Simulation of Aqueous Blend of Monoethanolamine and Glycerol for Carbon Dioxide Capture from Flue Gas

被引:13
|
作者
Mirzaei, Somayeh [1 ]
Shamiri, Ahmad [2 ,3 ]
Aroua, Mohamed Kheireddine [1 ]
机构
[1] Univ Malaya, Chem Engn Dept, Fac Engn, Kuala Lumpur 50603, Malaysia
[2] UCSI Univ, Chem & Petr Engn Dept, Fac Engn Technol & Built Environm, Kuala Lumpur 56000, Malaysia
[3] UCSI Univ, Proc Syst Engn Ctr, Fac Engn Technol & Built Environm, Kuala Lumpur 56000, Malaysia
关键词
VAPOR-LIQUID-EQUILIBRIA; RATE-BASED MODEL; CO2; CAPTURE; MASS-TRANSFER; PACKED-COLUMN; N-METHYLDIETHANOLAMINE; ALKANOLAMINE SYSTEMS; PHYSICAL-PROPERTIES; ABSORPTION; MIXTURES;
D O I
10.1021/acs.energyfuels.6b01230
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
This study investigated CO2 capture from flue gas by using glycerol as solvent. Absorption was simulated using a rate-based model with three cases under similar operating conditions. CO2 separation was first simulated using ENRTL-RK thermodynamic model with monoethanolamine (MEA) as. solvent. CO2 absorption was then simulated using NRTL-RK thermodynamic model with glycerol solvent, and then an aqueous mixture of MEA/glycerol was also simulated using ENRTL-RK thermodynamic model. Simulation results confirm that glycerol can be used as promoter with MEA solvent to enhance CO2 capture. The optimal glycerol concentration for CO2 absorption is 10-40 wt %, in which 10 wt % glycerol exhibits the lowest CO2 concentration in the outlet gas from the absorber. The CO2 removal efficiency increases from 62.24% for 10 wt % MEA aqueous solution to 64.33% for the mixture of 10 wt % MEA-10 wt % glycerol aqueous solution. The CO2 removal efficiency for 10 wt % glycerol aqueous solution is 27.31%.
引用
收藏
页码:9540 / 9553
页数:14
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