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新型两相吸收剂-离子液体系统高效捕获CO_(2)

Efficient capture of CO2 by a new biphasic solvent-ionic liquid system
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摘要 以四甲基乙二胺(TMEDA)为分相剂,选用了乙醇胺(MEA)、羟乙基乙二胺(AEEA)、三乙烯四胺(TETA)和二乙烯三胺(DETA)四种常用于捕获CO_(2)的一级胺与TMEDA以1∶2的质量比复配,其中TMEDA与AEEA组成的吸收剂吸收一定量的CO_(2)后可以形成液液分相,且吸收CO_(2)效果最佳,饱和吸收负荷可达1.620molCO_(2)/kg。采用1,8-二氮杂双环[5.4.0]十一碳-7-烯-咪唑([DBU][Im])离子液体与TMEDA-AEEA液液两相吸收剂混合,研究[DBU][Im]离子液体对两相吸收剂吸收性能和液液分相的影响,通过碳谱核磁共振法对有机胺及CO_(2)产物的物质分布进行分析。结果表明,向TMEDA-AEEA两相吸收剂中引入[DBU][Im]离子液体有助于提高CO_(2)吸收负荷,[DBU][Im]离子液体、水和CO_(2)反应产物主要分布于下液相,上液相存在TMEDA和少量[DBU][Im]离子液体。当TMEDA、AEEA、水、[DBU][Im]离子液体的质量比为10∶4∶5∶1时,该吸收剂富液相吸收负荷相比TMEDA-AEEA两相吸收剂提高了49.6%。 In this study,tetramethylethylenediamine(TMEDA)was used as phase separating agent,four kinds of amines(ethanolamine,aminoethylethanolamine,triethylenetetramine and diethylenetriamine)that commonly used to capture CO_(2) were mixed with TMEDA in a mass ratio of 1∶2.The solvent composed of TMEDA and AEEA could form a liquid-liquid phase separation after absorbing CO_(2),and had the best CO_(2) absorption characteristics,with absorption loading capacity of 1.620molCO_(2)/kg.The mixture of 1,8-diazabicyclo[5.4.0]undecano-7-en-imidazole([DBU][Im])ionic liquid and TMEDA-AEEA biphasic solvent was used to study the influence of[DBU][Im]on the absorption and phase separation characteristics.The material distribution of organic amine and CO_(2) products in two phases were analyzed by 13C NMR spectrum.It was indicated the introduction of[DBU][Im]ionic liquids into TMEDA-AEEA biphasic solvent was helpful to increase the CO_(2) absorption loading capacity.The[DBU][Im]ionic liquids,water and CO_(2) reaction products were mainly distributed in the lower liquid phase,while TMEDA and a small amount of[DBU][Im]ionic liquids existed in the upper liquid phase.When the mass ratio of TMEDA,AEEA,water and[DBU][Im]ionic liquid was 10∶4∶5∶1,the absorption loading of the rich liquid phase of the absorbent was 49.6%higher than that of TMEDA-AEEA biphasic solvent.
作者 吕超 张习文 金理健 杨林军 LYU Chao;ZHANG Xiwen;JIN Lijian;YANG Linjun(Key Laboratory of Energy Heat Conversion and Process Measurement and Control of the Ministry of Education,Southeast University,Nanjing 210096,Jiangsu,China)
出处 《化工进展》 EI CAS CSCD 北大核心 2023年第6期3226-3232,共7页 Chemical Industry and Engineering Progress
基金 内蒙古自治区科技重大专项(2021ZD0022)。
关键词 二氧化碳 两相吸收剂 [DBU][Im]离子液体 carbon dioxide biphasic solvent [DBU][IM]ionic liquid
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  • 1李长平,辛宝平,徐文国,张琦.疏水性离子液体萃取脱色水溶性染料实验研究[J].北京理工大学学报,2006,26(7):647-650. 被引量:21
  • 2吴庸烈,李国民,李俊凤,刘静芝.水蒸气在高分子膜中的透过行为与气体膜法脱湿[J].膜科学与技术,2007,27(3):1-1. 被引量:10
  • 3Rochelle G T. Amine scrubbing for CO2 capture [J].Science , 2009,325 : 1652 - 1654. 被引量:1
  • 4Freeman S A, Dugas R, Wagener D V, et al. Carbon dioxidecapture with concentrated, aqueous piperazine [J]. EnergyProcedia,2009,1: 1489 - 1496. 被引量:1
  • 5Benamor A,Ali B S,Aroua M K. Kinetic of CO2 absorptionand carbamate formation in aqueous solutions of diethanolamine[J]. Korean J Chem Eng, 2008,25(3) : 451 - 460. 被引量:1
  • 6Zhou S,Chen X,Nguyen T, et al. Aqueous ethlenediaminefor CO2 capture [J]. ChemSusChem , 2010,3 : 913 - 918. 被引量:1
  • 7Dugas R,Rochelle G T. Absorption and desorption rates ofcarbon dioxide with monoethanolamine and piperazine [J],Energy Procedia , 2009,1: 1163 - 1169. 被引量:1
  • 8Bishnoi S,Rochelle G T. Thermodynamics of piperazine/methyldiethanolamine/water/carbon dioxide [J]. Ind EngChem Res,2002,41: 604 - 612. 被引量:1
  • 9Vaidya P D,Kenig E Y. Acceleration of CO2 reaction withN,N-diethylethanolamine in aqueous solutions by piperazine[J]. Ind Eng Chem Res,2008,47: 34 - 38. 被引量:1
  • 10Konduku P, Baidya P, Kenig E. Kinetics of removal ofcarbon dioxide by aqueous solutions of N, N-diethylethanolamineand piperazine [J]. Environ Sci Technol, 2010, 44 : 2138 -2143. 被引量:1

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