Solubility of CO2 in 1-(2-hydroxyethyl)-3-methylimidazolium ionic liquids with different anions

Jalili, Amir Hossein; Mehdizadeh, Amir; Shokouhi, Mohammad; Sakhaeinia, Hossein; Taghikhani, Vahid

doi:10.1016/j.jct.2010.02.002

Cited by 99 publications

(51 citation statements)

References 26 publications

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“…The partial molar differences in enthalpy and entropy between the two states can be obtained by calculating the corresponding partial derivatives of the Gibbs free energy with respect to temperature The pressure range considered in this work is not too high to cause Henry's law constant to be a strong function of pressure and Henry's law is weakly dependent on pressure under the specified conditions. Therefore, it does not give rise to large errors if one ignores this pressure dependency [18,[21][22][23]. By means of this approximation and using equations (9)-(11), we estimated the thermodynamic functions of solution at infinite dilution for H 2 S and CO 2 in the IL.…”

Section: Resultsmentioning

confidence: 99%

“…diffusion coefficients of gases at various temperatures and pressures. In the past few years, a growing number of measurements reporting solubility and diffusion of CO 2 in various ILs have become available [5][6][7][8][9][10][11][12][13][14][15][16][17][18]. However, experimental data for the solubility and diffusion of hydrogen sulfide in ILs are scarce.…”

Section: Introductionmentioning

confidence: 99%

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Solubility and diffusion of CO2 and H2S in the ionic liquid 1-ethyl-3-methylimidazolium ethylsulfate

Jalili

Mehdizadeh

Shokouhi

et al. 2010

The Journal of Chemical Thermodynamics

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179

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Section: Resultsmentioning

confidence: 99%

Section: Introductionmentioning

confidence: 99%

Solubility and diffusion of CO2 and H2S in the ionic liquid 1-ethyl-3-methylimidazolium ethylsulfate

Jalili

Mehdizadeh

Shokouhi

et al. 2010

The Journal of Chemical Thermodynamics

Self Cite

179

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“…All the data exhibit linearity with zero intercept, which suggests the validity of the Henry's law [16]. Such physical solubility can also be observed in many non-task-specific ILs [17][18][19][20].…”

Section: Resultsmentioning

confidence: 86%

Solubility of CO2 in amide-based Brønsted acidic ionic liquids

Deng¹,

Cui²,

Chen³

et al. 2013

The Journal of Chemical Thermodynamics

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“…36 The comprehensive effects of the factors caused that CO 2 absorption performance increased and then decreased with the increase of n I .…”

Section: Physical Properties Of the Investigated Solventsmentioning

confidence: 98%

Enhancement of CO₂ capture performance of aqueous MEA by mixing with [NH₂e-mim][BF₄]

Wang

Rao

et al. 2018

RSC Adv.

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Alcohol amine solutions have a high absorption capacity and rate for CO 2 capture, however, there are some shortcomings such as high energy-consumption and low stability. To enhance CO 2 capture performance of aqueous MEA, a functional ionic liquid ([NH 2 e-mim][BF 4 ]) was introduced based on the advantages for CO 2 capture. Absorbents were prepared with the molar concentration ratio of [NH 2 e-mim] [BF 4 ] to the 30 vol% aqueous MEA of 0 : 10, 1 : 9, 2 : 8, 3 : 7, 4 : 6 and 6 : 4. The density and the viscosity of the investigated absorbents were measured and the effects of the molar fraction of [NH 2 e-mim][BF 4 ] (n I ) and temperature on CO 2 absorption performance were investigated. CO 2 desorption performance of the solvent at different temperatures was discussed. The stability performance of the absorbent with n I of 2 : 8 (I/M 2:8 ) was examined by five consecutive cyclic tests. The results showed that for pure CO 2 , the I/M 2:8 displayed the highest absorption performance at 303 K under 1 bar: a comparable CO 2 absorption capacity of the 30 vol% aqueous MEA and a higher CO 2 absorption rate at the later absorption stage.Moreover, with the increase of temperature, CO 2 absorption capacity and rate decreased, while CO 2 desorption efficiency and rate increased. 393 K was chosen as the optimum desorption temperature with the desorption efficiency of 99.31%. The introducing of IL contributed to CO 2 desorption performance of the absorbents significantly. The properties (CO 2 absorption capacity, mass loss, density and viscosity) of the I/M 2:8 during the cycles suggested that the IL-MEA mixture had an excellent stability performance.

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Solubility of CO2 in 1-(2-hydroxyethyl)-3-methylimidazolium ionic liquids with different anions

Cited by 99 publications

References 26 publications

Solubility and diffusion of CO2 and H2S in the ionic liquid 1-ethyl-3-methylimidazolium ethylsulfate

Solubility and diffusion of CO2 and H2S in the ionic liquid 1-ethyl-3-methylimidazolium ethylsulfate

Solubility of CO2 in amide-based Brønsted acidic ionic liquids

Enhancement of CO₂ capture performance of aqueous MEA by mixing with [NH₂e-mim][BF₄]

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Solubility of CO2 in 1-(2-hydroxyethyl)-3-methylimidazolium ionic liquids with different anions

Cited by 99 publications

References 26 publications

Solubility and diffusion of CO2 and H2S in the ionic liquid 1-ethyl-3-methylimidazolium ethylsulfate

Solubility and diffusion of CO2 and H2S in the ionic liquid 1-ethyl-3-methylimidazolium ethylsulfate

Solubility of CO2 in amide-based Brønsted acidic ionic liquids

Enhancement of CO2 capture performance of aqueous MEA by mixing with [NH2e-mim][BF4]

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Enhancement of CO₂ capture performance of aqueous MEA by mixing with [NH₂e-mim][BF₄]