1 Introduction

The increasing interest in ionic liquids has lead to research activities concerning thermodynamics and thermophysical properties of ionic liquid mixtures. Ionic liquids are comprised of a large organic cation and an inorganic polyatomic anion. In recent years they have also been considered as designer solvents as their physical properties can be tuned by careful selection of the anion or cation. They are widely used in many industrial processes such as organic synthesis, electrochemistry, separation processes, multiphase separation, etc. [14]. The physical and thermodynamic properties of an ionic liquid depend mostly on the nature and size of both their cation and anion constituents [57]. The chemical complexity of the cation and anion involved in the liquid structure also exhibit a challenge for theoreticians to understand thermodynamic properties of ionic liquids mixtures on the basis of molecular interactions. However, in spite of their practical importance, there is a considerable lack of data on thermodynamic properties [810] like V E, H E and \( \kappa_{S}^{\text{E}} \) of ionic liquid mixtures.

We are unaware of any \( V_{12}^{\text{E}} ,\,H_{12}^{\text{E}} \) and \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \) data of our studied mixtures with which the experimental data can be compared.

The topology of a molecule is described by vertices (atoms) and edges (bonds), called the molecular graph of a molecule, which in turn provides the total information contained in a molecule. Topological indices are a powerful tool [1115] for predicting physical and thermodynamic properties, biological activities, pharmacological and toxicological properties of liquids and their mixtures. Such indices are derived from the molecular structure without any experimental input. In recent studies [1620], we have employed Graph theory (which deals with the topology of a molecule) successfully to determine V E, H E, excess Gibbs energy G E, and \( \kappa_{S}^{\text{E}} \) of binary and ternary organic liquid mixtures. It will be of interest to see how Graph theory describes the thermodynamic properties of ionic liquid mixtures. A literature survey has revealed thermodynamic data have not been reported for 1-ethyl-3-methylimidazolium tetrafluoroborate (1) + N-methyl formamide or N,N-dimethyl formamide (2) mixtures. Consequently, we report here new ρ and u data of 1-ethyl-3-methylimidazolium tetrafluoroborate (1) + N-methyl formamide or N,N-dimethyl formamide (2) mixtures at (293.15, 298.15, 303.15 and 308.15) K and H E data of the same mixtures at 298.15 K over entire composition range.

2 Experimental

1-Ethyl-3-methylimidazolium tetrafluoroborate [emim][BF4] (Fluka, 0.98 GC) was used without further purification. The water content in this ionic liquid was regularly checked using Karl Fischer titrations [21] and the content of water was observed to be 350 ppm. N-methylformamide (NMF) (Fluka, >0.98 GC) was shaken with sodium hydroxide pellets and barium oxide for at least 4 h, filtered, and the filtrate was distilled under reduced pressure. The middle fraction was collected and stored in small bottles over anhydrous calcium chloride in a dessicator [22]. N,N-dimethylformamide (DMF) (Fluka, >0.98 GC) was distilled with benzene at atmospheric pressure and the water–benzene azeotrope was collected (which distills between 70 and 75 °C); the residual solution was shaken with powdered barium oxide, filtered and distilled under nitrogen at reduced pressure [23]. The purities of the purified liquids were checked by measuring their density and speed of sound values. The ρ and u values for the purified liquids (recorded in Table 1) compare well with their corresponding literature values [22, 2432].

Table 1 Comparison of densities, ρ, speeds of sound, u, and heat capacities, C p , of pure liquids with their literature values at T = (293.15, 298.15, 303.15, 308.15) K

The ρ and u values of the pure liquids and their binary mixtures were measured at the desired temperatures using a density and sound analyzer (Anton Paar DSA 5000) in the manner described elsewhere [33, 34]. The apparatus was calibrated with double distilled, deionized and degassed water. The mole fraction of each mixture was determined from the measured apparent masses of the components. All of the measurements were performed on an electronic balance. The uncertainties in mole fraction are 1 × 10−4. The uncertainties in the density and speed of sound measurements are 2 × 10−3 kg·m−3 and 0.1 m·s−1 respectively. The uncertainty in V E values predicted from density results is 0.1 %. Also, the uncertainty in the temperature measurement is ±0.01 K.

Values of H E for the studied mixtures were measured with a 2-drop calorimeter (model, 4600) supplied by the Calorimeter Sciences Corporation (CSC), USA, at 298.15 K. The 2-drop calorimeter consists of a reaction vessel, a rapidly responding thermoelectric device (TED) as the heat measuring sensor, an electric heater for calibration, and a burette system for titrant addition. The heat flow between the reaction vessel and the constant temperature block was detected by the TED sensor, amplified, and then converted from an analogue signal to a digital signal in the data collection system. The temperature of the constant temperature block was actively controlled using the block control TEDs. The amounts of liquids in the micro syringe and vial (in CSA 2-Drop Calorimeter) for enthalpy measurements were determined by weight and the uncertainty in mole fraction in enthalpy measurement is 1 × 10−4. The H E values of the present mixtures were measured in the manner described elsewhere [35]. The uncertainties in the measured H E values are 1 %.

