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ISRN Physical Chemistry
Volume 2013 (2013), Article ID 612837, 13 pages
Thermophysical Properties of Binary Liquid Systems of Ethanoic Acid, Propanoic Acid, and Butanoic Acid with Benzene or Acetophenone
University Institute of Chemical Engineering & Technology, Panjab University, Chandigarh-160 014, India
Received 10 June 2013; Accepted 14 July 2013
Academic Editors: A. Gil-Villegas, B.-T. Liu, and G. Pellicane
Copyright © 2013 R. Ahluwalia et al. This is an open access article distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.
The density (), viscosity (), and surface tension () of binary mixtures of carboxylic acids (CAs) (ethanoic acid (EA), propanoic acid (PA), butanoic acid (BA)) + benzene (BEN) or acetophenone (ACT) have been measured at 298.15, 308.15, and 318.15 K. From the experimental results, excess values of molar volume (), viscosity (), Gibb's free energy for the activation of low (), and surface tension () were evaluated and fitted to a Redlich-Kister type of equation. The parameter “” of Grunberg and Nissan expression has also been calculated. From the sign and magnitude of , , , , and “” values, it is concluded that specific interactions are present in CA+ACT system and these interactions are absent in CA + BEN mixtures. Various viscosity and surface tension models have been used to test the consistency of the data.
Studies on thermophysical properties of binary liquid mixtures containing carboxylic acids are not extensive [1–3]. In view of this, we have undertaken studies on binary mixtures of carboxylic acids (CAs), namely, ethanoic acid (EA), propanoic acid (PA), and butanoic acid (BA) which are self-associated solvents, with a nonpolar solvent benzene (BEN) and polar acetophenone (ACT). These acids exist as cyclic dimers in the pure state. However, trimers also exist which are formed because of strong interactions between ring dimers and monomers [4–6].
The excess properties , , , , and Grunberg and Nissan parameter “” computed from the experimental data (density (), viscosity (), and surface tension) ()) of binary mixtures of carboxylic acids (EA, PA, BA) with benzene and acetophenone have been determined. Benzene interacts with acid through Vander Waal's or London dispersion forces and acetophenone forms chemical aggregates with acid through hydrogen bonding. The results are used to theoretically justify the validity of various viscosity and surface tension models. The main thrust of the investigation is to correlate the experimental data in terms of the interacting components of the mixtures and to stress the factors affecting these interactions.
2. Experimental Section
Ethanoic acid, propanoic acid, butanoic acid, benzene, and acetophenone were purified by the standard methods described in the literature . Ethanoic acid (BDH, 99% assay) was washed with a calculated amount of acetic anhydride for about 10 h and was subjected to fractional distillation. Propanoic acid and butanoic acid (E. Merck, 99% assay) were dried over anhydrous sodium sulfate for two days and the samples were distilled over potassium permanganate. Benzene (E. Merck, 98.4% assay) was dried by keeping over anhydrous calcium chloride for six to eight hours and then fractionally distilled. Acetophenone (Merck, 99% assay) was also dried by keeping it over anhydrous calcium chloride for two days and distilled at reduced pressure. The purity of all the components was checked by comparing their experimental densities with that of the literature values . For each run, a fresh liquid mixture was prepared on a mass basis (precision of 1 × 10−5 g). The purity of each component with respect to the corresponding literature value is recorded in Table 1.
Densities () of the pure components and their mixtures were measured with a density meter (AP, DMA-48) calibrated at each temperature with ethanol and 1,2-dichloroethane. The densities were measured with an accuracy of 1 × 10−1 kg·m−3.
Viscosities () were determined using a modified Ubbelohde viscometer . At each temperature, the viscometer was calibrated against the known viscosities of benzene and carbon tetrachloride . The viscometer constants at each temperature were determined from the following where and are the temperature-dependent constants. At a particular temperature, an average value of the five consistently measured efflux times and the densities were used to calculate viscosity. The accuracy of the viscosity measurements is in the order of ±0.0013 mPa·s.
