Article ID Journal Published Year Pages File Type
6456183 Journal of CO2 Utilization 2017 7 Pages PDF
Abstract

•Biomass-derived activated carbons with high CO2 uptake are successfully prepared.•The highest CO2 capture capacity of 6.03 mmol/g at 273 K and 1 bar is achieved.•The highest CO2 capture capacity of 4.18 mmol/g at 298 K and 1 bar is achieved.•Micropore range for CO2 uptake at various temperatures and pressures are revealed.

This work reports on the preparation and examination of biomass-derived activated carbons featuring high CO2 adsorption capacity. A detailed micropore structure analysis and surface characterization were performed using nitrogen adsorption isotherms at 77 K and carbon dioxide isotherms at 273 K. At 273 K and 1 bar only micropores in the range of 0.30-0.86 nm were mainly effective for CO2 adsorption. When the temperature increased to 298 K, the ranges of effective micropores for CO2 adsorption at 1 bar decreased to 0.30-0.33 nm. For the typical flue gas conditions (partial pressure of CO2 0.15 bar), micropores in the range of 0.30-0.57 nm were mainly effective for CO2 adsorption. The precursor had a strong effect on the textural properties of the resulting carbon and CO2 adsorption. Activated carbon prepared from pomegranate peels showed the highest CO2 adsorption and selectivity (CO2/N2). The experimental isotherm data of activated carbon produced from pomegranate peels were analysed using Langmuir, Freundlich, Sips, and Toth isotherm equations. The fitting details showed that the multitemperature Toth equation is a powerful tool to mathematically represent CO2 isotherms on activated carbon produced from pomegranate peels. The isosteric heat of adsorption was calculated by fitting the Toth equation to the adsorption isotherms and applying the Clausius-Clapeyron equation. The value of the heterogeneity coefficient and isosteric heat of adsorption suggested heterogeneous interactions between CO2 and sorbent surface.

Related Topics
Physical Sciences and Engineering Chemical Engineering Catalysis
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