The equimolar liquid mixtures were prepared by mixing (1) and (2) components in a 1:1 (mol/mol) ratio. Spectra of the samples were recorded by a Perkin Elmer Spectrum RX-1, FTIR spectrometer.

3 Results

The experimental values of ρ 12 and u 12 of [emim][BF4] with NMF or DMF at (293.15, 298.15, 303.15 and 308.15) K, and \( H_{12}^{\text{E}} \) at 298.15 K, over the entire range of composition at atmospheric pressure are presented, respectively, in Tables 2 and 3. The \( V_{12}^{\text{E}} \) and \( \left( {\kappa_{S}^{{}} } \right)_{12} \)values for the studied mixtures were determined from density and speed of sound values using:

$$ V_{12}^{\text{E}} = \sum\limits_{i = 1}^{2} {x_{i} M_{i} (\rho_{12} )^{ - 1} - } \sum\limits_{i = 1}^{2} {x_{i} M_{i} (\rho_{i} )^{ - 1} } $$
(1)
$$ \left( {\kappa_{S} } \right)_{12} = \, (\rho_{12} u_{12}^{2} )^{ - 1} $$
(2)

where x i, M i and ρ i are the mole fraction, molar mass and density of [emim][BF4] and ρ 12 is the density of the (1 + 2) mixture. The \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \) values were then determined by using

$$ \kappa_{S}^{\text{E}} = \kappa_{S} - \kappa_{S}^{\text{id}} $$
(3)
Table 2 Measured densities, ρ 12, excess molar volumes, \( V_{12}^{\text{E}} \), speeds of sound, u 12, isentropic compressibilities, \( \left( {\kappa_{S}^{{}} } \right)_{12} \), and excess isentropic compressibilities, \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \), for the various (1 + 2) mixtures as a function of mole fraction, x 1, of component (1) at T = (293.15, 298.15, 303.15, 308.15) K
Table 3 Measured excess molar enthalpy, \( H_{12}^{\text{E}} \), values for the various (1 + 2) mixtures as a function of mole fraction x 1, of component (1) at 298.15 K

The \( \kappa_{S}^{\text{id}} \) values were evaluated by employing the following relation [36]

$$ \kappa_{S}^{\text{id}} = \sum\limits_{i = 1}^{2} {\phi_{i} \left[ {\kappa_{s,i} + \frac{{Tv_{i} \alpha_{i}^{2} }}{{C_{p,i} }}} \right] - T\left( {\sum\limits_{i = 1}^{2} {x_{i} v_{i} } } \right)\frac{{\left( {\sum\limits_{i = 1}^{2} {\phi_{i} \alpha_{i} } } \right)^{2} }}{{\left( {\sum\limits_{i = 1}^{2} {x_{i} C_{p,i} } } \right)}}} $$
(4)

where ϕ i is the volume fraction of component (1). The κ s,i , v i , α i and C p,i are isentropic compressibility, molar volume, thermal expansion coefficient, and molar heat capacity, respectively, of the pure component (1). The C p values for the investigated liquids were taken from the literature [22, 29, 3739] and are reported in Table 1. While the α values for [emim][BF4] were predicted by using experimental density data in the manner described elsewhere [40], those for NMF and DMF were taken from the literature [28]. The \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \) values for the (1 + 2) mixtures are recorded in Table 2.

The \( V_{12}^{\text{E}} ,H_{12}^{\text{E}} \) and \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \) values (plotted in Figs. 1, 2, 3, 4, 5, 6, 7, 8, 9) were fitted with the Redlich–Kister equation, Eq. 5:

$$ Y_{12}^{\text{E}} (Y = \,V\,{\text{or}}\,H\,{\text{or}}\,\kappa_{S}^{{}} )\,\, = \,x_{1} x_{2} [Y^{(0)} + \,Y^{(1)} (2x_{1} - 1) + Y^{(2)} (2x_{2} - 1)^{2} ] $$
(5)

where \( Y_{12}^{\left( n \right)} (n = 0 - 2) \), etc., are binary adjustable parameters and were determined by fitting \( Y_{12}^{\text{E}} \) (Y = V or H or κ S ) data to Eq. 5 using the least-squares method. The parameters along with their standard deviations, σ(\( Y_{12}^{\text{E}} \)) \( (Y = \,V\,{\text{or}}\,H\,{\text{or}}\,\kappa_{S} ) \), are listed in Table 4.

