Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid

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Abstract

The activity coefficient at infinite dilution, γ13, was determined by gas–liquid chromatography at temperatures from T = 308.15 to T = 348.15 K for 54 assorted solutes—among them, alkanes (linear, branched, or cyclic), alkenes, alkynes, aromatic hydrocarbons, alcohols, water, thiophene, tetrahydrofuran, 1,4-dioxane, ethers, acetone, ketones, acetonitrile, pyridine, and 1-nitropropane—in the novel bicyclic guanidine superbase-derived protic ionic liquid 1,3,4,6,7,8-hexahydro-1-methyl-2H-pyrimido[1,2-a]pyrimidine bis(pentafluoroethyl)sulfonylimide, [MTBDH][BETI]. The partial molar excess Gibbs free energy ΔG1E,, the partial molar excess enthalpy ΔH1E,, and entropy at reference temperature TrefΔS1E, at infinite dilution were calculated from the experimental γ13 values obtained over this temperature range. The gas–liquid partition coefficient, KL, was calculated for each solute and discussed in light of the Abraham solvation parameter model. The density of the IL as a function of temperature was also measured. The selectivities for heptane/benzene, heptane/thiophene, heptane/pyridine, and heptane/nitropropane separation problems were calculated from γ13 and compared to literature values for select ILs, as these separation problems are central to the petroleum industry.

Highlights

► Measurements of activity coefficients at infinite dilution using GLC. ► 54 Organic solvents and water in the ionic liquid [MTBDH][BETI]. ► High selectivity for heptane/pyridine separation. ► The excess thermodynamic functions, the gas–liquid partition coefficients were calculated. ► The Abraham solvation parameter model was presented.

Introduction

Ionic liquids (ILs) are attracting momentous attention as innovative alternatives to conventional organic solvents as N-methyl-2-pyrrolidinone (NMP) or sulfolane for countless solvent extraction and separation processes [1], [2], [3], [4]. Not limited to academic interest, the industrial importance of ILs is amply shown by the number of newly-emerged technologies currently entering or already on the market [5]. The prevalence of ILs stems from their unique and tailored properties, such as strong solvation and (in general) non-flammability and negligible volatility [1]. The sensible design of IL-based extraction processes requires a knowledge of the activity coefficients at infinite dilution, γ13, making possible the calculation of entrainer selectivity, S12, and capacity, k2 [6]. The rational selection of ILs for practical purposes in aliphatic/aromatic hydrocarbon separations was recently discussed in a fascinating review on the subject [7]. To aid technologists and engineers in selecting the appropriate IL for solving a range of separation problems, we propose that measurement of γ13 for a great many solutes in numerous and diverse ILs is a necessary step, particularly as studies of these materials shift from understanding the parameters that govern their fundamental properties to pursuing useful applications. The solute–solvent interactions in solution are controlled by γ13 and, thus, deeper knowledge of γ13 will make ILs more widely applicable. Furthermore, the range of extraction-robust cations and anions has been extended in recent years, allowing for the preparation of next-generation ILs with enhanced utility. In this regard, perfluorinated anions such as trifluorotris(perfluoroethyl)phosphate (FAP) [2], [8], [9], [10], [11] or nitrile-functionalized 1-alkylpyridinium and N-alkyl-N-methylpiperidinium cations [12], as prominent examples, have generated new opportunities in advanced extractions. Sustained effort on the part of synthetic chemists among the community of IL researchers is required to prepare additional and functional cations and anions, pushing the experimental space that can be explored in the generation of reliable data to advance this new separation technology.

Recently, a family of ILs based on N-alkylisoquinolinium or N-alkylquinolinium cations was fully described by our laboratory [13], [14], [15], [16], [17]. It was found, for example, that N-octylisoquinolinium bis(trifluoromethylsulfonyl)imide, [OiQuin][NTf2], was an excellent entrainer for the extraction of 2-phenylethanol from aqueous bio-media [17]. These sorts of studies remain limited, however. For instance, there exists in the literature but a single study of γ13 for different organic solutes in an IL based on the bis(pentafluoroethyl)sulfonylimide anion [BETI], in this case paired to the 1-butyl-3-methylimidazolium cation, [BMIM]+ [11]. In this particular study, it was revealed that [BMIM][BETI] exhibits both high selectivity (33.3) and capacity (2.51) in the heptane/pyridine separation process [11]. The prospect for tailoring the properties of the IL to meet the requirements of a specific application is particularly attractive. Recent results have suggested that double aromatic rings such as that found in benzimidazolium deserve further contemplation in separations. We feel that, likewise, bicylic cations warrant additional scrutiny.

Here, we report the activity coefficients at infinite dilution, γ13, for 54 solutes, including saturated and unsaturated alkanes, cycloalkanes, aromatic hydrocarbons, alcohols, water, thiophene, tetrahydrofuran, ethers, acetone, ketones, pyridine, and 1-nitropropane in the novel bicyclic guanidine superbase-derived protic IL 1,3,4,6,7,8-hexahydro-1-methyl-2H-pyrimido[1,2-a]pyrimidine bis(pentafluoroethyl)sulfonylimide, [MTBDH][BETI]. Values of γ13 were determined by gas–liquid chromatography at 10 K intervals from T = 308.15 K to T = 348.15 K. This work also provides a unique opportunity to make direct comparisons with previous results with [BMIM][BETI]. By way of additional characterization, we also determined the density of [MTBDH][BETI] as a function of temperature.

Section snippets

Materials

Synthesis, purification, and drying of the IL [MTBDH][BETI] to a purity of >0.995 mass fraction were carried out using literature procedures described extensively elsewhere [18]. Following its preparation, the sample was dried for several days at T = 350 K under reduced pressure to remove volatile impurities and trace water. The final water content was below 0.00037 mass fraction (370 · 10−6) as determined by Karl–Fisher titration. The different solutes, purchased from Aldrich or Fluka, had purities

Theoretical basis

The equations developed by Everett [21] and Cruickshank et al. [22] were used for the calculation of γ13 for solutes in [MTBDH][BETI] according to:lnγ13=lnn3RTVNP1-P1(B11-V1)RT+PoJ23(2B12-V1)RT,where n3 is the number of moles of solvent on the column packing, R is the gas constant, T is the column temperature, VN denotes the net retention volume of the solute, P1 is the saturated vapour pressure of the solute at temperature T, B11 is the second virial coefficient of pure solute, V1 is

Results and discussion

The average values of γ13 for different solutes in [MTBDH][BETI] over the temperature range from T = 308.15 to T = 348.15 K, obtained from two distinctly prepared columns, are presented in table 1. Critical data and virial coefficients of most of these solutes, needed for the calculation of γ13, can be found in the Supplementary data from our previous paper [19]. The typical influence of solute alkane chain length is observed. That is, values of γ13 tend to increase with a lengthening of the

Conclusions

Activity coefficients at infinite dilution for 54 assorted solutes in the superbase-derived IL [MTBDH][BETI] were measured by gas–liquid chromatography for temperatures ranging from T = 308.15 K to T = 348.15 K and compared to recently-published data for an IL bearing the same anion (i.e., [BMIM][BETI]) as well as related fluorous anions like [NTf2] and [FAP]. The selectivities at infinite dilution for the [MTBDH][BETI] system were not found to be particularly attractive for selected petroleum

Acknowledgments

This work has been supported by the National Science Center project 2011/01/B/ST5/00800. M. Królikowski wishes to thank the START Program of the Foundation for Polish Science.

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