TY - JOUR A1 - Kumelan, J. A1 - Tuma, Dirk A1 - Maurer, G. ED - Renon, H. T1 - Simultaneous solubility of carbon dioxide and hydrogen in the ionic liquid [hmim][Tf2N]: experimental results and correlation N2 - The solubility of a single gas as well as the simultaneous solubility of several gases in an ionic liquid is of great interest in many areas of chemical engineering, particularly in heterogeneous catalysis. One of the most interesting features involved in the study of the simultaneous solubility of several gases in a pure ionic liquid is the difference between experimental data and predictions for the simultaneous solubility (based on experimental data for the solubility of the single gases). The well soluble gas might act as a cosolvent or as an antisolvent for a sparsely soluble second gas. New experimental results and a correlation are presented for the simultaneous solubility of hydrogen (i.e., a sparsely soluble gas) and carbon dioxide (a well soluble gas) in the ionic liquid 1-hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)amide ([hmim][Tf2N]) at temperatures between 293 K and 373 K and pressures up to about 9.2 MPa. The experimental results reveal that carbon dioxide acts as a cosolvent for hydrogen in that particular ionic liquid. A correlation shows that the cosolvency effect can be modeled by considering interaction parameters between hydrogen and carbon dioxide in liquid [hmim][Tf2N]. The correlation can also be used to quantify that cosolvency effect: one mole of carbon dioxide in 1000 g of [hmim][Tf2N] increases the solubility of (small amounts of) hydrogen by about 20%. KW - Simultaneous solubility of gases KW - Carbon dioxide KW - Hydrogen KW - Ionic liquids KW - [hmim][Tf2N] KW - 1-Hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)amide PY - 2011 U6 - https://doi.org/10.1016/j.fluid.2011.08.013 SN - 0378-3812 VL - 311 SP - 9 EP - 16 PB - Elsevier B.V. CY - Amsterdam AN - OPUS4-24559 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Chobanov, K. A1 - Tuma, Dirk A1 - Maurer, G. ED - Renon, H. T1 - High-pressure phase behavior of ternary systems (carbon dioxide + alkanol + hydrophobic ionic liquid) N2 - Some homogeneous liquid mixtures of an ionic liquid and a lower alkanol (e.g., methanol) can be forced to undergo a liquid–liquid phase split (resulting in a three-phase liquid–liquid–vapor (L1L2V) equilibrium) by pressurization with a gas. Such systems exhibit the phenomenon of "salting out by a nearcritical gas". That phenomenon is often observed at temperatures around the critical temperature of the gas in liquid mixtures where at least one of the liquid components is a good solvent for that gas. New experimental results for both the L1L2V equilibrium and the corresponding critical endpoint lines of the two ternary systems (carbon dioxide + methanol + 1-n-butyl-3-methylimidazolium hexafluorophosphate [bmim][PF6]) and (carbon dioxide + 1-butanol + 1-n-hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)amide [hmim][Tf2N]) at temperatures between 293 and 333 K are reported. The experiments were performed with an "analytical method". The liquid–liquid phase split exists only at pressures between a lower critical endpoint line (where both liquid phases become critical and coexist with a vapor phase) and an upper critical endpoint line (where one of the phases becomes critical with the vapor phase while the critical phases coexist with another liquid phase). The compositions of the coexisting three phases L1, L2, and V differ considerably; a high-density, ionic liquid-rich liquid phase (L1) coexists with an alkanol-rich liquid phase (L2) of lower density and a vapor phase (V) that is virtually ionic liquid-free. For both systems, it was observed that, at constant temperature, increasing pressure shifts the L1 phase towards higher contents of ionic liquid and gas and less alkanol, whereas in the