Fig. 1
figure 1

Excess molar volumes, \( V_{12}^{\text{E}} \), at T = 293.15 for: (I) 1-ethyl-3-methylimidazolium tetrafluoroborate (1) + N-methyl formamide (2). The line represents fitting of the measured data with Eq. 5, pink curved line, Graph pink open circle, PFP pink filled circle. (II) 1-Ethyl-3-methylimidazolium tetrafluoroborate (1) + N,N-dimethyl formamide (2). The line represents fitting of the measured data with Eq. 5, violet curved line, Graph violet down-pointing open triangle, PFP violet down-pointing filled triangle

Fig. 2
figure 2

Excess molar volumes, \( V_{12}^{\text{E}} \), at T = 298.15 for: (I) 1-ethyl-3-methylimidazolium tetrafluoroborate (1) + N-methyl formamide (2). The line represents fitting of the measured data with Eq. 5, pink curved line, Graph pink open circle, PFP pink filled circle. (II) 1-Ethyl-3-methylimidazolium tetrafluoroborate (1) + N,N-dimethyl formamide (2). The line represents fitting of the measured data with Eq. 5, violet curved line, Graph violet down-pointing open triangle, PFP violet down-pointing filled triangle

Fig. 3
figure 3

Excess molar volumes, \( V_{12}^{\text{E}} \), at T = 303.15 for (I) 1-ethyl-3-methylimidazolium tetrafluoroborate (1) + N-methyl formamide (2). The line represents fitting of the measured data with Eq. 5, pink curved line, Graph pink open circle, PFP pink filled circle. (II) 1-Ethyl-3-methylimidazolium tetrafluoroborate (1) + N,N-dimethyl formamide (2). The line represents fitting of the measured data with Eq. 5, violet curved line, Graph violet down-pointing open triangle, PFP violet down-pointing filled triangle

Fig. 4
figure 4

Excess molar volumes, \( V_{12}^{\text{E}} \), at T = 308.15 for (I) 1-ethyl-3-methylimidazolium tetrafluoroborate (1) + N-methyl formamide (2). The line represents fitting of the measured data with Eq. 5, pink curved line, Graph pink open circle, PFP pink filled circle. (II) 1-Ethyl-3-methylimidazolium tetrafluoroborate (1) + N,N-dimethyl formamide (2). The line represents fitting of the measured data with Eq. 5, violet curved line, Graph violet down-pointing open triangle, PFP violet down-pointing filled triangle

Fig. 5
figure 5

Excess isentropic compressibilities, \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \), at T = 293.15 for (I) 1-ethyl-3-methylimidazolium tetrafluoroborate (1) + N-methyl formamide (2). The line represents fitting of the measured data with Eq. 5, pink curved line, Graph pink open circle, PFP pink filled circle. (II) 1-Ethyl-3-methylimidazolium tetrafluoroborate (1) + N,N-dimethyl formamide (2). The line represents fitting of the measured data with Eq. 5, violet curved line, Graph violet down-pointing open triangle, PFP violet down-pointing filled triangle

Fig. 6
figure 6

Excess isentropic compressibilities, \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \), at T = 298.15 for (I) 1-ethyl-3-methylimidazolium tetrafluoroborate (1) + N-methyl formamide (2). The line represents fitting of the measured data with Eq. 5, pink curved line, Graph pink open circle, PFP pink filled circle. (II) 1-Ethyl-3-methylimidazolium tetrafluoroborate (1) + N,N-dimethyl formamide (2). The line represents fitting of the measured data with Eq. 5, violet curved line, Graph violet down-pointing open triangle, PFP violet down-pointing filled triangle

Fig. 7
figure 7

Excess isentropic compressibilities, \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \), at T = 303.15 for (I) 1-ethyl-3-methylimidazolium tetrafluoroborate (1) + N-methyl formamide (2). The line represents fitting of the measured data with Eq. 5, pink curved line, Graph pink open circle, PFP pink filled circle. (II) 1-Ethyl-3-methylimidazolium tetrafluoroborate (1) + N,N-dimethyl formamide (2). The line represents fitting of the measured data with Eq. 5, violet curved line, Graph violet down-pointing open triangle, PFP violet down-pointing filled triangle

Fig. 8
figure 8

Excess isentropic compressibilities, \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \), at T = 308.15 for (I) 1-ethyl-3-methylimidazolium tetrafluoroborate (1) + N-methyl formamide (2). The line represents fitting of the measured data with Eq. 5, pink curved line, Graph pink open circle, PFP pink filled circle. (II) 1-Ethyl-3-methylimidazolium tetrafluoroborate (1) + N,N-dimethyl formamide (2). The line represents fitting of the measured data with Eq. 5, violet curved line, Graph violet down-pointing open triangle, PFP violet down-pointing filled triangle

