Effects of capillary condensation on adsorption and thermal desorption dynamics of water in zeolite 13X and layered beds

The effects of capillary condensation on the adsorption and thermal desorption dynamics of water in zeolite 13X beds and layered beds with zeolite 13X/silica gel or zeolite 13X/alumina were experimentally and theoretically studied. As the equilibrium isotherm of water on zeolite 13X pellet was found to be most favorable at a low relative humidity and indicated capillary condensation at a high relative humidity, it was possible to construct a non-isothermal model that included capillary condensation and that could successfully predict plateaus of temperature and concentration profiles in thermal regeneration. In adsorption breakthrough, by using a feed in the capillary condensation range of the isotherm on zeolite 13X, the breakthrough curve showed a shock wave in the low concentration and a proportionate pattern in the high concentration. In thermal desorption breakthrough, the desorbed water at the upper part of the bed was re-adsorbed at the lower part of the bed, and that re-adsorption mainly occurred in the capillary condensation range of the isotherm. Therefore, even though an adsorption was performed at a feed in the favorable range of the isotherm, and could be well predicted with type I isotherm, its desorption dynamics should be predicted by using the isotherm model with its consideration of capillary condensation. The layered bed with silica gel or alumina did not have any advantage over the zeolite 13X bed with respect to adsorption breakthrough performance. However, compared to the zeolite 13X bed, the complete regeneration time in the layered bed was drastically shortened due to a greater variation of the amount of equilibrium adsorption of water under temperature on both silica gel and alumina. In addition, since an increase in temperature led to a greater decrease of the amount of equilibrium adsorption of water on silica gel than on alumina, a layered bed with silica gel obviously could be regenerated more efficiently than a layered bed with alumina.

[1]  N. Wakao,et al.  Effect of fluid dispersion coefficients on particle-to-fluid heat transfer coefficients in packed beds , 1978 .

[2]  H. Ahn,et al.  Backfill Cycle of a Layered Bed H2 PSA Process , 1999 .

[3]  K. S. Knaebel,et al.  Pressure swing adsorption , 1993 .

[4]  H. Ahn,et al.  Adsorption dynamics of water in layered bed for air‐drying tsa process , 2003 .

[5]  N. Wakao,et al.  EFFECT OF FLUID DISPERSION COEFFICIENTS ON PARTICLE-TO-FLUID MASS TRANSFER COEFFICIENTS IN PACKED BEDS. CORRELATION OF SHERWOOD NUMBERS , 1978 .

[6]  R. Reid,et al.  The Properties of Gases and Liquids , 1977 .

[7]  J. Carter,et al.  The simultaneous adsorption of carbon dioxide and water vapour by fixed beds of molecular sieves , 1974 .

[8]  Jin Tae Kim,et al.  Adsorption equilibria of water vapor on alumina, zeolite 13X, and a zeolite X/activated carbon composite , 2003 .

[9]  R. T. Yang,et al.  Adsorber dynamics and optimal design of layered beds for multicomponent gas adsorption , 1998 .

[10]  Ravi Kumar,et al.  Nonequilibrium, nonisothermal desorption of single adsorbate by purge , 1986 .

[11]  Chang-Ha Lee,et al.  Effects of carbon‐to‐zeolite ratio on layered bed H2 PSA for coke oven gas , 1999 .

[12]  Seung Ju Lee,et al.  Adsorption equilibrium and kinetics of H2O on zeolite 13x , 2001 .

[13]  C. Pan,et al.  Nonisothermal Desorption by Gas Purge of Single Solutes in Fixed-Bed Adsorbers. I. Equilibrium Theory , 1975 .

[14]  R. T. Yang,et al.  Air-prepurification by pressure swing adsorption using single/layered beds , 2001 .

[15]  James A. Ritter,et al.  Evaluation of model approximations in simulating pressure swing adsorption-solvent vapor recovery , 1997 .

[16]  Sung-Yong Cho,et al.  Adsorption and thermal regeneration of methylene chloride vapor on an activated carbon bed , 1997 .

[17]  Douglas M. Ruthven,et al.  Principles of Adsorption and Adsorption Processes , 1984 .

[18]  J. Fair,et al.  Study of the adsorption and desorption of multiple adsorbates in a fixed bed , 1988 .

[19]  J. Fair,et al.  Parametric analysis of thermal regeneration of adsorption beds , 1988 .

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

[21]  Min-Bae Kim,et al.  Effects of Heat-Transfer Coefficients on Thermal Dynamics in a Near-Adiabatic Fixed Bed , 2004 .

[22]  D. Ruthven,et al.  Heat effects in adsorption column dynamics. 1. Comparison of one- and two-dimensional models , 1990 .

[23]  R. T. Yang,et al.  Gas Separation by Adsorption Processes , 1987 .

[24]  M. Setzer,et al.  A model to describe adsorption isotherms , 1996 .