TY - JOUR
T1 - Carbon dioxide capture by functionalized solid amine sorbents with simulated flue gas conditions
AU - Liu, Yamin
AU - Ye, Qing
AU - Shen, Mei
AU - Shi, Jingjin
AU - Chen, Jie
AU - Pan, Hua
AU - Shi, Yao
PY - 2011/7/1
Y1 - 2011/7/1
N2 - A novel solid amine sorbent was prepared using KIT-6-type mesoporous silica modified with tetraethylenepentamine (TEPA). Its adsorption behavior toward CO2 from simulated flue gases is investigated using an adsorption column. The adsorption capacities at temperatures of 303, 313, 333, 343, and 353 K are 2.10, 2.29, 2.58, 2.85, and 2.71 mmol g-1, respectively. Experimental adsorption isotherms were obtained, and the average isosteric heat of adsorption was 43.8 kJ/mol. The adsorption capacity increases to 3.2 mmol g-1 when the relative humidity (RH) of the simulated flue gas reaches 37%. The adsorption capacity is inhibited slightly by the presence of SO 2 at concentrations lower than 300 ppm but is not significantly influenced by NO at concentrations up to 400 ppm. The adsorbent is completely regenerated in 10 min at 393 K and a pressure of 5 KPa, with expected consumption energy of about 1.41 MJ kg-1 CO2. The adsorption capacity remains almost the same after 10 cycles of adsorption/regeneration with adsorption conditions of 10 vol % CO2, 100 ppm SO2, 200 ppm NO, 100% relative humidity, and a temperature of 393 K. The solid amine sorbent, KIT-6(TEPA), performs excellently for CO 2 capture and its separation from flue gas.
AB - A novel solid amine sorbent was prepared using KIT-6-type mesoporous silica modified with tetraethylenepentamine (TEPA). Its adsorption behavior toward CO2 from simulated flue gases is investigated using an adsorption column. The adsorption capacities at temperatures of 303, 313, 333, 343, and 353 K are 2.10, 2.29, 2.58, 2.85, and 2.71 mmol g-1, respectively. Experimental adsorption isotherms were obtained, and the average isosteric heat of adsorption was 43.8 kJ/mol. The adsorption capacity increases to 3.2 mmol g-1 when the relative humidity (RH) of the simulated flue gas reaches 37%. The adsorption capacity is inhibited slightly by the presence of SO 2 at concentrations lower than 300 ppm but is not significantly influenced by NO at concentrations up to 400 ppm. The adsorbent is completely regenerated in 10 min at 393 K and a pressure of 5 KPa, with expected consumption energy of about 1.41 MJ kg-1 CO2. The adsorption capacity remains almost the same after 10 cycles of adsorption/regeneration with adsorption conditions of 10 vol % CO2, 100 ppm SO2, 200 ppm NO, 100% relative humidity, and a temperature of 393 K. The solid amine sorbent, KIT-6(TEPA), performs excellently for CO 2 capture and its separation from flue gas.
UR - http://www.scopus.com/inward/record.url?scp=79959912675&partnerID=8YFLogxK
U2 - 10.1021/es200619j
DO - 10.1021/es200619j
M3 - 文章
C2 - 21671647
AN - SCOPUS:79959912675
SN - 0013-936X
VL - 45
SP - 5710
EP - 5716
JO - Environmental Science and Technology
JF - Environmental Science and Technology
IS - 13
ER -