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Adsorption of CO 2 by surface modified coal-based activated carbons: kinetic and thermodynamic analysis
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Abstract
The effects of different surface modifiers on the CO
2
adsorption capacity of coal-based activated carbons were studied, and the diffusion behavior, adsorption kinetics and thermodynamic parameters of CO
2
in activated carbons were analyzed. The results show that compared with ethylene glycol, 1,2-propylenediamine and zinc chloride, potassium hydroxide and sodium hydroxide can greatly improve CO
2
adsorption capacity. The adsorption rate is faster, and the adsorption capacity is larger, with the maximum CO
2
adsorption capacity being 33.54 mL/g. Fick's law can well describe the diffusion behavior of CO
2
in activated carbon. The addition of a surface modifier can increase the diffusion coefficient. The diffusion of CO
2
in activated carbon falls into the category of crystal diffusion. The adsorption kinetics of CO
2
before and after surface modification follow the Bangham equation. During the adsorption process, δ H < 0, δ G < 0, δ S < 0. Surface modification can reduce adsorption heat and promote adsorption, and the adsorption process is dominated by physisorption.
Walter de Gruyter GmbH
Title: Adsorption of CO
2
by surface modified coal-based activated carbons: kinetic and thermodynamic analysis
Description:
Abstract
The effects of different surface modifiers on the CO
2
adsorption capacity of coal-based activated carbons were studied, and the diffusion behavior, adsorption kinetics and thermodynamic parameters of CO
2
in activated carbons were analyzed.
The results show that compared with ethylene glycol, 1,2-propylenediamine and zinc chloride, potassium hydroxide and sodium hydroxide can greatly improve CO
2
adsorption capacity.
The adsorption rate is faster, and the adsorption capacity is larger, with the maximum CO
2
adsorption capacity being 33.
54 mL/g.
Fick's law can well describe the diffusion behavior of CO
2
in activated carbon.
The addition of a surface modifier can increase the diffusion coefficient.
The diffusion of CO
2
in activated carbon falls into the category of crystal diffusion.
The adsorption kinetics of CO
2
before and after surface modification follow the Bangham equation.
During the adsorption process, δ H < 0, δ G < 0, δ S < 0.
Surface modification can reduce adsorption heat and promote adsorption, and the adsorption process is dominated by physisorption.
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