Surface tension () of the pure components and their mixtures was determined by the differential capillary rise method , using (2). The difference in the liquid levels in two capillaries was measured with a cathetometer reading to 0.05 mm with a vernier constant of 0.01 mm. The surface tension values are accurate to within ±0.02 mN·m−1. Consider where , , , and are the heights of liquids in capillaries 1 and 2, and are the radii of the capillaries, and is the acceleration due to gravity (=9.80 m s−2), respectively. The constants , , and of (2) were determined by measuring the for two test liquids (benzene, ethyl ethanoate) of known and at 298.15 K. The constant was separately determined by noting the height of the test liquid in one of the capillaries. The corresponding radius of the capillary was determined from the measured weight of the mercury column of known length. The constants (, , and ) were assumed to be temperature independent. For each mixture of the respective systems and pure components, was recorded at three different temperatures over the entire composition range.
All the measurements were made at a constant temperature that was maintained with the help of a circulating type ultra cryostat (type MK 70, MLW, Germany) within ±0.02°C.
Experimental densities of pure components and their literature values at 298.15 K are given in Table 1. Experimental values of , , and were fitted to (3) using nonlinear regression technique . The computed coefficients of (3) and standard errors are listed in Table 3.
Equation (3) fits the experimental data within the average uncertainty in the temperature range of 298.15 K–318.15 K and
Based on the regular solution theory , Grunberg and Nissan proposed an empirical expression for viscosities of real mixtures: where and refer to the dynamic viscosities of the pure liquid components 1 and 2, respectively, and are the mole fractions of components 1 and 2, respectively, in the mixture, and “” is a parameter which denotes the measure of strength of interaction between the two components. The values of “” are reported in Table 2.
From the experimental data, excess molar properties, namely; , , , and were calculated  from the following expressions: where and are the molecular weight and density of the carboxylic acids. The same symbols with subscript 2 refer to BEN or ACT, respectively. , , and are the molar volumes and , , and are the surface tension of the 1st, and 2nd components and mixture, respectively.
Graphical representations of , , , and as a function of the mole fraction () of CA are given in Figures 1–8, respectively. Each of these functions, , , and , has been fitted to the Redlich-Kister relation : where , , and are adjustable parameters and have been evaluated by the method of least squares. The value of these parameters along with standard deviation is reported in Table 4. Consider where is the total number of experimental points.
Stevanovic et al.  have recently compared the available correlation models for liquid mixture viscosities of organic compounds. Amongst the available correlations for predicting the binary liquid mixture viscosity, the present experimental binary viscosity data was fitted to the following five correlations.
McAllister's  model: where and are interaction parameters.
Heric  model: where is a deviation function given by Here, and are interaction parameters.
Auslander  model: where , , and are parameters representing binary interactions.
Teja and Rice  model: where for or 2 component or the mixture must be evaluated at a temperature and at a temperature . is the system temperature and is an adjustable interaction parameter having a value unity. The interaction parameter has been shown to be independent of temperature and composition [19, 20]. The subscript indicates a reduced quantity.
Kubendran et al. model : where , , and are binary interaction constants.
The observed data on surface tension of binary mixtures was fitted to the following models available in the literature.
Zihao and Jufu model : where and are interaction parameters.
Rice and Teja model : where for or 2 component or the mixture
Here, is to be evaluated at a temperature = and at a temperature = . is the system temperature and is an adjustable interaction parameter having a value around unity. The interaction parameter has been shown to be independent of temperature and composition [19, 20]. The subscript indicates a reduced quantity.
Empirical two-constant model : where and are binary interaction parameters.
The values of as illustrated in Figures 1 and 2 are positive for the entire concentration range at all the three temperatures for the systems EA + BEN, PA + BEN, and BA + BEN and negative for the remaining three systems. About 5% more negative or less positive values at higher temperatures for all the systems may be due to increased population of acid monomers to enter into the hetero-intermolecular interactions.
The positive and negative values may be explained by considering the following three steps equilibria accompanying the mixing process as proposed by Lark and Banipal : where and denote a dimer and a monomer of the acid under question. The first process is accompanied with a large volume increase in the right direction; the second is isochoric; that is, the volume of the dimer is assumed to be equal to twice the value of the monomer [4, 5]; the third step is accompanied with large contraction in case of ACT and expansion in case of BEN. So the addition of ACT or BEN to anyone of the acids first creates monomers by the first two steps resulting in expansion. In the third step, stronger heteromolecular dipole-dipole interactions result in the observed negative in case of CA + ACT and positive values in the case of CA + BEN system due to induced dipole-dipole interactions. Therefore, the third step is accompanied with contraction in volume in case of ACT and expansion in case of BEN.
