Modeling and Simulation of CO2 Absorption with Amine Component Solvent
Chen, Y. J. ; Yao, Y. H. ; Zhang, X. P. ; Li, C. S. ; Dong, H. F. ; Huang, Y. ; Ren, B. Z.
2012
会议名称11th International Symposium on Process Systems Engineering (PSE)
会议日期JUL 15-19, 2012
会议地点Singapore, SINGAPORE
关键词CO2 capture Blended amine Electrolyte-NRTL model Simulation VAPOR-LIQUID-EQUILIBRIUM CARBON-DIOXIDE MONOETHANOLAMINE
页码525-529
中文摘要Blended amine solvent has been shown unique and predominant performance while used to capture CO2 compared with the single amine solvent. Calculations were compared with experimental solubility measurements of CO2 in aqueous ternary and quaternary systems of H2O, MEA and AMP. Electrolyte non-random two liquid (ENRTL) theory was employed to fit solubility data in three ternary systems CO2-H2O-MEA and CO2-H2O-AMP. The binary interaction energy parameters for the ionic species were obtained by regression of the experimental solubility data of the ternary systems. A good agreement between the calculated values and the experimental data was achieved. Process simulation for CO2 removal using an equilibrium approach was performed with newly fitted parameters. The simulation results have been compared with the pilot plant experimental data.
收录类别CPCI
会议网址://WOS:000316676100097
会议录11th International Symposium on Process Systems Engineering, Pts a and B
语种英语
内容类型会议论文
源URL[http://ir.ipe.ac.cn/handle/122111/11079]  
专题过程工程研究所_研究所(批量导入)
推荐引用方式
GB/T 7714
Chen, Y. J.,Yao, Y. H.,Zhang, X. P.,et al. Modeling and Simulation of CO2 Absorption with Amine Component Solvent[C]. 见:11th International Symposium on Process Systems Engineering (PSE). Singapore, SINGAPORE. JUL 15-19, 2012.://WOS:000316676100097.
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