Fig. 9
figure 9

Excess molar enthalpies, \( H_{12}^{\text{E}} \), at T = 298.15 for (I) 1-ethyl-3-methylimidazolium tetrafluoroborate (1) + N-methyl formamide (2). The line represents fitting of the measured data with Eq. 5, pink curved line, Graph pink open circle, PFP pink filled circle. (II) 1-Ethyl-3-methylimidazolium tetrafluoroborate (1) + N,N-dimethyl formamide (2). The line represents fitting of the measured data with Eq. 5, violet curved line, Graph violet down-pointing open triangle, PFP violet down-pointing filled triangle

Table 4 Binary adjustable parameters \( Y_{12}^{\text{E}} (Y = \,V\,{\text{or}}\,H\,{\text{or}}\,\kappa_{S} ) \), n = 0–2 of Eq. 5, along with their corresponding standard deviations, σ(\( Y_{12}^{\text{E}} \)) of \( V_{12}^{\text{E}} ,H_{12}^{\text{E}} \) and \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \) at T = (293.15, 298.15, 303.15, and 308.15) K

4 Discussion

The \( V_{12}^{\text{E}} \) and \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \) values for the (1 + 2) mixtures are negative over the entire composition range and for the equimolar composition follow the sequence: NMF > DMF. However, while the \( H_{12}^{\text{E}} \) values for the [emim][BF4] (1) + DMF (2) mixtures are negative, those for [emim][BF4] (1) + NMF (2) mixtures are positive over the entire composition range.

The \( H_{12}^{\text{E}} \) data of the studied mixtures may be explained qualitatively, if it is assumed that (i) [emim][BF4] is characterized by ionic interactions and exists as its monomer, while NMF and DMF exist as associated entities and there is formation of 1–2 n contacts in the mixed state; (ii) unlike 1–2 n contacts lead to weakening of ionic interactions and also rupture of the associated amide molecules to form their respective monomers; and (iii) ion–dipole interactions (between the N atom of the imidazolium ring and the fluorine atom of the [BF4] anion with the oxygen atom of NMF or DMF and the hydrogen atom of NMF) exist in the mixtures. The \( H_{12}^{\text{E}} \) values for [emim][BF4] (1) + DMF (2) mixtures suggest that the contribution to \( H_{12}^{\text{E}} \) due to factors (i) and (iii) outweigh the contribution to \( H_{12}^{\text{E}} \) due to factor (ii), and thus the overall \( H_{12}^{\text{E}} \) values for this mixture are negative. Further, amide–amide interactions become weaker in the sequence primary > secondary > tertiary, so the contribution to \( H_{12}^{\text{E}} \) due to rupture of NMF–NMF interactions upon mixing will be larger than that related to the breaking of DMF–DMF interactions, and consequently the contribution to \( H_{12}^{\text{E}} \) from factor (ii) will outweigh the contribution due to factors (ii) and (iii), which leads to the positive values of \( H_{12}^{\text{E}} \) for [emim][BF4] (1) + NMF (2) mixtures.

The sign as well as the magnitude of \( V_{12}^{\text{E}} \) and \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \) arise due to (i) rupture of associated entities in the mixed state, to (ii) the molecular arrangement and packing of the constituents of mixtures, and (iii) molecular interactions existing in these mixtures. The negative \( V_{12}^{\text{E}} \) values for these mixtures suggest that the contribution to \( V_{12}^{\text{E}} \) due to ion—the dipole interactions and molecular packing is more than that of the contribution from rupture of associated entities. This may be due to (i) the larger difference between the molar volumes of [emim][BF4] (154.70 × 10−6 m3·mol−1) and NMF (59.06 × 10−6 m3·mol−1) or DMF (77.28 × 10−6 m3·mol−1), which allows small molecules to fit into the available free volume of the ionic liquid; and (ii) ion–dipole interactions occur in the mixtures. Further, the \( V_{12}^{\text{E}} \) values suggest that (1 + 2) mixtures contain relatively more packed structure in the mixed state as compared to their pure states. The temperature coefficients (∂V E/∂T) and (∂\( \kappa_{S}^{\text{E}} \)/∂T) are negative for the studied mixtures, which in turn suggests that the ion–dipole interaction increases with rise in temperature. The decrease in speed of sound values for the mixtures with increasing temperature also supports this viewpoint.

5 Graph Theory

5.1 Excess Molar Volumes

Graph theory deals with the topology of molecules constituting the mixture. As the topology of the molecules changes on addition of component 1–2 or vice versa, it is, therefore, worthwhile to analyze the \( V_{12}^{\text{E}} \) data in terms of Graph theory. According to this theory, \( V_{12}^{\text{E}} \) is given [41] by:

$$ V_{12}^{\text{E}} = \alpha_{ 1 2} \left\{ {\left[ {\Upsigma x_{i}(^{ 3} \xi_{i} )_{\text{m}} } \right]^{ - 1} - \Upsigma x_{i} (^{3} \xi_{i} )^{ - 1} } \right\} $$
(6)

