Phase diagrams of ionic liquids-based aqueous biphasic systems as a platform for extraction processes
Introduction
Aqueous biphasic systems (ABS) are usually formed as a result of the mutual incompatibility in aqueous solution of two polymers, one polymer and one salt, or two salts above a certain concentration [1]. These systems are mainly composed by water and thereby capable to provide an excellent environment for a large set of cells and biologically active substances. In this way, ABS are commonly investigated for the extraction and purification of distinct (bio)molecules, such as proteins [2], [3], [4], [5], [6] and amino-acids [7], [8], [9], [10], [11], [12]. They allow a high effectiveness, high yield, improved purity degree, a proper selectivity, technological simplicity and low cost [13]. Furthermore, ABS are considered as environmentally friendly techniques, since volatile organic solvents are not employed in the whole process [14]. The application of polymer-based ABS is well-documented [15], [16], [17], [18], nevertheless, most of these aqueous systems present high viscosities, form opaque systems and are considered as limited techniques in terms of the range of polarities of the coexisting phases [19]. There has been, therefore, an effort to find new liquid–liquid alternatives, mainly in the application of distinct and non-polymeric ABS.
In the last decade, the use of ionic liquids (ILs) as a new agent in the formation of ABS has attracted a considerable interest as promising “greener” alternatives to volatile and hazardous organic solvents. This increasing attention is largely justified by their unique properties, such as their negligible vapor pressure, high chemical and thermal stability, their non-flammability, high ionic conductivity, wide electrochemical potential window and high solvation ability. In fact, these ionic compounds are normally known by their tunable properties, which mean that they can be designed for a specific purpose by the selection of the adequate cation/anion combination. Moreover, and allied with their tunable character, the use of ILs in the formation of ABS allows the possibility of tailoring their polarities and affinities by the organization of the ions in the bulk [20].
The use of ILs in the formation of ABS grew steadily [21], [22] since in 2003 Rogers and co-workers [23] reported, for the first time, that hydrophilic ILs had the capacity to form ABS in the presence of some inorganic salts. Different lines of research were considered when studying the use of ILs as ABS promoting agents [21], [22] namely, the study of the salt type, where phosphate [8], [9], [10], [23], [24], [25], [26], [27], [28], [29], [30], [31], [32], [33], hydrogenophosphate [8], [25], [26], [28], [34], [35], sulfate [25], [27], [30], [36] and carbonate [8], [25], [27], [32], [37], [38] and a range of other salts [21], [39] were applied, as well as carbohydrates [7], [40], polymers [41], [42], amino-acids [43], [44], and more recently anionic surfactants [45]. Furthermore, recent studies have introduced citrate-based salts in the formulation of IL-based ABS because they are more biodegradable and less toxic than most other salts [46], [47], [48]. Nevertheless, on most of these liquid–liquid extraction systems, the pH is not adequately controlled, which is a crucial issue regarding the separation or purification of some particular biomolecules, namely proteins [49] and enzymes [50]. Only recently, the inorganic potassium phosphate buffer (K2HPO4/KH2PO4) and the organic potassium citrate buffer (C6H5K3O7/C6H8O7) solutions (both at pH 7), have been focus of interest among researchers considering not only their ability to form ABS when conjugated with ILs, but also their applicability while extraction and purification systems for several biomolecules [2], [6], [34], [49], [50], [51], [52], [53], [54].
Another aspect of major importance when considering the IL-based ABS formation is the study of the impact of the different ILs, not only in what concerns the use of several cations families [21], the imidazolium being one of the most investigated [41], [55], but also considering the effect of the cation alkyl side chain length [8], [10], [56] and finally, different anions [24], [51]. More recently, and since the number of new IL families is increasing, some works concerning the use of new families, such as the acyclic phosphonium, quaternary ammonium and, more recently, the cholinium-based ILs, were reported [9], [57], [58], [59].
Taking into account the significant extraction efficiencies achieved recently for paracetamol [53] and natural dyes [49] in presence of ammonium compounds, a study on the expansion of the range of ionic liquid-based aqueous biphasic systems (IL-ABS) as a platform for extraction processes is here reported. For that purpose imidazolium-, pyridinium-, phosphonium-, ammonium- and cholinium-based ILs were evaluate toward their ability to form ABS in presence of potassium phosphate buffer (KH2PO4/K2HPO4), potassium citrate buffer (C6H5K3O7/C6H8O7) and potassium carbonate (K2CO3) solutions.
This work is divided into four main sections: (i) the first addresses the pH influence; (ii) the second reports the impact of different cation cores, (iii) the third describes the influence of the cation side alkyl chain length and anion effect, and the (iv) addresses the salt effect. In this context, it was chosen to evaluate one inorganic salt (K2CO3 at pH ∼13) and two buffers with different ionic strength: the organic and benign potassium citrate buffer (C6H5K3O7/C6H8O7 at pH 5, 6, 7 and 8) and the inorganic potassium phosphate buffer (KH2PO4/K2HPO4 at pH 7).
Section snippets
Materials
In this work, thirteen distinct ILs were investigated in terms of their capacity for ABS formation in conjugation with three salts. Their full name, acronym and purities are presented in table 1, being their respective ionic structures depicted in figure 1.
Phosphonium- and cholinium ILs were purchased from Cytec and Fluka, respectively and the ammonium-based ILs were acquired at Sigma–Aldrich. The [C4mim]Cl and [C4mpy]Cl were from Iolitec (Ionic Liquid Technologies, Heilbronn, Germany). The
Results and discussion
The present study addresses the capacity of different ammonium-, phosphonium-, cholinium-, imidazolinum- and pyridinium-based ILs for ABS formation with distinct salts, namely K2CO3, K2HPO4/KH2PO4 and C6H5K3O7/C6H8O7. All phase diagrams were determined at T = (298 ± 1) K and atmospheric pressure. The experimental weight fraction data for all the studied systems are provided in the Supporting information, tables S2 to S41. The solubility curve for the system [C4mim]Cl + C6H5K3O7/C6H8O7 at pH 7 + H2O
Conclusions
In this work novel ABS were determined as a platform for distinct extraction processes. Taking into account the phase diagram behavior, the effect of pH, IL cation core, alkyl side chain length, IL anion nature, and distinct salts in what concerns their capacity induce ABS formation was presented and discussed. In general, the ability to form ABS increases with the pH and alkyl chain length for all systems studied. Moreover, the influence of the cation core and anion nature of the ILs on their
Acknowledgments
The authors are grateful for financial support from FEDER funds through the program COMPETE and by national fund through the Portuguese Foundation for Science and Technology (FCT) under the scope of the projects Pest-C/CTM/LA0011/2013 and PTDC/AAC-AMB/119172/2010. The authors also acknowledge FCT for the post-doctoral and doctoral Grants SFRH/BPD/79263/2011 and SFRH/BD/85871/2012 of S.P.M. Ventura and T.E. Sintra, respectively.
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