Isothermal versus Non-isothermal Adsorption-Desorption Cycling of Triamine-Grafted Pore-Expanded MCM-41 Mesoporous Silica for CO2 Capture from Flue Gas

被引:102
作者
Belmabkhout, Youssef [1 ]
Sayari, Abdelhamid [1 ]
机构
[1] Univ Ottawa, Dept Chem, Ottawa, ON K1N 6N5, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
CARBON-DIOXIDE CAPTURE; SOLID AMINE SORBENT; SWING ADSORPTION; SEPARATION; TECHNOLOGY; REMOVAL; EQUILIBRIUM; TEMPERATURE; ADSORBENTS; DRY;
D O I
10.1021/ef100679e
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
CO2 adsorption-desorption isotherms for triamine-grafted pore-expanded mesoporous silica (TRI-PE-MCM-41) were measured up to 25 bar using the same adsorption and pretreatment temperatures at 298, 323, and 343 K and compared to CO2 adsorption data for 13X zeolite, aminated metal organic framework (Zn-Atz MOF), and Darco activated carbon (Darco-AC). Cyclic isothermal adsorption-desorption measurements of pure CO2 and a 10:90 CO2/N-2 mixture were carried out using vacuum swing (VS) and concentration swing (CS) regeneration modes at 298 and 343 K, in dry and humid conditions, and compared to cyclic non-isothermal desorption measurements, i.e., temperature swing (TS) and temperature-vacuum swing (TVS) regeneration operations. In addition to high CO2 selectivity, it was found that, in comparison to the three other adsorbents, TRI-PE-MCM-41 exhibited higher CO2 uptake in the presence of a 10:90 CO2/N-2 mixture in both dry and humid conditions. Cyclic experiments using VS regeneration mode at 343 K gave a similar CO2 uptake as the TS regeneration mode. Similar to liquid-phase CO2 absorption, SO2 had a deleterious effect on CO2 adsorption.
引用
收藏
页码:5273 / 5280
页数:8
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