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Type
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Journal
Article
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|
Author
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Yingying
Zhang
|
|
Author
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Xiaoyan
Ji
|
|
URL
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|
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Volume
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162
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|
Pages
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1160-1170
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Publication
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Applied
Energy
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Date
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January
15, 2016
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|
Abstract
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CO2 capture
and storage can efficiently mitigate CO2 emissions, because CO2 capture is a
crucial energy-intensive process. Ionic liquids (ILs) are potential liquid
absorbents for CO2 separation. Researchers explore the CO2 absorption
capacity and selectivity of ILs. While ILs have been screened for CO2
separation, only specific ILs have been examined in terms of energy
consumption. Researchers collected 76 conventional ILs and screened them in
terms of energy consumption to establish potential ILs for CO2 separation.
Seventeen ILs were screened according to the CO2 dissolution enthalpy and CO2 working capacity criteria obtained from the Henry’s law constant in the preliminary screening. Seven ILs were then screened from the 17 ILs according to the CO2 working capacity from the measured CO2 solubility in the final screening. The energy consumptions of the seven screened ILs (i.e., [Emim][NTf2], [Bmim][BF4], [Bmim][PF6], [Bmim][NTf2], [Hmim][NTf2], [Bmpy][NTf2], and [Hmpy][NTf2]) were calculated, and the corresponding gas solubility selectivities were discussed. The energy consumptions and properties of the seven screened ILs were compared with those of the commercial CO2 absorbents of 30 wt% MEA, 30 wt% MDEA, and dimethyl ethers of polyethylene glycol (Selexol™ or Coastal AGR®). Results revealed that the energy consumptions of the seven screened ILs were lower than those of the commercial CO2 absorbents. [Hmpy][NTf2] showed the lowest energy consumption among the seven screened ILs under the operating conditions set. |
Wednesday, May 4, 2016
Screening of conventional ionic liquids for carbon dioxide capture and separation
Screening
of conventional ionic liquids for carbon dioxide capture and separation
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