Ionic liquids (ILs) are low-melting organic salts,which are composed of unsymmetrical organic cation and inorganic anion [1],and have negligible vapour pressure,wide liquid range,high thermal,and chemical stabilities which make them potentially “green” replacements for conventional volatile and toxic organic solvents. Due to their unique physical and chemical properties [2],ILs are emerging as alternative green solvents,in other words,as alternative reaction media for synthesis [3],dispersants [4],and catalysis [5],but also as lubricants [6],or modifiers of mobile [7] and stationary phases in separation sciences [8]. As one of the environmentally benign “green” solvents,[BMIM]BF4 has been used in many scientific fields and their applications continue to expand [9]. For exploration and design of the applications of [BMIM]BF4,the physical and physico-chemical properties of this ionic liquid are needed. The interactions between ILs and solvents are often quantified by the Flory-Huggins interaction parameters and the weight fraction activity coefficients,thus assisting in the selection of proper solvents for every application [10]. The activity coefficient at infinite dilution is also important,because it describes the extreme case in which only solute-solvent interactions contribute to nonideality [11]. The solubility parameter,which is a concept that has been used to estimate various physicochemical parameters [12, 13],was used to understand the intermolecular interactions responsible for solvation in the studied ILs.
Many considerable and interesting research studies have been performed to study the density,viscosity,electrochemical stability and activity coefficients at infinite dilution of [BMIM]BF4. Kim et al. [14] measured the density,viscosity,refractive index,ionic conductivity,and electrochemical stability of [BMIM]BF4 at room temperature,found that electrochemical windows in the stability was 4.7 V of [BMIM]BF4. Revelli et al [15] determined the activity coefficients at infinite dilution of [BMIM]BF4 from 303.35 K to 332.55 K,found that interfacial adsorption contribution of polar solutes in [BMIM]BF4 was lower than that in imidazolium-based ionic liquids with a bromide anion. However,to the best of our knowledge,the properties including Flory-Huggins interaction parameter,weight fraction activity coefficient,and solubility parameter of [BMIM]BF4 have not been comprehensively reported. To obtain these parameters of ILs,several different methods [16] can be used,such as the mechanical measurements,swelling measurements,group contribution methods,viscosity measurements and IGC [17]. Among these methods,IGC has been demonstrated to be an effective tool for measuring the thermodynamic properties of ILs [18, 19, 20, 21, 22] over a wide temperature range.
This work aims to determine the solubility parameter of [BMIM]BF4 via IGC. Meanwhile,the molar heat of sorption,weight fraction activity coefficient and Flory-Huggins interaction parameter were determined,which provided considerable quantitative information for further research.
The specific retention volume Vg0,which is used to describe the elution behavior of probes,can be calculated using the following equation [23]:
The specific retention volume Vg0 can be used for the calculation of thermodynamic properties. The weight fraction activity coefficient,Ω 1∞,and the molar heat (enthalpy) of sorption,Δ H1S,of the probe absorbed by [BMIM]BF4 are given by the following equations [24, 25]:
From the obtained weight fraction activity coefficient values,the molar enthalpy of mixing Δ Hl∞,and values of heats of vaporization Δ Hv,can be calculated according to the following thermodynamic relations [26, 27]:
Using Flory-Huggins theory,the interactions between [BMIM]BF4 and the probes may be expressed by means of Flory-Huggins parameter,χ 12∞,which is calculated by the equations [28, 29]:
The solubility parameter of each probe,δ 1,or the square root of cohesive energy density (CED) for the volatile solute is related to enthalpy of vaporization,Δ Ev,and the molar volume as follows [17]:
The solubility parameter of [BMIM]BF4,δ 2,can be calculated by using the following equation [30, 31]:
By plotting the left hand side of this equation versus δ 1,a straight line having a slope of 2 δ 2/RT and an intercept of (- δ 22/RT) is obtained. The solubility parameter of [BMIM]BF4 can be determined from the slope or the intercept of the straight line. This relation has been widely used in IGC to estimate the solubility parameters of the stationary [32].
The ionic liquid [BMIM]BF4 investigated in this work was obtained from Chengjie Chemical Co.,Ltd. (China)with a quoted purity of greater than 0.99 mass fraction. A homologous series of n-alkanes from n-C10 to n-C12 were used as non-polar probes. Dichloromethane,acetone,chloroform,ethyl acetate,carbon tetrachloride,methyl acetate,cyclohexane,toluene,ethanol and methanol were used as polar probes. All chemicals used in this work were of analytical purity and without further purification.
The stationary phase used in this work was prepared by dissolving a weighed sample of the [BMIM]BF4 in dichloromethane and depositing the solution on a weighed amount of silicon alkylation 102 monomer support (60-80 mesh). The mixture was allowed to dry under rotary evaporator by slow evaporation,being stirred to ensure a homogeneous mixture. The stationary phase consisted of 20% (mass percentage) of the [BMIM]BF4. The coated support was packed into a stainless steel column with 0.2 cm inner diameter and 120 cm length. Before experiment,the column was conditioned by blowing nitrogen at 393 K for 8 h.
The IGC measurements were performed on a commercial Shimadzu QP 2010 gas chromatograph,equipped with a thermal conductivity detector. The GC solution (2.30.00) was used to trace detector signals in the analysis. The injector and detector temperatures were kept at 503 K and 533 K,respectively. Dried nitrogen was used as carrier gas with a flow-rate of about 20 mL/min throughout the experiment. The flow rate of nitrogen was measured with a soap bubble flowmeter at room temperature. The temperature of the oven ranged from 333 K to 373 K varied in 10 K increments. In this experiment,air was used to act as the non-interacting void volume maker to determine the column hold-up time of other probe solvents. The mass of the stationary phase,retention time,dead time,column temperature,flow rate,and input and output pressures,all have experimental errors. Based on the error propagation law,the δ 2 was estimated to have a relative uncertainty within ±5%.