The values of EA, PA, and BA are 4.76, 4.88, and 4.82, respectively. It is expected that the order of dimerization constants of various acids would increase in the same order. The increasing dimerization constant would lead to a smaller number of available monomers and thus to a smaller volume increase as described by (22).
However, the observed order of for the CA + BEN system is as follows: BA > PA > EA (Table 6). This shows that in case of BEN there are strong acid-solvent interactions which govern the magnitude and sign of , which increases as the inductive effect of alkyl chain of the acid as is also observed by Lark et al. . Similar results were also obtained by Venkateswarlu and Raman  as the positive excess volumes of 1,2-dichloroethane and 1,2-dibromoethane with three acids observe the following order: BA > PA > EA, which is the same as discussed above; that is, the increase in chain length of acid contributes to the decrease in excess volume. The large negative values in the case of CA + ACT mixture arise due to depolymerization of acid accompanied with strong hydrogen-bonded heterocomplex formation. However, in CA + ACT system, the values follow the order PA > BA > EA as was also observed by Lark et al.  in CA + MEOH system.
The data presented in Figures 3 and 4 reveal that excess viscosity is positive for the systems EA + ACT, PA + ACT, and BA + ACT, and is negative for the systems EA + BEN, PA + BEN, and BA + BEN at 298.15 K. The algebraic positive values of may be represented in the following order: PA + ACT > EA + ACT > BA + ACT > BA + BEN > PA + BEN > EA + BEN. The sign and magnitude of depend on the combined effect of the factors such as molecular size, shape, and intermolecular forces. The positive value of for the CA + ACT system suggests that the viscosity of the mixture is higher than that of the pure components and hence the fluidity of the mixture is low. This indicates the presence of a specific interaction such as the formation of charge-transfer complex between unlike molecules. The negative value of in the systems EA + BEN, PA + BEN, and BA + BEN suggests the mutual loss of a specific interaction in like molecules that outweigh the specific interaction between unlike molecules. The positive values of increase with the increase in temperature in all these systems. The values almost observe the similar trend as observed by as shown in Figures 5 and 6.
The variation of Grunberg and Nissan parameter “” with composition of a particular mixture is not large. The values of “” are negative for CA + BEN system and positive for CA + ACT system for most of the concentration range. The positive values of “” for CA + ACT system show that CA forms an intermolecular complex with ACT in the liquid phase. The values of “” increase with the increase in temperature in all the systems showing that the interactions between the components increase with the increase in temperature. Even the negative values of “” for CA + BEN system change their sign from negative to positive with the increase in temperature from 298.15 to 318.15 K.
According to Hildebrand , free volume is necessary for flow and then shrinkage on mixing (which would reduce the free volume) would be associated with increase in viscosity of the system. If is defined as , where is the experimental viscosity of the mixture and is the ideal viscosity, calculated using then this quantity could be related to free volume of the solution according to Stairs  by the following equation:
According to (26), a plot of versus should be linear. However, when is plotted against , a nonlinear plot was obtained in the present study. However, when is plotted against , a single straight line with a nonzero intercept was obtained in Figure 9. This type of result is not unexpected, because the expression for takes into account both viscosity and volume. Also, in all these systems, positive and negative and vice versa have been observed for most of the concentration range. This behaviour was also observed by Palepu et al.  in binary mixtures o-chlorophenol with substituted anilines.
From the literature, no clear cut theoretical basis has been proposed for the prediction of nonideal behaviour of the binary mixtures in terms of their values. However, recently, Papaioannou and Panayiotou  have correlated the sign of values with values and the deviations from Raoult's law. Their observation reveals the following.(1)Corresponding to the positive enthalpies of mixing , positive volume of mixing and positive deviations from Raoult's law, values, have been observed to be negative. (2)Corresponding to the negative enthalpies of mixing , negative volume of mixing and negative deviations from Raoult's law, values have, been observed to be positive. As shown in Figures 7 and 8, the excess surface tension () values are negative for CA + BEN system and are positive for CA + ACT system. The positive values of excess surface tension () increase with the rise in temperature in all systems. The negative value of in CA + BEN system is due to the predominance of the following factors: homopolymer complex formation and the tendency of the component with lower surface tension to be adsorbed at the interface. But in CA + ACT system complex formed are block copolymer and also dipole-dipole interactions between carboxylic functional group of CA and carbonyl group of ACT in the bulk phase rather than in the interface.