L2 phase the mole fractions of ionic liquid and alkanol decrease. Higher temperatures result in a smaller difference between the pressures of both critical endpoint lines. Experimental results for both critical endpoint lines and for the compositions of the coexisting liquid phases are reported. KW - Room-temperature ionic lilquids KW - [bmim][PF6] and [hmim][Tf2N] KW - Alkanol KW - Carbon dioxide KW - High-pressure phase equilibria KW - Salting-out behavior KW - Critical endpoints PY - 2010 U6 - https://doi.org/10.1016/j.fluid.2010.02.015 SN - 0378-3812 VL - 294 IS - 1-2 SP - 54 EP - 66 PB - Elsevier CY - Amsterdam AN - OPUS4-22060 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Lim, B.-H. A1 - Choe, W.-H. A1 - Shim, J.-J. A1 - Ra, C. S. A1 - Tuma, Dirk A1 - Lee, H. A1 - Lee, C. S. T1 - High-pressure solubility of carbon dioxide in imidazolium-based ionic liquids with anions [PF6] and [BF4] N2 - The solubility of carbon dioxide in three ionic liquids (ILs) under supercritical fluid condition was measured at pressures up to 32 MPa and at temperatures of 313.15, 323.15, and 333.15 K in a high-pressure view cell. The imidazolium-derivative ionic liquids 1-butyl-3-methylimidazolium hexafluorophosphate ([bmim][PF6]), 1-butyl-3-methylimidazolium tetrafluoroborate ([bmim][BF4]), and 1-octyl-3-methylimidazolium tetrafluoroborate ([omim][BF4]) were employed in this research. The effects of pressure, temperature, nature of anion and cation as well as the water content on the solubility of CO2 in the ILs were investigated experimentally. The solubility of CO2 in the IL was higher for the ILs with longer cationic alkyl group and for the ILs with lower anion polarity. The lower the water content or the lower the temperature as well as the higher the pressure, the higher was the solubility of CO2. KW - Solubility KW - Carbon dioxide KW - Ionic liquid KW - Water content KW - Anion KW - Cation KW - Ionische Flüssigkeiten KW - Gaslöslichkeiten PY - 2009 SN - 0256-1115 VL - 26 IS - 4 SP - 1130 EP - 1136 PB - Inst. CY - Seoul AN - OPUS4-19579 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Safarov, J. A1 - Abdullayeva, G. A1 - Bashirov, M. A1 - Tuma, Dirk A1 - Bashirov, R. T1 - The ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate revisited: Solubility of carbon dioxide over an extended range of temperature and pressure N2 - Solubility data of carbon dioxide (CO2) in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate [EMIM][CH3SO3] at T= (273.15 to 413.15) K and pressures up to p= 5.0 MPa are reported. The solubility measurements were carried out using an isochoric method which operates in decrements of ΔT = 20 K within the investigated temperature range and at selected four different pressure steps ranging froma pressure p of around 5.0 MPa down to around 0.4 MPa. The solubility of CO2 in the ionic liquid monotonously decreases with increasing temperatures at a constant pressure. Within the p,T-range investigated, CO2 displayed a solubility in [EMIM] [CH3SO3] from a mole fraction x= 0.0160 mol·mol−1 and a corresponding molality m = 0.0791 mol·kg−1 at T = 413.15 K and p =0.432 MPa up to x = 0.4049 mol·mol−1 and m = 3.2982 mol·kg−1 at T = 293.15 K and p = 4.577 MPa. Henry's law constant was calculated from the solubility data reported here, and literature data were reviewed for comparison. Additionally, thermodynamic state properties that can be derived from Henry's law constant, such as the Gibbs energy of solvation ΔsolG, the enthalpy of solvation ΔsolH, the entropy of solvation ΔsolS, and the heat capacity of solvation ΔsolCp, were calculated. KW - Hydrophilic ionic liquid KW - Carbon dioxide KW - High-pressure solubility PY - 2021 U6 - https://doi.org/10.1016/j.molliq.2021.115920 SN - 0167-7322 VL - 333 SP - 115920 PB - Elsevier B. V. CY - Amsterdam AN - OPUS4-52436 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER -