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Original article
12 (
8
); 5079-5085
doi:
10.1016/j.arabjc.2016.12.004

Densities, viscosities, and refractive indices for binary and ternary mixtures of formamide (1) + N,N-dimethylacetamide (2) + 2-methyl-1-butanol (3) at 298.15 K for the liquid region and at ambient pressure

Department of Physical Chemistry, Faculty of Chemistry, Bu-Ali Sina University, Hamedan, Iran

⁎Corresponding author. Fax: +98 8118282807. iloukhani@basu.ac.ir (Hossein Iloukhani)

Disclaimer:
This article was originally published by Elsevier and was migrated to Scientific Scholar after the change of Publisher.

Peer review under responsibility of King Saud University.

Abstract

This article reports experimental densities ρ, viscosities η, and refractive indices nD, of the ternary systems of formamide (1) + N,N-dimethylacetamide (2) + 2-methyl-1-butanol (3) and the binary systems of formamide (1) + N,N-dimethylacetamide (2), formamide (1) + 2-methyl-1-butanol (3), and N,N-dimethylacetamide (2) + 2-methyl-1-butanol (3) over the entire range of composition at T = 298.15 K for the liquid region and at ambient pressure. Excess molar volumes V m E , deviations in the viscosity Δη, and deviations in the refractive index ΔnD, for the mixtures were derived from the experimental data. The binary and ternary data of V m E , Δη, and ΔnD, were correlated as a function of the mole fraction by using the Redlich–Kister and the Cibulka equations, respectively. The results are consistent with the self-association of alcohol and the polar characters of used amide. McAlister’s multibody interaction model is used for correlating the kinematic viscosity of binary mixtures, with mole fraction. The experimental and the constituted binary and ternary systems are analyzed to discuss the nature and strength of intermolecular interactions in these mixtures.

Keywords

Excess molar volume
Deviation in the viscosity and Refractive index
Formamide
N,N-dimethylacetamide
2-Methyl-1-butanol
1

1 Introduction

This paper is a part of an ongoing research program in which we study thermodynamic, and transport properties of binary and ternary mixtures (Iloukhani and Zarei, 2004; Iloukhani et al., 2000; Iloukhani and Rakhshi, 2009; Zarei and Iloukhani, 2003; Khanlarzadeh and Iloukhani, 2011; Fattahi and Iloukhani, 2010). Experimental data of properties such as density ρ , and viscosity η , and refractive index nD, at over the whole composition range for binary and ternary liquid mixtures are useful for a full understanding of their thermodynamic and transport properties, as well as for practical chemical engineering purposes (Matthew and Koga, 2002; Zhang et al., 2008). On the other hand, excess thermodynamic properties and deviations of non-thermodynamic ones of binary liquid mixtures are fundamental for the design of industrial equipment and for the interpretation of the liquid state, particularly when polar components are involved. These properties have also been used as a qualitative and quantitative guide to predict the extent of complex formation in this kind of mixtures (Gomez Marigliano and Solimo, 2002). Here, we have measured densities ρ , viscosities η , and refractive indices nD, for the binary and ternary systems formed by formamide, N,N-dimethylacetamide, and 2-methyl-1-butanol at T = 298.15 K for the liquid region and at ambient pressure for the whole composition range. The data obtained are used to calculate excess molar volumes, deviations in the viscosity, deviations in the refractive index, and excess Gibbs energies of activation of viscous flow of the binary and ternary mixtures. The excess and deviation quantities of binary mixtures have been fitted to the Redlich–Kister equation to determine the coefficients. For correlating the ternary data, the Cibulka equation was used. The kinematic viscosity data for the binary mixtures were fitted to McAllister’s interaction model and their parameters have been calculated.

2

2 Experimental

2.1

2.1 Materials

The mole fraction purity of the components from Merck were as follows: formamide (w ⩾ 99), N,N-dimethylacetamide (w ⩾ 99), and 2-methyl-1-butanol (w ⩾ 99), where w is mass fraction. All chemical substances were used without any further purification. Purity of each compound was checked by measuring the densities and refractive index and found to be in good agreement with values found in the literature (Nain, 2007; Cases et al., 2001; Gimenez et al., 2008; Iloukhani and Khanlarzadeh, 2006; Resa et al., 2005), reported in Table 1.

