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Updated: Aug 5, 2026

Dynamic Pore-scale Reservoir-condition Imaging of Reaction in Carbonates Using Synchrotron Fast Tomography
Published on: February 21, 2017
CO2-induced pore blocking in dolomite during the carbonation stage of the calcium looping process
Rubens C Toledo1, Tadakadzwa Pswarayi2, David V Valim1
1UNESP - São Paulo State University, School of Engineering and Science, Department of Energy and Chemistry, LC3 - Laboratory of Combustion and Carbon Capture, Guaratinguetá, 12516-410, SP, Brazil.
Abstract:
The continuing development of carbon capture technologies, particularly calcium looping (CaL), relies on optimizing sorbent performance and understanding degradation mechanisms. CaL long-term efficiency is compromised by sorbent deactivation, primarily due to pore blockage during carbonation and sintering over repeated calcination/carbonation cycles. This study focuses on elucidating the pore blockage phenomena in a Brazilian dolomite-based sorbent during the carbonation stage. Dolomite samples were subjected to partial carbonation in a vertical tubular reactor for residence times ranging from 0 to 60 min. Thermogravimetric analysis (TGA) was employed to validate the carbonation states achieved during sample preparation, whereas N2 porosimetry was used to monitor the temporal evolution of pore blockage. A novel approach utilizing the Kullback-Leibler divergence was employed to quantify deviations in pore volume distribution caused by carbonation relative to a freshly calcined reference, and the pore size distributions were parameterized using a Beta Probability Density Function (PDF). Porosimetry analysis showed carbonation predominantly affected mesopores in the 30-100 Å range. While pore blockage was initially distributed relatively uniformly across pore sizes, after about 10 min it became increasingly localized within this specific pore size interval, resulting in a progressive shift of the overall distribution toward smaller pores. Notably, even after 60 min of carbonation, a residual pore volume remains available. The proposed methodology successfully quantified the transition from the kinetically controlled to the diffusion-controlled carbonation stage within approximately 5-7.5 min. The Beta PDF provided an excellent fit to the experimental pore size distributions (R2≥0.90), and the proposed correlation for pore blockage dynamics reproduced the experimental behavior with satisfactory accuracy (mean R2=0.76). Overall, this framework demonstrates the potential of combining Beta-PDF modeling and Kullback-Leibler divergence as quantitative tools for investigating pore blockage phenomena in CaL sorbents.
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