Highlighting the Role of Activated Carbon Particle Size on CO2 Capture from Model Flue Gas

被引:34
作者
Balsamo, Marco [1 ]
Rodriguez-Reinoso, Francisco [2 ]
Montagnaro, Fabio [3 ]
Lancia, Amedeo [1 ]
Erto, Alessandro [1 ]
机构
[1] Univ Naples Federico II, Dipartimento Ingn Chim Mat & Prod Ind, I-80125 Naples, Italy
[2] Inst Univ Mat, Lab Mat Avanzados, Dept Quim Inorgan, E-03080 Alicante, Spain
[3] Univ Naples Federico II, Dipartimento Sci Chim, I-80126 Naples, Italy
关键词
COAL COMBUSTION ASH; DIOXIDE CAPTURE; ADSORPTION; KINETICS; GASIFICATION; CAPACITY; SEQUESTRATION; EQUILIBRIA; SORBENT; REUSE;
D O I
10.1021/ie4018034
中图分类号
TQ [化学工业];
学科分类号
081705 [工业催化];
摘要
CO2 adsorption onto two particle size classes of the commercial activated carbon Filtrasorb 400, namely 600-900 pm (sample F600-900) and 900-1200 mu m (sample F900-1200), was investigated at 293 K under model flue gas conditions in a fixed-bed column. Equilibrium adsorption capacity for a typical 15% CO2 postcombustion effluent was 0.7 mol kg(-1) for both investigated adsorbents. In both cases, CO2 breakthrough curves showed a reduction of the characteristic breakpoint time and faster capture kinetics at higher pollutant concentration in the feed (in the range 1-15%). Dynamic adsorption data highlighted the important role played by wider micropores in determining a quicker adsorption process for finer particles. Mathematical modeling of the 15% CO2 breakthrough curve allowed identifying intraparticle diffusion as the limiting step of the adsorption process. Numerical analysis provided values of the intraparticle mass-transfer resistances equal to 1.7 and 3.3 s for F600-900 and F900-1200, respectively.
引用
收藏
页码:12183 / 12191
页数:9
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