Table 1 Comparison of measured densities and refractive indices of the pure components with literature values at 298.15 K.
Component ρ ( g / cm 3 ) n D
Experimental Literature Experimental Literature
Formamide 1.12904 1.12908a 1.4455 1.4468b
N,N-dimethylacetamide 0.93624 0.93634c 1.4357 1.4356d
2-Methyl-1-butanol 0.81537 0.8150e 1.4087 1.4086e

2.2

2.2 Apparatus and procedure

Densities of the pure liquids and their mixture were measured with an Anton Paar DMA 4500 oscillating U-tube densimeter, operated in the static mode and the uncertainties were estimated to be within ±1 × 10−2 kg m−3. The temperature in the cell was regulated to ±0.01 K with a solid-state thermostat. The apparatus was calibrated once a day with dry air and double-distilled freshly degassed water. The mixtures were prepared by weighing amounts of the pure liquids by syringing into stoppered bottles to prevent evaporation and reducing possible errors in mole fraction calculations. Ternary mixtures were prepared by mixing the three components. Each mixture was immediately used after it was well-mixed by shaking. All the weightings were performed on an electronic balance (AB 204-N Mettler) accurate to 0.1 mg. The uncertainty in the mole fraction is estimated to be lower than ±2 × 10−4.

Dynamic viscosities at 298.15 K were measured with an Ubbelohde viscometer. The equation for viscosity, according to Poiseuille’s law, is

(1)
η = ρ υ = ρ ( kt - c / t ) where k and c are the viscometer constants and t, η , and ν , are the efflux time, dynamic viscosity, and kinematic viscosity, respectively. The uncertainty of the viscosity measurements was estimated to be less than ±2 × 10−3 mPa s. The viscometer was suspended in a thermostated water bath maintained to ±0.01 K. An electronic digital stopwatch with uncertainty to ±0.01 s was used for flow time measurements. At least three repetitions of each data point obtained were reproducible to ±0.05 s, and the results were averaged.

Refractive indices were measured using a digital Abbe-type refractometer. Water was circulated into the prism of the refractometer by a circulation pump connected to an external thermostated water bath. The uncertainty of the refractive index is on the order of 0.0002 units.

3

3 Results and discussion

Table 2 lists the experimental densities, viscosities, refractive indices, excess molar volumes, deviations in viscosity, deviations in refractive index and excess Gibbs energy of activation for three binary systems formamide (1) + N,N-dimethylacetamide (2), formamide (1) + 2-methyl-1-butanol (3), and N,N-dimethylacetamide (2) + 2-methyl-1-butanol (3) at 298.15 K. The excess molar volumes V m E , were calculated from density data according to

