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 | |
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. |
个性服务 |
查看访问统计 |
相关权益政策 |
暂无数据 |
收藏/分享 |
除非特别说明,本系统中所有内容都受版权保护,并保留所有权利。
修改评论