Diffusion mechanism of CO2 in 13X zeolite beads

A systematic study of the diffusion mechanism of CO2 in commercial 13X zeolite beads is presented. In order to gain a complete understanding of the diffusion process of CO2, kinetic measurements with a Zero Length Column (ZLC) system and a volumetric apparatus have been carried out. The ZLC experiments were carried out on a single bead of zeolite 13X at 38 °C at a partial pressure of CO2 of 0.1 bar, conditions representative of post-combustion capture. Experiments with different carrier gases clearly show that the diffusion process is controlled by the transport inside the macropores. Volumetric measurements using a Quantachrome Autosorb system were carried out at different concentrations. These experiments are without a carrier gas and the low pressure measurements show clearly Knudsen diffusion control in both the uptake cell and the bead macropores. At increasing CO2 concentrations the transport mechanism shifts from Knudsen diffusion in the macropores to a completely heat limited process. Both sets of experiments are consistent with independent measurements of bead void fraction and tortuosity and confirm that under the range of conditions that are typical of a carbon capture process the system is controlled by macropore diffusion mechanisms.

[1]  T. Chakrabarti,et al.  Concentration and Recovery of Coliphages from Water with Bituminous Coal , 2008, Water environment research : a research publication of the Water Environment Federation.

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

[3]  D. Ruthven,et al.  Analysis of ZLC desorption curves for gaseous systems , 1996 .

[4]  K. P. Möller,et al.  The effect of a crystal size distribution on ZLC experiments , 2002 .

[5]  Jun Zhang,et al.  Capture of CO2 from high humidity flue gas by vacuum swing adsorption with zeolite 13X , 2008 .

[6]  Alírio E. Rodrigues,et al.  Adsorption Equilibrium of Methane, Carbon Dioxide, and Nitrogen on Zeolite 13X at High Pressures , 2004 .

[7]  M. Kočiřík,et al.  Analytical solution of simultaneous mass and heat transfer in zeolite crystals under constant-volume/variable-pressure conditions , 1984 .

[8]  M. Douglas LeVan,et al.  Measurement of Mass Transfer Rates in Adsorbents: New Combined-Technique Frequency Response Apparatus and Application to CO2 in 13X Zeolite , 2012 .

[9]  D. Ruthven,et al.  Analysis of thermal effects in adsorption rate measurements , 1979 .

[10]  S. Hyun,et al.  Diffusion Mechanism of Carbon Dioxide in Zeolite 4A and CaX Pellets , 2004 .

[11]  Armin D. Ebner,et al.  State-of-the-art Adsorption and Membrane Separation Processes for Carbon Dioxide Production from Carbon Dioxide Emitting Industries , 2009 .

[12]  G. Onyestyák,et al.  Frequency Response Study of Adsorbate Mobilities of Different Character in Various Commercial Adsorbents , 1999 .

[13]  D. Ruthven,et al.  Diffusion of oxygen and nitrogen in 5A zeolite crystals and commercial 5A pellets , 1993 .

[14]  Cheng-Tung Chou,et al.  Carbon dioxide recovery by vacuum swing adsorption , 2004 .

[15]  Andrea Ramírez,et al.  Comparative assessment of CO2 capture technologies for carbon-intensive industrial processes , 2012 .

[16]  John Crank,et al.  The Mathematics Of Diffusion , 1956 .

[17]  Stefano Brandani,et al.  Efficient Simulation and Acceleration of Convergence for a Dual Piston Pressure Swing Adsorption System , 2013 .

[18]  P. Harlick,et al.  An experimental adsorbent screening study for CO2 removal from N2 , 2004 .