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Mechanism and Kinetics of CO2 Absorption into an Aqueous Solution of a Triamino-Functionalized Ionic Liquid

机译:三氨基功能化离子液体在水溶液中吸收CO2的机理和动力学

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摘要

A novel ionic liquid (1-aminoethyl-3-methylimidazolium lysinate, [C(2)NH(2)MIm][Lys]) functionalized with three amino groups had been developed for carbon dioxide (CO2) capture in this work. The CO2 absorption loading of [C(2)NH(2)MIm] [Lys] solution was found to be 1.59 mol CO2/mol IL with a concentration of 0.5 mol/L at 313.15 K, which was much higher than that of the most existing dual functionalized Its. Besides, [C(2)NH(2)MIm] [Lys] also owned a good regenerability even after 6 regeneration cycles. According to the results of C-13 nuclear magnetic resonance (C-13 NMR), CO2 absorption into [C(2)NH(2)MIm] [Lys] solution could be divided into two stages, which began with the formation of carbamate, and followed by the hydration of CO2 to form carbonate/bicarbonate. Meanwhile, the desorption of the saturated [C(2)NH(2)MIm] [Lys] was proven to be a reverse process of the adsorption. Based on the Mechanism results, the kinetics of CO2 capture into [C(2)NH(2)MIm] [Lys] solution was investigated by using a double stirred-cell absorber at temperatures ranging from 303 to 333 K. Under the pseudo first-order regime, the overall reaction rate constants (k(ov).) and the forward second-order rate constants (k(2)) under different concentrations and temperature were obtained, which were both increased considerably as temperature increased. Moreover, the values of enhancement factor (E) were linear with C-RNR2 and temperature. The Arrhenius equation of CO2 absorption was also estimated, and the activation energy was calculated to be 25.5 kJ.mol(-1).
机译:已经开发了一种具有三个氨基官能化的新型离子液体(1-氨基乙基-3-甲基咪唑鎓赖氨酸盐,[C(2)NH(2)MIm] [Lys]),用于捕获二氧化碳(CO2)。发现[C(2)NH(2)MIm] [Lys]溶液的CO2吸收负荷为1.59 mol CO2 / mol IL,在313.15 K时的浓度为0.5 mol / L,远高于其大多数现有的双重功能化了。此外,即使经过6个再生循环,[C(2)NH(2)MIm] [Lys]也具有良好的再生性。根据C-13核磁共振(C-13 NMR)的结果,可将CO2吸收到[C(2)NH(2)MIm] [Lys]溶液中分为两个阶段,从形成氨基甲酸酯开始,然后将CO2水合形成碳酸盐/碳酸氢盐。同时,饱和[C(2)NH(2)MIm] [Lys]的解吸被证明是吸附的逆过程。根据机理结果,使用双搅拌池吸收器在303至333 K的温度下研究了CO2捕集到[C(2)NH(2)MIm] [Lys]溶液中的动力学。获得不同浓度和温度下的总反应速率常数(k(ov)。)和正向二阶速率常数(k(2)),它们均随温度升高而显着增加。此外,增强因子(E)的值与C-RNR2和温度呈线性关系。还估算了Arrhenius的CO2吸收方程,计算出的活化能为25.5 kJ.mol(-1)。

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  • 来源
    《Energy & fuels》 |2017年第2期|1793-1802|共10页
  • 作者单位

    Huaqiao Univ, Coll Chem Engn, Xiamen 361021, Peoples R China;

    Huaqiao Univ, Coll Chem Engn, Xiamen 361021, Peoples R China;

    Huaqiao Univ, Coll Chem Engn, Xiamen 361021, Peoples R China;

    Huaqiao Univ, Coll Chem Engn, Xiamen 361021, Peoples R China;

    Huaqiao Univ, Coll Chem Engn, Xiamen 361021, Peoples R China;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
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  • 入库时间 2022-08-18 00:39:28

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