The Vg0 data are essential in the determination of physicochemical or thermodynamic properties of a material by IGC [33, 34]. The V0g values of the solvents on the [BMIM]BF4 obtained from the IGC measurements from 333 K to 373 K with 10 K intervals were determined using equation (1). Figs. 1 and 2 give examples of plotting ln Vg0 versus 1/T for the [BMIM]BF4. It can be seen that the values of ln Vg0 varied with the reciprocal temperatures. ln Vg0 decreased with increasing temperatures.
The Δ H1S value was obtained from the slope of ln Vg0 versus 1/T using equation (3). Δ Hl∞ was obtained from the slope of ln Ω 1∞ versus 1/T using equation (4). Table 1 shows experimentally obtained Δ HlS,Δ Hl∞ and Δ Hv in the temperature range of 333-373 K. The sorption process was dependent on the chemical natures of IL and the interactions between [BMIM]BF4 and the probes. From the data in Table 1,it can be seen that the molar heats of sorption of the probes increased as the numbers of CH2 groups in probe molecule increased,indicating that longer CH2 chains in the probe molecule resulted in stronger interaction between the probe and [BMIM]BF4. As more CH2 groups are added to probes,the heat of sorption becomes more exothermic,because the chemical nature and the number of carbons of each probe are different from each other. The polar probes have higher molar heats of sorption than the nonpolar probes,because the nonpolar probes exhibited dispersive forces during interaction with the n-alkane groups of [BMIM]BF4,whereas the polar probes have dipole-dipole forces and dispersive forces during interaction with the polar groups of [BMIM]BF4.
The value of the weight fraction activity coefficient at infinite dilution is especially important. It has been proposed that Ω 1∞ values can be used to evaluate the compatibility [35]. The following rule has been formulated: Ω 1∞<5,good solvents; 5< Ω 1∞<10,the probe is characterized as “moderate solvents”; Ω 1∞>10,poor solvents. The Ω 1∞ value was calculated based on equation (2) and listed in Table 2. As shown in Table 2,n-C10 to n-C12,carbon tetrachloride,cyclohexane and toluene are poor solvents for [BMIM]BF4,while dichloromethane and chloroform are good solvents for [BMIM]BF4.
The Flory-Huggins parameter χ 12∞ is a measurement of the compatibility of a material-solvent pair. The lower the values of χ 12∞ are,the higher the compatibility will be [36]. The values of χ 12∞ confirmed the evaluations on the values of Ω 1∞. Theoretically,χ 12∞ values smaller than 0.5 indicates IL-solvent systems; χ 12∞ values larger than 1 indicates an IL-non-solvent system; and 0.5< χ 12∞<1 values indicates that the solvent is moderate [37]. The χ 12∞ values between [BMIM]BF4 and the solvents were calculated based on equation (6) at four temperatures,and listed in Tables 3. As shown in Table 3,that parameter again indicated that dichloromethane,acetone,chloroform,methyl acetate,ethanol and methanol were good solvents for [BMIM]BF4.
The Flory-Huggins parameter has two contributions: entropic and enthalpic [38]. The entropic contribution is related to the free volume of the solvent,which increased with increasing temperature. The enthalpic contribution is related to the intermolecular forces between the materials and the solvents,which decreased with increasing temperature. As can be seen from Table 3,the Flory-Huggins parameters of some probes,which include dichloromethane,acetone,chloroform,ethyl acetate,carbon tetrachloride,methyl acetate,toluene and benzene,increased with increasing temperature. It means that the entropic contribution is greater than the enthalpic contribution. The Flory-Huggins parameters of the others decreased with increasing temperature,which means the entropic contribution is greater than the enthalpic contribution,such as n-C10 to n-C12,cyclohexane.
Knowledge on solubility parameters of the IL used in the aforementioned technological applications is of vital importance and has been found to be a useful guide in the selection of solvents for Ils [39]. The solubility parameter,δ 2,for [BMIM]BF4 was evaluated from equation (8),which was obtained from slopes or intercepts of the plots of δ 12/RT- χ 12∞/V1 versus δ 1 as shown in Fig. 3. The solubility parameters of [BMIM]BF4 were measured at five temperatures to obtain the temperature dependence. The solubility parameters decreased with increasing temperature,which fitted an empirical relationship from Fig. 4. The values in reported literature were mostly calculated or determined at room temperature. The extrapolated value for δ 2 at 298 K was found to be 23.39 (J/cm3)0.5.
IGC was proven to be a versatile and useful technique for determining the thermodynamic properties of [BMIM]BF4. IGC technique was successfully applied to determine [BMIM]BF4-solvent and [BMIM]BF4-non-solvent interactions. According to the weight fraction activity coefficient and Flory-Huggins interaction parameter of the various solvents with the [BMIM]BF4,the results indicated that dichloromethane,acetone,chloroform,methyl acetate,ethanol and methanol were good solvents for [BMIM]BF4; n-C10 to n-C12,carbon tetrachloride,cyclohexane and toluene were bad solvents for [BMIM]BF4 at experimental temperatures. The solubility parameter of [BMIM]BF4 was determined as 23.39 (J/cm3)0.5 by the extrapolation at 298 K.