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Absorption performance of CO2 in high concentrated [Bmim][Lys]-MDEA aqueous solution

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  • Fu, Dong
  • Zhang, Pan
  • Wang, LeMeng

Abstract

The absorption performance of CO2 in 1-butyl-3-methylimidazolium lysinate ([Bmim][Lys]) promoted N-methyldiethanolamine (MDEA) aqueous solution was investigated at the temperatures ranging from 303.2 K to 323.2 K. The mass fractions of MDEA and [Bmim][Lys] respectively ranged from 0.3 to 0.45 and 0.05 to 0.15. The viscosities of CO2-unloaded and CO2-loaded MDEA-[Bmim][Lys] aqueous solutions were measured and modeled. The influences of temperature and concentration on the absorption capacity of CO2 were determined. The effects of temperature, solution concentration and solution viscosity on the absorption rate were illustrated.

Suggested Citation

  • Fu, Dong & Zhang, Pan & Wang, LeMeng, 2016. "Absorption performance of CO2 in high concentrated [Bmim][Lys]-MDEA aqueous solution," Energy, Elsevier, vol. 113(C), pages 1-8.
  • Handle: RePEc:eee:energy:v:113:y:2016:i:c:p:1-8
    DOI: 10.1016/j.energy.2016.07.049
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    References listed on IDEAS

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    1. Zhang, Minkai & Guo, Yincheng, 2013. "Rate based modeling of absorption and regeneration for CO2 capture by aqueous ammonia solution," Applied Energy, Elsevier, vol. 111(C), pages 142-152.
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    3. Fu, Dong & Zhang, Pan, 2015. "Investigation of the absorption performance and viscosity for CO2 capture process using [Bmim][Gly] promoted MDEA (N-methyldiethanolamine) aqueous solution," Energy, Elsevier, vol. 87(C), pages 165-172.
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    Cited by:

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    2. Bikash K. Mondal & Syamalendu S. Bandyopadhyay & Amar N. Samanta, 2017. "Equilibrium solubility measurement and Kent‐Eisenberg modeling of CO 2 absorption in aqueous mixture of N‐methyldiethanolamine and hexamethylenediamine," Greenhouse Gases: Science and Technology, Blackwell Publishing, vol. 7(1), pages 202-214, February.
    3. Zhang, Pan & Tian, XiangFeng & Fu, Dong, 2018. "CO2 removal in tray tower by using AAILs activated MDEA aqueous solution," Energy, Elsevier, vol. 161(C), pages 1122-1132.
    4. Wang, Rujie & Liu, Shanshan & Wang, Lidong & Li, Qiangwei & Zhang, Shihan & Chen, Bo & Jiang, Lei & Zhang, Yifeng, 2019. "Superior energy-saving splitter in monoethanolamine-based biphasic solvents for CO2 capture from coal-fired flue gas," Applied Energy, Elsevier, vol. 242(C), pages 302-310.
    5. Chen, Yifeng & Sun, Yunhao & Yang, Zhuhong & Lu, Xiaohua & Ji, Xiaoyan, 2020. "CO2 separation using a hybrid choline-2-pyrrolidine-carboxylic acid/polyethylene glycol/water absorbent," Applied Energy, Elsevier, vol. 257(C).
    6. Meng, Fanli & Fu, Kun & Wang, Xueli & Wang, Yixiao & Wang, Lemeng & Fu, Dong, 2024. "Study on absorption and regeneration performance of EHA-DMSO non-aqueous absorbent for CO2 capture from flue gas," Energy, Elsevier, vol. 286(C).
    7. Zhou, Xiaobin & Jing, Guohua & Lv, Bihong & Liu, Fan & Zhou, Zuoming, 2019. "Low-viscosity and efficient regeneration of carbon dioxide capture using a biphasic solvent regulated by 2-amino-2-methyl-1-propanol," Applied Energy, Elsevier, vol. 235(C), pages 379-390.

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    Keywords

    Absorption performance; Viscosity; CO2; [Bmim][Lys]; MDEA;
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