where α 12 is a constant characteristic of the (1 + 2) mixtures. The (3 ξ i ) and (3ξ i )m (i = 1 or 2) are the connectivity parameters of third degree of the components (1) and (2) in the pure and mixed state and are defined [42] by:

$$ ^{3} \xi = \sum\limits_{{\user2{m} < \user2{n} < \user2{o} < \user2{p}}} {\left( {\delta _{\user2{m}}^{{\text{v}}} \,\delta _{\user2{n}}^{{\text{v}}} \,\delta _{\user2{o}}^{{\text{v}}} \,\delta _{\user2{p}}^{{\text{v}}} } \right)^{{ - 0.5}} } $$
(7)

where the \( \delta_{\text{m}}^{{{\upnu}}} \) etc. values have the same significance as described elsewhere [43]. The evaluation of \( V_{12}^{\text{E}} \) from Eq. 6 requires knowledge of the connectivity parameters of third degree, (3 ξ i ) (i = 1 or 2) or (3 ξ i )m (i = 1 or 2), that are parameters of the components of mixtures in their pure and mixed state. In the present investigations, we have evaluated these parameters from the measured \( V_{12}^{\text{E}} \) data at one temperature and 1 mole fraction (x 1 = 0.5). The (3 ξ i ) or (3 ξ i )m (i = 1 or 2) values were then subsequently utilized to predict \( V_{12}^{\text{E}} \) at other mole fractions. Such \( V_{12}^{\text{E}} \) values are shown in Figs. 1, 2, 3, 4 and are compared with the corresponding experimental values. Also, the (3 ξ i ), (3 ξ i )m (i = 1 or 2), and α 12 values are listed in Table 5. Examination of Figs. 1, 2, 3, 4 reveals that the (3 ξ i ) or (3 ξ i )m (i = 1 or 2) values reproduce the experimental \( V_{12}^{\text{E}} \) data reasonably well and hence (3 ξ i ) or (3 ξ i )m (i = 1 or 2) can be utilized to extract information about the state of 1 and 2 in the pure and mixed states.

Table 5 Interaction energies \( \chi^{*} ,\chi_{12}^{/} \), etc. parameters of Eq. 9 along with connectivity parameters of the third degree of a molecule, (3 ξ i ) or (3 ξ i )m (i = 1 or 2), and α 12 of Eq. 6 utilized in Graph theory for the determination of \( V_{12}^{\text{E}} ,H_{12}^{\text{E}} \) and \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \) at T = (293.15, 298.15, 303.15, 308.15) K

A number of structures were proposed for [emim][BF4], NMF and DMF, and their 3 ξ / values were determined (using Eq. 7) taking in consideration their molecular structure. The structure or combination of structures that yielded 3 ξ / values that are comparable with the 3 ξ values (Table 5) were considered to be a representative structure of that component. For the (1 + 2) mixtures, it was assumed that [emim][BF4], NMF and DMF in their pure states exist as the molecular entities I, II–III, and IV–V, respectively (Scheme 1). The 3 ξ / value for molecular entity I was predicted by using the proposed structure of [emim][BF4] based on IR, Raman spectra and quantum mechanics analysis [4446]. The proposed structure suggest that (i) the [BF4] anion is positioned over the imidazolium ring of the [emim]+ cation and has short contacts with H–C(2) as well as a proton of the –CH3 group (in imidazolium ring); and (ii) ion-pair formation strongly influences three antisymmetric B–F stretching vibrations of the [BF4] anion and out-of-plane, stretching vibrations of the H–C(2) moiety of the cation. The 3 ξ / values for molecular entities I–V were then calculated to be 1.639, 0.236, 0.947, 0.211, 0.809. The experimental 3 ξ values are 1.505 and 1.502, 1.096, 1.095 for [emim][BF4], NMF, and DMF (Table 5), which suggests that while [emim][BF4] exist as a monomer (molecular entity I, 3 ξ /= 1.639), NMF (molecular entity III, 3 ξ /= 0.947) and DMF (molecular entity V, 3 ξ /= 0.809) exist as associated entities in their pure state. The state of components in (1 + 2) mixed solutions were then studied by predicting (3 ξ /2 )m values of NMF or DMF in [emim][BF4]. For this purpose, we assumed that [emim][BF4] (1) + NMF or DMF (2) mixtures possessed molecular entities VI and VII, respectively.

