According to equations (2,3,4),the molar heat of sorption of the probes into the [HMIM]BF4,Δ H1S,the molar enthalpy of mixing at infinite dilution,Δ Hl∞,and the heat of vaporization,Δ Hv,in the temperature range from 343.15 to 373.15 K can be obtained,and the values are shown in Table 1. The sorption process was dependent on the chemical nature of IL and the interactions between the [HMIM]BF4 and probes. Probes with different chemical natures have different interactions with [HMIM]BF4. Alkanes would reveal their dispersive interactions with [HMIM]BF4,while acetates,halogenated and oxy probes revealed the dipole-dipole and H-bonding interactions,aromatic and cyclic probes revealed the van der Waal’s interactions. The data in Table 1 can reflect which solvent is closer to dissolve [HMIM]BF4 and which solvent shows a stronger interaction with [HMIM]BF4. It can be seen from Table 1 that the partial molar heat of mixing,Δ Hl∞,for n-alkanes,alcohols and halogenated probes have negative values,which reflect exothermic mixing. However,the values are positive for tetrahydrofuran,acetone,acetates,ether,aromatic and cyclic probes that reflect endothermic mixing. According to equation (2),the molar heats of sorption,Δ H1S,of the probes into the [HMIM]BF4 were obtained. As for the n-alkanes,the number of CH2 groups in the n-alkanes series would affect the values of the exothermic molar heat of sorption. When more CH2 groups were added to the probes,the heat of sorption became more exothermic,which led to the stronger interaction between the probes and [HMIM]BF4. In addition,the values of Δ H1S for dichloromethane,chloroform,and carbon tetrachloride increased with the number of Cl atoms in the probe molecules increasing. Specifically,the CH2 groups exhibited dispersive forces during interaction of the CH2 groups of [HMIM]BF4,whereas the polar groups had the dipole-dipole forces during interaction with the polar groups of [HMIM]BF4.
The Flory-Huggins interaction parameter between IL and solvents ( χ 12∞) played a significant role in predicting the thermodynamic state of IL mixed with the solvents,swelled with solid,blended with another liquid,and in many other applications. It can be calculated based on equation (8),and the results are given in Table 2. χ 12∞ has been proposed to indicate the interactions between IL-solute systems. The following rule has been formulated among researchers in thermodynamics: χ 12∞>1,bad solvents; χ 12∞<0.5,good solvents [30]. For all examined solvents,high Flory-Huggins interaction parameter values reflected the poor compatibility/miscibility and were observed for n-C6,n-C7,n-C8,n-C9,diethyl ether,tetrahydrofuran,benzene and cyclohexane,which indicated they are bad solvents for [HMIM]BF4. While low Flory-Huggins interaction parameters reflected good solubility and were observed for toluene,m-xylene,ethanol,methanol,dichloromethane,tetrachloromethane,chloroform,acetone,ethyl acetate and methyl acetate,which indicated they are good solvents.
The activity coefficients at infinite dilution provide great information about the strength of the ionic liquid with organic solvents. The values were calculated based on equation (6),as listed in Table 3. The increase of the temperature resulted in the decrease of γ 12∞ for n-alkanes,ether,alcohols,tetrahydrofuran,benzene,toluene,m-xylene and cyclohexane. However,the opposite trend was observed for some probes,especially for dichloromethane,tetrachloromethane,chloroform,acetone,ethyl acetate and methyl acetate,as shown clearly in Fig. 3 and Fig. 4. Higher values of γ 12∞ were observed for n-C6,n-C7,n-C8,n-C9 benzene,tetrahydrofuran,diethyl ether,and cyclohexane,which indicated weak interactions between the probes and [HMIM]BF4. Smaller values of γ 12∞ were observed for alcohols,acetone,dichloromethane,tetrachloromethane,chloroform,ethyl acetate and methyl acetate,toluene,and m-xylene,which indicated the stronger interaction with [HMIM]BF4. All the results were consistent with the χ 12∞ values.
Knowledge of the solubility parameters of IL is of vital importance for the selection of solvents for ILs. The solubility parameter,δ 2,for [HMIM]BF4 was obtained from the slope of the plot of δ 12/(RT)- χ 12∞/V1 against δ 1 by equation (9) (Fig. 5). The δ 2 for [HMIM]BF4 were measured at four temperatures to obtain the temperature dependence of the solubility parameters and the results are listed in Table 4. The δ 2 linearly increased with the increase of temperature (Fig. 6). The extrapolated value for δ 2 at 298.15K was found to be 23.70 (J\5cm-3)0.5,which was consistent with the 23.3 (J\5cm-3)0.5 value reported by Foco et al. [13].