Representation of Phase Behavior of Ionic Liquids Using the Equation of State for Square-well Chain Fluids with Variable Range*

LI Jinlong (李進(jìn)龍), HE Qing (何清), HE Changchun (何昌春), PENG Changjun (彭昌軍) and LIU Honglai (劉洪來)

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Representation of Phase Behavior of Ionic Liquids Using the Equation of State for Square-well Chain Fluids with Variable Range*

LI Jinlong (李進(jìn)龍), HE Qing (何清), HE Changchun (何昌春), PENG Changjun (彭昌軍)**and LIU Honglai (劉洪來)

State Key Laboratory of Chemical Engineering and Department of Chemistry, East China University of Science and Technology, Shanghai 200237, China

An equation of state (EOS) for square-well chain fluids with variable range (SWCF-VR) developed based on statistical mechanics for chemical association was employed for the calculations of pressure-volume-temperature () and phase equilibrium of pure ionic liquids (ILs) and their mixtures. The new molecular parameters for 23 ILs were obtained by fitting their experimental density data over a wide temperature and pressure ranges. The molecular parameters of ILs composed of homologous organic cation and an identical anion such as [Cmim][NTf2] are good linear with respect to their molecular weight, indicating that the molecular parameters of homologous substances, subsequentlyand vapor-liquid equilibria vapor-liquid equilibria (VLE) can be predicted using the generalized parameter when no experimental data were available. The new set of parameters were satisfactorily used for calculations of the property of solvent and ILs mixture and the solubility of gas in various ILs at low pressure only using one temperature-independent binary interaction parameter.

equation of state, ionic liquids, square-well chain, phase behavior

1 INTRODUCTION

Ionic liquids (ILs) were typically composed of large organic cations and small organic/inorganic anions, and usually considered as a kind of special organic salt. In the past decade, they have received increasing attention due to their promising practice applications in chemistry and engineering such as reaction, separation, catalyzation,[1, 2]. ILs have a wide variety of unique thermophysical properties which include negligible vapor pressure, nonflammability, good thermal and chemical stability, high ionic conductivity, wide liquid region and so on. In particular, the properties of ILs can be artificially tailored for a practical requirement by the right selection of the cation and anion. Therefore, thousands of ILs can be designed and synthesized for specific applications in different fields. In these growing research and utilization, it is necessary to know the physiochemical properties of ILs and their mixtures such as, heat capacity, phase equilibrium,.

The physicochemical and thermodynamic properties of pure ILs and their mixtures have been extensively studiedexperimental methods [3]. In recent years, many theoretical approaches have also been used for the representation of the thermodynamic characteristics and phase behavior of systems containing ILs. The traditional regular solution theory [4], group contribution methods [5], activity coefficient models [6, 7] and cubic equations of state [8] have successfully been applied to model the properties including Henry’s constants, solubilities, liquid-liquid equilibrium,. Several attempts trying to use the SAFT-based models to compute the different thermodynamic properties have been done by different authors. Kroon. [9] modeled ILs as a mixture of two specific components of cations and anions with dipolar interaction, and the pure component parameters of size, energy, association were estimated by literature data, while the segment number parameter was fitted to the experimental density data. Then, they rescaled the pure ionic liquid parameter by fitting the experimentaldata with a wide temperature range and limiting tPC-PSAFT [10] to calculate the phase behavior of ILs at low pressure [11], whereas Andreu and Vega [12] considered ILs as a Lennard-Jones chains with an associating site. The previous studies in our group have shown that ILs can be considered as a square-well chain-like molecule with an associating site or an associating diblock component as well [13-15]. Actually, many studies have indicated that ILs molecules usually exist as ion pairs or cluster and have large sizes, and then, it is reasonable to treat them as chainlike molecules [11-16]. Recently, Wang and coworkers [17] presented an equation of state (EOS) for ILs based on perturbation theory by taking the dispersive and electrostatic interaction into account. In this work, ILs was simply assumed as a chainlike molecule with square-well interaction potential and the pure molecular parameters were obtained by fitting the experimental density data with a wide rang of temperature and pressure. Then, the density and phase equilibrium properties of mixtures containing ILs were predicted and calculated.

2 Brief review of SWCF-VR EOS

In a previous work [18] an equation of state for square-well chain fluid with variable interaction range has been developed on the basis of statistical mechanics for chemical association. In this model a new dispersive contribution to the Helmholtz function for square-well monomers with variable well width range of 1.1≤≤3.0 was established by using the perturbation theory and integral equation approach. Furthermore, the contribution from chain formation was separated into two parts: one is from the hard sphere and the other from the effect of square-well potential. The EOS can well reproduce the compressibility factor and vapor-liquid coexistence curves of pure model fluids and mixtures. It can also be used for the representations ofand VLE for real substances satisfactorily [19-21].

A-component mixture of square-well chains is considered to be comprised ofNchain molecules of component. Each molecule in a mixture is composed ofrtangent spheres with same diametersσ. According to the previous work [18] the residual Helmholtz function and the compressibility factor of a mixture can be written as

In this EOS each pure non-associating component is characterized by four molecular parameters: segment number per molecule (r), segment diameter (σ), segment-segment interaction energy parameter (ε/) and reduced well width (). These parameters can be obtained by fitting experimental saturated vapor pressure and/or liquid density data of pure fluids [19, 20]. For a mixture the binary energy interaction parameterinεcan be determined from experimental data in order to improve the model accuracy.

