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The further activation and functionalization of semicoke for CO2 capture from flue gases.
Wang, Xia; Zeng, Wulan; Guo, Qingjie; Geng, Qijin; Yan, Yongmei; Hu, Xiude.
  • Wang X; Department of Chemistry and Chemical Engineering, Weifang University Weifang 261061 Shandong China xiawangwfu@163.com +86 536 8785283 +86 536 8785283.
  • Zeng W; Department of Chemistry and Chemical Engineering, Weifang University Weifang 261061 Shandong China xiawangwfu@163.com +86 536 8785283 +86 536 8785283.
  • Guo Q; State Key Laboratory of High-efficiency Utilization of Coal and Green Chemical Engineering, Ningxia University Yinchuan 750021 China.
  • Geng Q; Department of Chemistry and Chemical Engineering, Weifang University Weifang 261061 Shandong China xiawangwfu@163.com +86 536 8785283 +86 536 8785283.
  • Yan Y; Department of Chemistry and Chemical Engineering, Weifang University Weifang 261061 Shandong China xiawangwfu@163.com +86 536 8785283 +86 536 8785283.
  • Hu X; State Key Laboratory of High-efficiency Utilization of Coal and Green Chemical Engineering, Ningxia University Yinchuan 750021 China.
RSC Adv ; 8(62): 35521-35527, 2018 Oct 15.
Article en En | MEDLINE | ID: mdl-35547898
To systematically study CO2 adsorption performance, semicoke from the low-rank lignite was further activated and functionalized for CO2 capture from flue gases. The effect of the activation conditions, such as the activation temperature, activation time and HCl washing, and the tetraethylenepentamine (TEPA)-functionalization on CO2 adsorption were investigated; the pore structure and surface morphology of the semicoke under different activation conditions were characterized. Both the surface structure and adsorption performance of the activated semicoke could be improved under appropriate activation and acid-treatment conditions. The optimal breakthrough and equilibrium adsorption capacity for the TEPA-functionalized HCl-washed activated semicoke were separately 2.68 and 3.70 mmol g-1 at 60 °C for the simulated flue gas of 15 vol% CO2 and 85 vol% N2. After ten adsorption-desorption cycles, the equilibrium adsorption capacity was still 3.43 mmol g-1, and the semicoke-based sorbent showed good regenerability.