(2)
V m E = i = 1 n x i M i ( ρ - 1 - ρ i - 1 ) where xi, Mi, and ρ i are the mole fraction, molar mass, and density of the pure component i, respectively. ρ is the density of mixture, and n is the number of components. In the system studied, excess molar volumes are negative for the system formamide (1) + N,N-dimethylacetamide (2) over the whole composition range. For the system formamide (1) + 2-methyl-1-butanol (3), and N,N-dimethylacetamide (2) + 2-methyl-1-butanol (3) an inversion of sign of V m E , is observed over part of the concentration range. In first system values V m E , are positive at lower concentrations of alcohol and negative at higher concentrations of it. Fig. 1 shows the excess molar volumes for the three binary systems at T = 298.15 K. A plausible qualitative interpretation of the behavior of these mixtures with composition has been suggested. In the systems considered here, we can recognize four different effects as being important, (i) hydrogen bond rupture, (ii) dispersive interactions between unlike molecules, (iii) intermolecular dipolar interactions, and (iv) geometrical fitting between components. The positive contribution to V m E , is expected from first two effects while opposite contribution from remaining two. The volumetric behavior of the formamide + N,N-dimethylacetamide mixture shows that effect (iii) and (iv) which leads to packing in volumes, predominates over the two (i) and (ii), which contribute to expansion. For the system of formamide (1) + 2-methyl-1-butanol (3), positive values of V m E , were observed in the region of x1 below 0.56 while negative values of V m E , were found for the other composition ranges. Mixing of formamide with alkanols would induce mutual dissociation of the hydrogen bonded structures present in pure liquids with subsequent formation of (new) H-bonds (C⚌⋯OH—O) between proton acceptor oxygen atom (with two lone pair of electrons) of C⚌O group of formamide and hydrogen atom of ⚌OH group(s) of alkanol molecules. Therefore at high concentration of alcohol dissociation is dominate while at low concentration opposite contribution (associated through hydrogen bonding and leading to a contraction in volume) is dominate. For the system of N,N-dimethylacetamide (2) + 2-methyl-1-butanol (3), negative values of V m E , were observed in the region of x1 below 0.32 while positive values of V m E , were found for the other composition ranges. A sigmoid shape observed may be attributed to the hydrogen bond effect that occurred between amide and alcohol. At low concentration of amide, hydrogen bonding is dominant resulting in negative values of V m E , whereas at higher mole fraction of amide, dispersive forces are dominant resulting in positive values of V m E . The other reason for this observation is steric hindrance of the two methyl groups of N,N-dimethylacetamide.
Table 2 Experimental densities ρ , viscosities η , refractive indices n D , excess molar volumes V m E , deviations in the viscosity Δ η , deviations in the Refractive Index Δ n D , and excess Gibbs energy of activation Δ G E , of viscous flow for the binary systems at 298.15 K.
x ρ ( g / cm 3 ) η ( mPa s ) n D V m E ( cm 3 / mol ) Δ η ( mP s ) Δ G E (J/mol) Δ n D
Formamide (1)+N,N-dimethylacetamide (2)
0.0811 0.94490 1.049 1.4370 −0.153 −0.027 192.719 0.0005
0.1596 0.95381 1.242 1.4381 −0.271 −0.010 409.411 0.0008
0.2403 0.96353 1.469 1.4391 −0.355 0.034 609.464 0.0010
0.3204 0.97372 1.740 1.4401 −0.395 0.125 811.345 0.0013
0.3978 0.98431 2.045 1.4410 −0.403 0.256 993.374 0.0014
0.4799 0.99664 2.402 1.4418 −0.390 0.427 1152.539 0.0014
0.5591 1.00974 2.735 1.4424 −0.351 0.583 1235.356 0.0012
0.6407 1.02512 3.080 1.4430 −0.308 0.743 1271.056 0.0010
0.7204 1.04190 3.340 1.4436 −0.235 0.824 1208.165 0.0008
0.7995 1.06156 3.464 1.4441 −0.175 0.770 1022.015 0.0006
0.8793 1.08485 3.485 1.4446 −0.110 0.612 741.455 0.0003
0.9607 1.11319 3.319 1.4452 −0.036 0.262 297.445 0.0001
N,N-dimethylacetamide (2)+2-methyl-1-butanol (3)
0.0803 0.82341 3.357 1.4106 −0.071 −0.804 −378.556 −0.0003
0.1600 0.83174 2.661 1.4125 −0.041 −1.216 −633.888 −0.0005
0.2397 0.84036 2.218 1.4145 −0.001 −1.375 −764.390 −0.0007
0.3207 0.84932 1.915 1.4164 0.020 −1.390 −804.579 −0.0009
0.3987 0.85820 1.685 1.4184 0.040 −1.343 −810.324 −0.0010
0.4801 0.86769 1.510 1.4206 0.071 −1.229 −757.163 −0.0011
0.5598 0.87731 1.367 1.4228 0.080 −1.089 −687.375 −0.0010
0.6402 0.88735 1.262 1.4249 0.079 −0.909 −566.148 −0.0010
0.7200 0.89768 1.157 1.4272 0.065 −0.731 −465.563 −0.0009
0.7996 0.90826 1.073 1.4295 0.050 −0.532 −338.052 −0.0008
0.8800 0.91934 0.999 1.4315 0.023 −0.321 −197.646 −0.0006
0.9588 0.93037 0.927 1.4344 0.007 −0.112 −70.095 −0.0002
Formamide (1)+2-methyl-1-butanol (3)
0.0801 0.82461 4.092 1.4096 0.066 −0.252 −67.299 −0.0020
0.1609 0.83532 3.983 1.4108 0.091 −0.257 −1.657 −0.0038
0.2398 0.84723 3.999 1.4121 0.092 −0.137 130.185 −0.0054
0.3199 0.86110 4.064 1.4139 0.066 0.032 284.186 −0.0066
0.4005 0.87688 4.147 1.4159 0.049 0.220 439.098 −0.0075
0.4808 0.89504 4.229 1.4181 0.018 0.406 579.834 −0.0083
0.5609 0.91594 4.301 1.4206 −0.007 0.583 701.292 −0.0087
0.6401 0.94020 4.331 1.4236 −0.037 0.716 781.568 −0.0087
0.7200 0.96901 4.317 1.4274 −0.057 0.807 819.646 −0.0078
0.7997 1.00348 4.146 1.4313 −0.067 0.739 744.175 −0.0068
0.8809 1.04647 3.792 1.4364 −0.071 0.491 522.241 −0.0047
0.9601 1.09837 3.347 1.4417 −0.043 0.149 181.922 −0.0023
Variation of excess molar volume V m E with mole fraction x1 for the binary systems at T = 298.15 K: ♦, Formamide (1) + N,N-dimethylacetamide (2); ▴, N,N-dimethylacetamide (2) + 2-methyl-1-butanol (3); ●, Formamide (1) + 2-methyl-1-butanol (3). Solid curves were calculated from the Redlich–Kister equation.
Figure 1 Variation of excess molar volume V m E with mole fraction x1 for the binary systems at T = 298.15 K: ♦, Formamide (1) + N,N-dimethylacetamide (2); ▴, N,N-dimethylacetamide (2) + 2-methyl-1-butanol (3); ●, Formamide (1) + 2-methyl-1-butanol (3). Solid curves were calculated from the Redlich–Kister equation.