3 Results and Discussion

3.1 The molecular parameters and pVT properties of ILs

The EOS is used to correlate the experimental density data with a wide temperature and pressure ranges for pure ILs, and the molecular parameters of segment number (), segment diameter () and dispersion energy (/) are obtained using a simplex method. During the regression, the objective function is based on the minimization of calculated errors of the liquid density

whereNis the experimental point number andis the experimental density data. The superscript “exp” and “cal” denote the experimental and calculated results, respectively. The calculated results and molecular parameters (,3,/) are listed in Table 1 and the overall average deviation of specific volumes and the overall correlation coefficient are 0.07% and 0.9980, respectively. In addition, the range of temperature and pressure, number of data and cited literatures are also given. For all ILs investigated, the optimal reduced well width is fixed as 1.5 as this model can well capture thebehavior of ILs over a wide range of temperature and pressure only using three model parameters.

From Table 1 it is found that the molecular parameters of ILs composed of homologous organic cations and same anions are good linear with respect to their molecular weights (). For instance, the relationships between the numerical values of,3and(/) and molecular weight for the homologous ILs of [Cmim][NTf2] can be fittedlinear functions as follows

Table 1 Molecular parameters and correlated results of pVT data for ILs (λ1.5)

In the molecular level, the homologous ILs of [Cmim][NTf2] can be regarded as a compound composed of two different groups,.., [Cmim]+and [NTf2]－, in which the anion is identical and the molecular mass only linearly increases with increasing number of carbon atom in cations. In addition, the real molecule in this model is assumed to be composed ofhard sphere segment with diametersurrounded by square-well potentials. The segment number () and the molecular size parameter (3) should increase with increasing molecular weight for homologous series. Thus, it is not surprising that the molecular parameters or their combinations for homologous ILs such as [Cmim][NTf2] linearly increase with increasing molecular mass. Using these generalized model parameters, theproperties and phase behavior of homologous compounds, [Cmim][NTf2], can be predicted even no experimental data is available. The molecular parameters for [C7mim][NTf2] by Eqs. (4)-(6) are obtained without using its experimental density data and the corresponding liquid density is predicted as presented in Fig. 1. The agreement with experiments [31] is satisfactory over a wide temperature and pressure ranges, indicating that this model can be successfully used to predict the thermodynamic propertiesfor some ILs. Furthermore, it is found that the energy parameter between segments of all ILs is larger than that of normal molecules [19, 20]. The reason might be attributed to the fact that there are strong electrostatic interaction between cations and anions in ILs.

Figure 1 Comparison of predicted (line) and experimental [31] (symbols) volumes for [C7mim][NTf2]

/K: 1—293.15; 2—313.15; 3—333.15; 4—353.15; 5—393.15

3.2 Properties of IL mixtures

Figure 2 Comparison of predicted (line) and experimental [32] (symbols) density for [C4mim][PF6](1) + [C4mim][BF4] (2) mixture

Figure 3 Comparison of predicted (line) and experimental[33] (symbols) density for [C4mim][BF4](1) + [C4mim][NTf2] (2) mixture

Phase equilibria for ILs mixtures also require that temperature and pressure of vapor-liquid coexistence phases, and chemical potential of corresponding componentin vapor-liquid mixtures are equal. In fact, ILs have extremely low vapor pressure and the solubility of ILs in vapor phase is very small at equilibria and can be ignored. Thus, the equilibrium equation for binary ILs mixtures at a fixed temperature can be written as

wheremis the number of experimental data points. In calculations, the molecular parameters of normal small molecules were directly gained from our previous work [20].

The temperature-independent binary interaction parametersκand calculated results are listed in Table 2. The overall average relative deviation between calculated and experimental equilibrium pressure and the overall correlation coefficient for all systems are 4.96% and 0.9771, respectively. The average relative deviation of the equilibrium pressure for solvent?+?ILs systems is 4.53%. For gas?+?ILs systems at elevated pressure, it is 5.56% with one temperature-independent adjustable binary interaction parameter. It is observed from Table 2 that the differences in the quality of ILs and the experimental methods used by the different researchers could result in a little different value of the adjustable binary interaction parameter and average deviation for the same system, for example, for CO2+?[C4min][PF6] system as shown by Wang[13].

Table 2 The correlated results for solubility of solvents/gases in ILs

Figure 4 Phase equilibria diagram for CO2(1)?+?[C4min][PF6] (2) at different temperatures with comparison of this work (solid line) and soft-SAFT (dash line)

/K: 1—283; 2—298; 3—323; 4—348

Figure 5-diagram for CHF3(1)?+?[C4min][PF6](2) at two different mole fraction of CHF3with comparison of this work (solid line) and tPC-PSAFT (dash line)

molar fraction of CHF3: 1—0.203; 2—0.302; 3—0.4

4 Conclusions

In this work, an equation of state for square-well chainlike fluid with variable range was applied to represent theand phase behavior of pure ILs and their mixtures. Both normal fluids and ILs were modeled as a square-well chainlike molecule with dispersion interactions in the EOS. The experimental density data with a wide range of temperature and pressure can be well captured by the model and the average absolute relative deviation is only 0.07%. The new molecular parameters of ILs comprised of homologous cations and an identical anion show good linear relations with respect to molecular weight. Coupled with one-fluid mixture rule, the properties of ILs mixtures were predicted or correlated with one temperature- independent interaction parameter and, in all cases, the results at low pressure were satisfactory.

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2009-06-22,

2009-10-14.

the National Natural Science Foundation of China (20876041, 20736002), the National Basic Research Program of China (2009CB219902), Program for Changjiang Scholars and Innovative Research Team in University of China (IRT0721) and the 111 Project of China (B08021).

** To whom correspondence should be addressed. E-mail: cjpeng@ecust.edu.cn