Scheme 1
scheme 1

Connectivity parameters, 3 ξ / of the third degree for various molecular entities

In evaluating (3 ξ /2 )m values for these molecular entities VI and VII, it was assumed that while molecular entity VI is characterized by interactions between the N atom (N-3) of [emim]+ as well as a fluorine atom of [BF4] with oxygen and hydrogen atoms of NMF, molecular entity VII is characterized by interactions among the N atom (N-3) of [emim]+ as well as the fluorine atom of [BF4] with the oxygen of DMF. The (3 ξ /2 )m values for these molecular entities were then predicted to be 0.891 and 1.084, respectively. The experimental (3 ξ 2)m values of 1.096 and 1.095 for [emim][BF4] (1) + NMF or DMF (2) mixtures (Table 5) suggest that these mixtures contain molecular entities VI and VII. To substantiate the existence of molecular entities VI and VII, we analyzed the spectral data of pure [emim][BF4], NMF, DMF and [emim][BF4] (1) + NMF or DMF (2) equimolar mixtures. Analysis of the IR data revealed that while [emim][BF4], NMF and DMF in their pure states show characteristic vibrations at 3,130 cm−1 (C–H vibrations), 524 cm−1 (B–F stretching), 1,672 and 1,670 cm−1 (C=O), 3,170 cm−1 (N–H) [47], the [emim][BF4] (1) + NMF or DMF (2) mixtures showed characteristic vibrations at 3,156 and 3,162 cm−1 (C–H vibrations), 536 and 533 cm−1 (B–F stretching), 1,660 and 1,659 cm−1 (C=O), and 3,182 cm−1 (N–H), respectively. The IR studies thus suggest that addition of NMF or DMF to [emim][BF4] does influence (i) the H–C(2) vibrations of [emim]+, (ii) B–F stretching of [BF4], (iii) C=O vibrations of NMF or DMF, and (iv) N–H vibrations of NMF. Furthermore, shifting of the C–H vibrations to higher wave numbers suggest breaking of interactions between the hydrogen atom of the imidazolium ring of [emim]+ and fluorine atom of [BF4], which in turn support the existence of molecular entities VI and VII in the studied mixtures.

5.2 Excess Molar Enthalpies and Excess Isentropic Compressibilities

The analysis of \( V_{12}^{\text{E}} \) data for the investigated mixtures in terms of Graph theory has revealed that while [emim][BF4] exists as a monomer, NMF and DMF exist as associated entities. The measured \( H_{12}^{\text{E}} \) and \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \) data can be analyzed in terms of Graph theory, if it is assumed that the (1 + 2) investigated mixture formation involves the following processes: (i) formation of unlike 1–2 n contacts; (ii) unlike contact formation then weakens 2 n –2 n interactions and ionic interactions in [emim][BF4], which leads to the depolymerization of 2 n to form monomers of 2 components; and (iii) monomers of 1 and 2 undergo ion–dipole interactions to form a 1:1 molecular complex. If \( \chi_{12} ,\chi_{22} \) and \( \chi_{12}^{/} \) represent molar interaction and molar compressibility interaction parameters for 1–2 n contacts, depolymerization of 2 n components, and ion–dipole interactions between 1 and 2 components, then the change in thermodynamic properties, \( Y_{12}^{\text{E}} \) (Y = H or κ S ) is given [4851] by:

$$ \begin{aligned} Y_{{12}}^{{\text{E}}} \left( {Y = {\text{ Hor }}\kappa _{S} } \right) & = \left[ {\frac{{x_{1} x_{2}\left( {^{3} \xi _{1} /^{3} \xi _{2} } \right)}}{{x_{1} + x_{2}\left( {^{3} \xi _{1} /^{3} \xi _{2} } \right)}}} \right]\left[{\chi _{{12}} } \right] + {\frac{x_{1}^{2} x_{2} \left( {^{3} \xi_{1} /^{3} \xi _{2} } \right)}{x_{1} + x_{2} \left( {^{3} \xi_{1} /^{3} \xi _{2} } \right)}}\left[ {\chi _{{22}} } \right] \\& \quad + \left[ {\frac{{x_{1} x_{2}^{2} \left( {^{3} \xi_{1} /^{3} \xi _{2} } \right)}}{{x_{1} + x_{2} \left( {^{3} \xi_{1} /^{3} \xi _{2} } \right)}}} \right]\left[ {\chi _{{12}}^{/} }\right] \\\end{aligned} $$
(8)

.

Further, if it is assumed that the interaction parameters for unlike contacts and ion–dipole interactions between the (1) and (2) components are nearly equal, χ 12 ≅ χ 22 = χ *, then Eq. 8 reduces to:

$$ Y_{12}^{\text{E}} (Y \, = { H } {\text{or }}\kappa_{S} ) = \left[ {\frac{{x_{1} x_{2} \left( {{}^{3}\xi_{1} /{}^{3}\xi_{2} } \right)}}{{x_{1} + x_{2} \left( {{}^{3}\xi_{1} /{}^{3}\xi_{2} } \right)}}} \right]\left[ {\left( {1 + x_{1} } \right)\chi^{*} + x_{2} \chi_{12}^{/} } \right] $$
(9)

