. O2, N2, Ar, CO2, CH4, C2H6, and SF6 on Silicalite , 1996 .

[8]  C. Tien,et al.  Adsorption of gas mixtures on adsorbents with heterogeneous surfaces , 1988 .

[9]  Runsheng Bai Effect of energy correlation on multicomponent adsorption equilibria prediction using heterogeneous extended Langmuir model , 2000 .

[10]  D. Do,et al.  On the Azeotropic Behaviour of Adsorption Systems , 1999 .

[11]  Paul A. Webley,et al.  Fast finite-volume method for PSA/VSA cycle simulation-experimental validation , 2001 .

[12]  Chang-Ha Lee,et al.  Adsorption dynamics of a layered bed PSA for H2 recovery from coke oven gas , 1998 .

[13]  R. Danner,et al.  Mixture Adsorption Equilibria of Ethane and Ethylene on 13X Molecular Sieves , 1978 .

[14]  M. Douglas LeVan,et al.  Binary Langmuir and Freundlich isotherms for ideal adsorbed solutions , 1981 .

[15]  J. A. Ritter,et al.  New model that describes adsorption of laterally interacting gas mixtures on random heterogeneous surfaces. 1. Parametric study and correlation with binary data , 1998 .

[16]  Imre Zwiebel,et al.  Multicomponent adsorption equilibria of nonideal mixtures , 1986 .

[17]  James A. Ritter,et al.  An extended Langmuir model for adsorption of gas mixtures on heterogeneous surfaces , 1990 .

[18]  R. Gorte,et al.  Calorimetric Heats of Adsorption and Adsorption Isotherms. 2. O2, N2, Ar, CO2, CH4, C2H6, and SF6 on NaX, H-ZSM-5, and Na-ZSM-5 Zeolites , 1996 .

[19]  James A. Ritter,et al.  Solvent Vapor Recovery by Pressure Swing Adsorption. III. Comparison of Simulation with Experiment for the Butane—Activated Carbon System , 1999 .

[20]  A. Myers,et al.  Mixed-Gas Adsorption , 2001 .

[21]  Alírio E. Rodrigues,et al.  A General Package for the Simulation of Cyclic Adsorption Processes , 1999 .

[22]  Y. C. Chen,et al.  A versatile process simulator for adsorptive separations , 1994 .

[23]  Ravi Kumar,et al.  Correlation of Multicomponent Gas Adsorption by the Dual-Site Langmuir Model. Application to Nitrogen/Oxygen Adsorption on 5A-Zeolite , 1996 .

[24]  James A. Ritter,et al.  Pressure swing adsorption cycles for improved solvent vapor enrichment , 2000 .

[25]  T. J. Lafrenz,et al.  A New Adsorption Model for Analyzing Gas−Solid Equilibria in Porous Materials , 1996 .

[26]  A. Myers,et al.  Adsorption of Gas Mixtures: Effect of Energetic Heterogeneity , 1988 .

[27]  W. T. Ziegler,et al.  Adsorption of Methane, Ethane, and Ethylene Gases and Their Binary and Ternary Mixtures and Carbon Dioxide on Activated Carbon at 212-301 K and Pressures to 35 Atmospheres , 1980 .

[28]  James A. Ritter,et al.  Stripping PSA cycles for CO2 recovery from flue gas at high temperature using a hydrotalcite-like adsorbent , 2006 .