TY - JOUR
T1 - Separation factors for [amim]Cl–CO2 biphasic systems from high pressure density and partition coefficient measurements
AU - Hiraga, Yuya
AU - Kato, Aya
AU - Sato, Yoshiyuki
AU - Aida, Taku
AU - Watanabe, Masaru
AU - Smith, Richard L.
N1 - Funding Information:
This work was supported by Japan Society for the Promotion of Science (JSPS) Grant in Aid for JSPS Fellows (Number 254392), Japan
Publisher Copyright:
© 2015 Elsevier B.V.
PY - 2015/11/26
Y1 - 2015/11/26
N2 - In this work, densities and viscosities at atmospheric pressure and densities at high pressures of the ionic liquid, [amim]Cl (1-allyl-3-methylimidazolium chloride) were measured. The densities were evaluated by correlation with the Tait equation and the ePC-SAFT equation of state. Both relationships could describe the experimental density data over the full range of all temperatures (313–373 K) and pressures (0.1–200 MPa) within 0.007% and 0.053%, respectively. Infinite dilution partition coefficients, Kw3∞, of fundamental benzene derivatives (chlorobenzene, bromobenzene, benzaldehyde and benzyl alcohol) between [amim]Cl and supercritical carbon dioxide were measured at 313–353 K and 6–21 MPa. The ePC-SAFT applied as a predictive model for the experimental partition coefficient gave high deviations (>900%). However, when the ePC-SAFT was applied as a correlative model, average deviation in Kw3∞ were 20%. A previously proposed semi-empirical LSER-δ model could correlate the Kw3∞ data to within 8.9%. Separation factors of solutes in [amim]Cl–CO2 system were calculated with ePC-SAFT model and compared with literature results for [bmim]Cl–CO2 since both of these ionic liquids have application to biomass processing. For each given ionic liquid, [amim]Cl and [bmim]Cl, the separation factors of non-polar or slightly polar compounds (chlorobenzene, bromobenzene and benzaldehyde) to the reference polar compound (benzyl alcohol) were always greater than 100, with [amim]Cl–CO2 always having a higher separation factor than [bmim]Cl–CO2. Thus, [amim]Cl–CO2 can probably provide better separation between non-polar and polar mixtures than [bmim]Cl–CO2.
AB - In this work, densities and viscosities at atmospheric pressure and densities at high pressures of the ionic liquid, [amim]Cl (1-allyl-3-methylimidazolium chloride) were measured. The densities were evaluated by correlation with the Tait equation and the ePC-SAFT equation of state. Both relationships could describe the experimental density data over the full range of all temperatures (313–373 K) and pressures (0.1–200 MPa) within 0.007% and 0.053%, respectively. Infinite dilution partition coefficients, Kw3∞, of fundamental benzene derivatives (chlorobenzene, bromobenzene, benzaldehyde and benzyl alcohol) between [amim]Cl and supercritical carbon dioxide were measured at 313–353 K and 6–21 MPa. The ePC-SAFT applied as a predictive model for the experimental partition coefficient gave high deviations (>900%). However, when the ePC-SAFT was applied as a correlative model, average deviation in Kw3∞ were 20%. A previously proposed semi-empirical LSER-δ model could correlate the Kw3∞ data to within 8.9%. Separation factors of solutes in [amim]Cl–CO2 system were calculated with ePC-SAFT model and compared with literature results for [bmim]Cl–CO2 since both of these ionic liquids have application to biomass processing. For each given ionic liquid, [amim]Cl and [bmim]Cl, the separation factors of non-polar or slightly polar compounds (chlorobenzene, bromobenzene and benzaldehyde) to the reference polar compound (benzyl alcohol) were always greater than 100, with [amim]Cl–CO2 always having a higher separation factor than [bmim]Cl–CO2. Thus, [amim]Cl–CO2 can probably provide better separation between non-polar and polar mixtures than [bmim]Cl–CO2.
KW - Allyl-ionic liquid
KW - Equation of state
KW - High pressure density
KW - Partition coefficient
KW - Separation factor
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U2 - 10.1016/j.seppur.2015.03.008
DO - 10.1016/j.seppur.2015.03.008
M3 - Article
AN - SCOPUS:84979752035
SN - 1383-5866
VL - 155
SP - 139
EP - 148
JO - Gas Separation and Purification
JF - Gas Separation and Purification
ER -