The viscosity deviations Δ η , and excess Gibbs energies of activation of viscous flow Δ G E , for binary mixtures can be calculated as

(3)
Δ η = η - i N x i η i
(4)
Δ G E = RT ln ( ν M ) - i = 1 c x i ln ( ν i M i )
where M is the molecular weight, xi is the mole fraction and c refers to the number of components in the mixture η , is the absolute viscosity of the mixtures and η i , is the absolute viscosity of pure component i. The Δ η , values are also graphically represented as a function of mole fraction at 298.15 K in Fig. 2. It is observed that the Δ η , values for system formamide (1) + N,N-dimethylacetamide (2) and formamide (1) + 2-methyl-1-butanol (3), an inversion of sign of Δ η , are observed over part of the concentration range. This reveals that the strength of specific interaction is not the only factor influencing the viscosity deviation of liquid mixtures. The molecular size and shape of the components also play an equally important role. According to Meyer et al. the observed negative values of Δ G E correspond to the existence of solute–solute association.
Variation of deviation in the viscosity Δ η with mole fraction x1 for the binary systems at T = 298.15 K: ♦, Formamide (1) + N,N-dimethylacetamide (2); ▴, N,N-dimethylacetamide (2) + 2-methyl-2-methyl-1-butanol (3); ●, Formamide (1) + 2-methyl-1-butanol (3). Solid curves were calculated from the Redlich–Kister equation.
Figure 2 Variation of deviation in the viscosity Δ η with mole fraction x1 for the binary systems at T = 298.15 K: ♦, Formamide (1) + N,N-dimethylacetamide (2); ▴, N,N-dimethylacetamide (2) + 2-methyl-2-methyl-1-butanol (3); ●, Formamide (1) + 2-methyl-1-butanol (3). Solid curves were calculated from the Redlich–Kister equation.

The deviation in the refractive index from the mole fraction average Δ n D , is given by