Equation 9 contains two unknown χ * and \( \chi_{12}^{/} \) parameters. These parameters were evaluated by using \( H_{12}^{\text{E}} \) and \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \) data at x 1 = 0.4 and 0.6, and were then subsequently utilized to predict \( H_{12}^{\text{E}} \) and \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \) values of (1 + 2) mixtures at other values of x 1. Such \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \) and \( H_{12}^{\text{E}} \) values of the investigated mixtures are plotted in Figs. 5, 6, 7, 8 and 9, respectively, and are compared with their experimental values. The χ * and \( \chi_{12}^{/} \) parameters, along with deviations between experimental \( V_{12}^{\text{E}} ,\left( {\kappa_{S}^{\text{E}} } \right)_{12} \) and \( H_{12}^{\text{E}} \) values and the corresponding values obtained from Graph theory, are recorded in Table 5. Examination of Figs. 5, 6, 7, 8, 9 reveals that the \( H_{12}^{\text{E}} \) and \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \) values compare well with their experimental values which, in turn, supports the various assumptions made in deriving Eq. 9.

6 Prigogine–Flory–Patterson (PFP) Theory

6.1 Excess Molar Volumes

The PFP theory [52] assumes that \( V_{12}^{\text{E}} \) is the sum of three contributions: (i) an interaction contribution, (ii) a free volume contribution, and (iii) an internal pressure contribution.

Each contributing term is given by:

$$ \frac{{V_{\text{interactiont}}^{\text{E}} }}{{\sum\limits_{i = 1}^{2} {x_{i} v_{i}^{*} } }} = \frac{{\left[ {(\tilde{v}^{1/3} - 1)\tilde{v}\psi_{1} \theta_{2} \chi_{12}^{*} } \right]}}{{\left[ {\left( {4/3} \right)\tilde{v}^{ - 1/3} - 1} \right]\tilde{v}}} $$
(10)
$$ \frac{{V_{\text{free - volume}}^{\text{E}} }}{{\sum\limits_{i = 1}^{2} {x_{i} v_{i}^{*} } }} = \left[ {\left( {\tilde{v}_{1} - \tilde{v}_{2} } \right)^{2} \left\{ {\left( {14/9} \right)\tilde{v}^{ - 1/3} - 1} \right\}} \right]\frac{{\psi_{1} \psi_{2} }}{{[\left( {4/3} \right)\tilde{v}^{ - 1/3} - 1]\tilde{v}}} $$
(11)
$$ \frac{{V_{{P^{*} {\text{effict}}}}^{\text{E}} }}{{\sum\limits_{i = 1}^{2} {x_{i} v_{i}^{*} } }} = \frac{{(\tilde{v}_{1} - \tilde{v}_{2} )\,(P_{1}^{*} - P_{2}^{*} )\,\psi_{1} \psi_{2} }}{{(P_{1}^{*} \psi_{2} - P_{2}^{*} \psi_{1} )}} $$
(12)

6.2 Excess Molar Enthalpies

According to the PFP theory [53], \( H_{12}^{\text{E}} \) values are due to interaction contributions as well as free volume contributions and are expressed by:

$$ H_{12}^{\text{E}} = H_{\text{interaction}}^{\text{E}} + H_{\text{free - volume}}^{\text{E}} $$
(13)

where

$$ \frac{{H_{\text{interaction}}^{\text{E}} }}{{(x_{1} U_{1}^{*} + x_{2} U_{2}^{*} )}} = \left( {\frac{{\chi_{12} \theta_{2} \psi_{1} }}{{P_{1}^{*} }}} \right)\,\left( {\tilde{U}\tilde{T}_{U} + \tilde{T}_{U} \tilde{C}_{P} \tilde{T}_{U} } \right) $$
(14)
$$ \frac{{H_{\text{free - volume}}^{\text{E}} }}{{(x_{1} U_{1}^{*} + x_{2} U_{2}^{*} )}} = \tilde{C}_{p} (\tilde{T}_{U} )\left( {\psi_{1} \tilde{T}_{1} + \psi_{2} \tilde{T}_{2} - \tilde{T}_{U} } \right) $$
(15)

6.3 Excess Isentropic Compressibilities

The quantity \( \left( {\kappa_{S}} \right)_{12} \) is given [54] by:

$$ \left( {\kappa_{S} } \right)_{12} = - \frac{1}{V}\left( {\frac{\partial V}{\partial p}} \right)_{S} $$
(16)

where

$$ \left( {\frac{\partial V}{\partial p}} \right)_{S} = \left( {\frac{\partial V}{\partial p}} \right)_{T} + TC_{p}^{ - 1} \left( {\frac{\partial V}{\partial T}} \right)_{p} $$
(17)

\( \left( {\frac{\partial V}{\partial p}} \right)_{T} \) and \( \left( {\frac{\partial V}{\partial T}} \right)_{p} \) are expressed by Eqs. 18 and 19, respectively, where

$$ \left( {\frac{\partial V}{\partial p}} \right)_{T} = \left( {\frac{{ - \tilde{v}^{7/3} + 2\tilde{v}^{2} - \tilde{v}^{5/3} }}{{4/3 - \tilde{v}^{1/3} }}} \right)\frac{{V^{*} }}{{p^{*} }}\frac{1}{{\tilde{T}}} $$
(18)
$$ \left( {\frac{\partial V}{\partial T}} \right)_{p} = \left( {\frac{{\tilde{v}^{4/3} - \tilde{v}}}{{4/3 - \tilde{v}^{1/3} }}} \right)\frac{{V^{*} }}{T} $$
(19)

All of the terms in Eqs. 1019 have the same significance as described elsewhere [55, 56].