(5)
Δ n D = n D - i n x i n D , i where n D and n D , i are the refractive index of the mixture and the refractive index of pure component i, respectively. For the whole composition range, the Δ n D , values are negative for systems formamide (1) + 2-methyl-1-butanol (3) and N,N-dimethylacetamide (2) + 2-methyl-1-butanol (3). The Δ n D , values for system formamide (1) + N,N-dimethylacetamide (2) are positive. Figs. 3 and 4 show the results of Δ n D , and Δ G E for the three binary mixtures at T = 298.15 K respectively. The mixing functions V m E , Δ η , and Δ n D were represented mathematically by the Redlich–Kister equation for correlating the experimental data (Redlich and Kister, 1948):
(6)
Δ Q ij = x i x j k = 0 m A k ( x j - x i ) k
where Δ Q ij refers to V m E / cm 3 mol - 1 , Δ η / mPa s , and Δ n D for each ij binary pair; xi is the mole fraction of component i; and Ak values are the coefficients. The values of coefficients Ak were determined by a multiple regression analysis based on the least squares method and are summarized along with the standard deviations between the experimental and the fitted values of the respective functions in Table 3. The standard deviation is defined by
(7)
σ = i = 1 n ( Δ Q exp , i + Δ Q cal , i ) / ( n - p ) 1 2
where n is the number of experimental points and p is the number of adjustable parameters. The experimental densities, viscosities, excess molar volumes, deviations in the viscosity, deviations in refractive index and excess Gibbs energy of activation of the ternary mixtures system formamide (1) + N,N-dimethylacetamide (2) + 2-methy1-butanol (3) at 298.15 K are listed in Table 4. The derived data ( V m E , Δ η , and Δ n D ) as defined in Eqs. (2)–(5) for the ternary system were correlated respectively using the equation
(8)
Δ Q 123 = Δ Q bin + x 1 x 2 x 3 Δ 123
(9)
Δ Q bin = i = 1 3 j . i 3 Δ Q ij
where Δ Q 123 refers to V m E , Δ η , and Δ n D , for the ternary system formamide (1) + N,N-dimethylacetamide (2) + 2-methyl-1-butanol (3). Δ Q ij in Eq. (9) is the binary contribution of each ij pair to the V m E , Δ η , and Δ n D , given by Eq. (6) with the parameters shown in Table 3. The ternary contribution term Δ 123 was correlated using the expression suggested by Cibulka (1982):
(10)
Δ 123 = B 0 + B 1 x 1 + B 2 x 2
where the ternary parameters B0, B1, and B2 were determined with the optimization algorithm similar to that for the binary parameters. The fitting parameters and the corresponding standard deviations are given in Table 3. As can be expected, the ternary system shows the same change in binary systems. McAllister’s multibody-interaction model (McAllister, 1960) is widely used for correlating the kinematic viscosity of binary mixtures with mole fraction. The three-body model is defined as
(11)
ln ν = x 1 3 ln ν 1 + 3 x 1 2 x 2 ln v 12 + 3 x 1 x 2 2 ln v 21 + x 2 3 ln ν 2 - ln x 1 + x 2 M 2 M 1 + 3 x 1 2 x 2 ln 2 / 3 + M 2 3 M 1 + 3 x 1 x 2 2 ln 1 / 3 + 2 M 2 3 M 1 + x 2 3 ln ( M 2 / M 1 )
and the four-body model is given by
(12)
ln ν = x 1 4 ln ν 1 + 4 x 1 3 x 2 ln ν 1112 + 6 x 1 2 x 2 2 ln ν 1122 + 4 x 1 x 2 3 ln ν 2221 + x 2 4 ln ν 2 - ln x 1 + x 2 M 2 M 1 + 4 x 1 x 2 3 ln 1 + 3 M 2 / M 1 4 + x 2 4 ln ( M 2 / M 1 ) + 4 x 1 3 x 2 ln 3 + M 2 / M 1 4 + 6 x 1 2 x 2 2 ln 1 + M 2 / M 1 2