The \( V_{12}^{\text{E}} ,H_{12}^{\text{E}} \) and \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \) values by PFP theory can be predicted if the interaction energy parameter \( \chi_{12}^{*} \), in addition to the Flory’s parameters and isobaric heat capacities of the pure liquids and mixtures, are known. The interaction parameter \( \chi_{12}^{*} \) was determined by fitting of the \( H_{12}^{\text{E}} \) value of investigated (1 + 2) mixtures at x 1 = 0.5 to Eq. 21:

$$ H_{12}^{\text{E}} = \sum {x_{i} p_{i}^{*} \left( {U_{i}^{ - 1} - U_{\text{cal}}^{ - 1} } \right) + x_{1} U_{1}^{*} \theta_{2} \chi_{12}^{*} U_{\text{cal}}^{ - 1} } $$
(20)

The various parameters for the pure components were determined using isothermal compressibility results reported in the literature [22, 29, 3335]. The κ T values for [emim][BF4] were predicted in the manner described elsewhere [40, 57], and for NMF and DMF were determined by using their ∆H v values [58]. Such \( V_{12}^{\text{E}} ,\left( {\kappa_{S}^{\text{E}} } \right)_{12} \) and \( H_{12}^{\text{E}} \) values are plotted in Figs. 1, 2, 3, 4, 5, 6, 7, 8 and 9, respectively. Further, the interaction energy parameter \( \chi_{12}^{*} \), along with deviations between experimental \( V_{12}^{\text{E}} ,\left( {\kappa_{S}^{\text{E}} } \right)_{12} \) and \( H_{12}^{\text{E}} \) values and the corresponding values obtained from PFP theory are reported in Table 6. Examination of Figs. 1, 2, 3, 4, 5, 6, 7, 8, 9 reveals that the PFP theory correctly predicts the sign of \( V_{12}^{\text{E}} ,H_{12}^{\text{E}} \) and \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \) values for all of the studied mixtures. However, quantitative agreement is not as impressive as compared to the values predicted by Graph theory. The failure of the PFP theory to correctly predict the magnitude of \( V_{12}^{\text{E}} ,H_{12}^{\text{E}} \) and \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \) data may be due to strong interactions between unlike molecules in the mixtures. Further, examination of \( \chi_{12}^{*} \) values for [emim][BF4] (1) + NMF or DMF (2) mixtures indicates that, while the \( \chi_{12}^{*} \) values for [emim][BF4] (1) + NMF (2) are positive, those for [emim][BF4] (1) + DMF (2) are negative. This is probably due to strong self-association of NMF in comparison to DMF, which prevents strong interaction between NMF and [emim][BF4] leading to the positive value for \( \chi_{12}^{*} \).

Table 6 Values of the interaction energy, \( \chi_{ij}^{*} \), parameter of the PFP theory along with the standard deviations σ(V E, PFP), \( \sigma (\kappa_{S}^{\text{E}} ,{\text{ PFP}}) \), and σ(H E, PFP) from experimental values, \( V_{12}^{\text{E}} ,H_{12}^{\text{E}} \) and \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \), and the values obtained from the PFP theory

7 Conclusion

The experimental density and speed of sound data of the investigated ionic liquid binary mixtures have been utilized to determine \( V_{12}^{\text{E}} \) and \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \). The \( V_{12}^{\text{E}} ,H_{12}^{\text{E}} \) and \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \) data have been fitted to Redlich–Kister equation to predict binary adjustable parameters and standard deviations. The \( V_{12}^{\text{E}} ,H_{12}^{\text{E}} \) and \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \) data for the studied ionic liquid mixtures have been analyzed in terms of Graph theory. It has been observed that Graph theory, which has been applied for the first time to ionic liquid mixtures, described well the observed thermodynamic properties as well as the state of components in their pure and mixed states. The \( V_{12}^{\text{E}} ,H_{12}^{\text{E}} \) and \( \left( {\kappa_{S}^{\text{E}} } \right)_{12} \) data have also been analyzed in terms of PFP theory. The agreement between experimental values and the values determined by PFP theory is not impressive, although the sign of the predicted values are the same as the experimental values.