where ν , ν 1 , and ν 2 are the kinematic viscosities of the mixture and the viscosities of pure components 1 and 2, respectively. ν 12 , ν 21 , ν 1112 , ν 1122 and ν 2221 are the model parameters. Table 5 records the calculated results with the standard deviation defined as in Eq. (7). It is shown that McAllister’s four-body equation gave a better result for those three systems.
Variation of deviation in the refractive index Δ n D with mole fraction x1 for the binary systems at T = 298.15 K: ♦, Formamide (1) + N,N-dimethylacetamide (2); ▴, N,N-dimethylacetamide (2) + 2-methyl-1-butanol (3); ●, Formamide (1) + 2-methyl-1-butanol (3). Solid curves were calculated from the Redlich–Kister equation.
Figure 3 Variation of deviation in the refractive index Δ n D with mole fraction x1 for the binary systems at T = 298.15 K: ♦, Formamide (1) + N,N-dimethylacetamide (2); ▴, N,N-dimethylacetamide (2) + 2-methyl-1-butanol (3); ●, Formamide (1) + 2-methyl-1-butanol (3). Solid curves were calculated from the Redlich–Kister equation.
Excess Gibs energies of the binary mixtures vs. mole fraction x1 for the binary systems at T = 298.15 K: ♦, Formamide (1) + N,N-dimethylacetamide (2); ▴, N,N-dimethylacetamide (2) + 2-methyl-1-butanol (3); ●, Formamide (1) + 2-methyl-1-butanol (3).
Figure 4 Excess Gibs energies of the binary mixtures vs. mole fraction x1 for the binary systems at T = 298.15 K: ♦, Formamide (1) + N,N-dimethylacetamide (2); ▴, N,N-dimethylacetamide (2) + 2-methyl-1-butanol (3); ●, Formamide (1) + 2-methyl-1-butanol (3).
Table 3 Binary coefficients of the Redlich−Kister equation Ak, at 298.15 K and ternary coefficients of the Cibulka equation for V m E , Δ η , and Δ n D at 298.15 K.
Δ Q ij A 0 A 1 A 2 A 3 A 4 σ
Formamide (1)+N,N-dimethylacetamide (2)
V m E (cm3/mol) −1.5233 0.8383 −0.0966 −0.2925 0.1409 0.0039
Δ η ( mPa s ) 1.8886 4.1602 1.4651 −0.2627 0.1721 0.0114
Δ n D 0.0054 −0.0018 −0.0028 −0.001 0.0024 0.000036
N,N-dimethylacetamide (2)+2-methyl-1-butanol (3)
V m E (cm3/mol) 0.2899 0.1039 −0.2824 0.8259 −0.9068 0.0069
Δ η ( mPa s ) −4.7762 3.3975 −2.4403 1.9729 −0.9216 0.00474
Δ n D −0.0042 −0.0008 −0.0017 0.0003 0.0027 0.000036
Formamide (1)+2-methyl-1-butanol (3)
V m E (cm3/mol) 0.0363 −0.6418 0.3016 −0.5868 −0.5001 0.0043
Δ η ( mPa s ) 1.7763 4.9465 1.3156 −0.3651 −4.5054 0.0143
Δ n D −0.0344 −0.0078 0.0072 −0.0097 −0.0228 0.000227
Δ Q 123 B 0 B 1 B 2 σ
V m E (cm3/mol) 1.6013 −3.5073 −2.8107 0.0372
Δ η / ( mPa s ) 5.02495 −16.6239 −10.6946 0.0229
Δ n D 0199.0 −0.0106 0.0007 0.0002
Table 4 Experimental densities ρ , viscosities η , refractive Indices n D , excess molar volumes V m E , deviation in the viscosity Δ η , deviations in the refractive index Δ n D , and excess Gibbs energy of activation Δ G E , of viscous flow for the ternary for the system formamide (1) + N,N-dimethylacetamide (2) + 2-methyl-1-butanol (3) at 298.15 K.
x 1 x 2 ρ ( g / cm 3 ) η ( mPa s ) n D V m E ( cm 3 / mol ) Δ η ( mPa s ) Δ G E (J/mol) Δ n D
0.1015 0.0834 0.8368 3.295 1.4123 0.066 −0.720 −236.041 −0.0024
0.1014 0.1867 0.8490 2.605 1.4153 0.061 −1.044 −408.908 −0.0022
0.1016 0.2894 0.8617 2.183 1.4181 0.039 −1.101 −439.286 −0.0022
0.1025 0.3915 0.8748 1.875 1.4211 0.025 −1.046 −411.146 −0.0019
0.1009 0.4918 0.8879 1.658 1.4243 −0.013 −0.909 −322.437 −0.0014
0.1013 0.5960 0.9023 1.472 1.4274 −0.051 −0.724 −205.464 −0.0011
0.1000 0.6974 0.9167 1.331 1.4306 −0.115 −0.507 −60.532 −0.0006
0.0999 0.7984 0.9315 1.201 1.434 −0.151 −0.278 82.433 0.0001
0.2067 0.0703 0.8510 3.463 1.4138 0.062 −0.463 0.500 −0.0044
0.2060 0.1752 0.8649 2.856 1.4174 0.013 −0.698 −65.313 −0.0036
0.2055 0.2801 0.8792 2.410 1.4207 −0.027 −0.772 −74.981 −0.0031
0.2048 0.3854 0.8942 2.102 1.4242 −0.079 −0.708 −2.705 −0.0024
0.2037 0.4901 0.9097 1.860 1.4277 −0.147 −0.579 102.201 −0.0017
0.2023 0.5952 0.9257 1.651 1.4314 −0.208 −0.417 214.427 −0.0008
0.2009 0.6989 0.9420 1.486 1.4351 −0.267 −0.216 354.827 0.0001
0.3128 0.0609 0.8686 3.665 1.4161 0.028 −0.156 256.269 −0.0058
0.3106 0.1720 0.8848 3.083 1.4200 −0.046 −0.347 256.998 −0.0048
0.3107 0.2765 0.9009 2.658 1.4239 −0.099 −0.401 295.196 −0.0037
0.3088 0.3830 0.9179 2.351 1.4280 −0.180 −0.332 401.388 −0.0024
0.3057 0.4898 0.9351 2.074 1.4319 −0.248 −0.234 499.750 −0.0013
0.3026 0.5964 0.9530 1.852 1.436 −0.327 −0.081 626.389 0.0001
0.4193 0.0561 0.8901 3.846 1.4187 −0.008 0.146 491.786 −0.0069
0.4170 0.1659 0.9082 3.328 1.4231 −0.095 0.015 552.277 −0.0054
0.4112 0.2743 0.9258 2.906 1.4274 −0.174 −0.029 626.429 −0.0038
0.4098 0.3851 0.9459 2.566 1.4323 −0.264 0.021 739.573 −0.0019
0.4048 0.4940 0.9652 2.280 1.4366 −0.338 0.116 857.658 −0.0003
0.5243 0.0560 0.9165 3.986 1.4221 −0.048 0.422 691.211 −0.0074
0.5196 0.1690 0.9371 3.498 1.4272 −0.148 0.329 791.397 −0.0052
0.5122 0.2813 0.9575 3.105 1.4321 −0.237 0.325 914.353 −0.0030
0.5068 0.3913 0.9788 2.764 1.4371 −0.321 0.367 1036.467 −0.0008
0.6262 0.0608 0.9487 4.058 1.4264 −0.085 0.643 837.740 −0.0070
0.6195 0.1749 0.9721 3.617 1.4319 −0.195 0.598 973.379 −0.0043
0.6091 0.2894 0.9913 3.189 1.4369 −0.068 0.563 1089.410 −0.0020
0.7231 0.0704 0.9875 4.002 1.4314 −0.101 0.746 892.271 −0.0058
0.7118 0.1866 1.0132 3.616 1.4376 −0.218 0.759 1061.625 −0.0023
0.8146 0.0835 1.0352 3.772 1.4378 −0.139 0.682 811.692 −0.0031
Table 5 Binary coefficients of McAlister,s multibody-interaction equations and standard deviations σ , for kinematic viscosities at 298.15 K.
Three-body Four-body
ν 12 ( mm 2 /s ) ν 2 , 1 ( mm 2 / s ) σ ( mm 2 / s ) ν 1112 ( mm 2 / s ) ν 1122 ( mm 2 / s ) ν 2221 ( mm 2 / s ) σ ( mm 2 / s )
Formamide (1)+N,N-dimethylacetamide (2)
5.0746 1.7067 0.0135 1.49633 1.02288 0.414879 0.0095
N,N-dimethylacetamide (2)+2-methyl-1-butanol (3)
1.4621 1.5566 0.0297 0.203471 0.535476 0.685996 0.0071
Formamide (1)+2-methyl-1-butanol (3)
7.3493 3.6403 0.0355 1.72536 1.67282 1.37031 0.0349

4

4 Conclusions

Excess molar volumes, viscosities, and refractive index deviations for mixtures of formamide (1) + N,N-dimethylacetamide (2) + 2-methyl-1-butanol (3) were obtained from experimental results and fitted by the Redlich–Kister and Cibulka equations. Positive quantities show that dominant factors are physical interactions, and negative values suggested that the main factor in the interactional forces is chemical interactions. McAllister’s multibody-interaction model was used for correlating the kinematic viscosity of binary mixtures with mole fraction. Results showed that McAllister’s four-body equation gave a better result for those three systems.

Acknowledgment

The authors would like to thank the Bu-Ali Sina University for providing the necessary facilities to carry out the research.

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