The interaction parameters of various models used can change with temperature but not with composition, but the interaction parameter in Rice and Teja and Teja and Rice models, based on the theory of corresponding states, has been shown to be independent of temperature and composition [19, 20]. It is observed that the models of McAllister, Auslander, and Teja and Rice fit the experimental viscosity data very well as compared to the Heric and Krishnan and Laddha models. Surface tension data is well predicted by the empirical two-parameter model  as well as by Rice and Teja model. The Zihao & Jufu model, based on the work of Hildebrand & Scott , also predicts satisfactory results for the systems studied.
The author (R. Ahluwalia) is grateful to CSIR, India, for the award of Senior Research Fellowship to carry out this research work successfully.
- R. Ahluwalia, R. K. Wanchoo, and J. L. Vashisht, “Some physical properties of binary liquid systems: (ethanoic acid or propanoic acid or butanoic acid + ethanenitrile),” Physics and Chemistry of Liquids, vol. 29, pp. 87–96, 1995.
- B. S. Lark and T. S. Banipal, “Excess volumes and excess enthalpies of acetic and its methyl substituted acids + acetonitrile,” Canadian Journal of Chemistry, vol. 63, pp. 3269–3275, 1985.
- M. C. S. Subha and S. Brahmaji Rao, “Thermodynamic properties of binary acid-base mixtures,” Journal of Chemical and Engineering Data, vol. 33, no. 2, pp. 104–106, 1988.
- H. E. Affsprung, G. H. Findenegg, and F. Kohler, “The volumetric and dielectric behaviour of acetic acid in mixtures with nonpolar liquids,” Journal of the Chemical Society A, pp. 1364–1370, 1968.
- G. Bolat, D. Sutiman, and G. Lisa, “Experimental densities of binary mixtures: acetic acid with benzene at several temperatures,” AIP Conference Proceedings, vol. 1332, no. 1, p. 270, 2011.
- R. K. Wanchoo, J. Narayan, G. K. Raina, and V. K. Rattan, “Excess properties of (2-propanal + ethylacetate or benzene) binary liquid mixture,” Chemical Engineering Communications, vol. 81, no. 1, pp. 145–156, 1989.
- J. A. Riddick and W. B. Bunger, Techniques of Chemistry, vol. II, Wiley-Interscience, New York, NY, USA, 1970.
- A. Weissberger, Techniques of Organic Chemistry, Interscience, New York, NY, USA, 3rd edition, 1965.
- B. P. Levitt, Findlay’s Practical Physical Chemistry, Longman, London, UK, 9th edition, 1973.
- G. C. Franchini, A. Marchetti, M. Tagliazucchi, L. Tassi, and G. Tosi, “Ethane-1,2-diol-2-methoxyethanol solvent system. Dependence of the relative permittivity and refractive index on the temperature and composition of the binary mixture,” Journal of the Chemical Society, Faraday Transactions, vol. 87, no. 16, pp. 2583–2588, 1991.
- L. Grunberg and A. H. Nissan, “Mixture law for viscosity,” Nature, vol. 164, no. 4175, pp. 799–800, 1949.
- R. C. Reid, J. M. Prausnitz, and T. K. Sherwood, The Properties of Gases and Liquids, McGraw Hill, New York, NY, USA, 3rd edition, 1958.
- O. Redlich and A. T. Kister, “Algebraic representation of thermodynamic properties and the classification of solutions,” Industrial & Engineering Chemistry, vol. 40, pp. 345–348, 1948.
- A. B. K. Stevanovic, G. M. Babic, M. Lj Kijevcanin, S. P. Serbanoviv, and D. K. Grozdanic, “Correlation of the liquid mixture viscosities,” Journal of the Serbian Chemical Society, vol. 77, no. 8, pp. 1083–1089, 2012.
- R. L. McAllister, “The viscosity of liquid mixtures,” AIChE Journal, vol. 6, pp. 427–431, 1960.
- E. L. Heric, “On the viscosity of ternary mixtures,” Journal of Chemical and Engineering Data, vol. 11, no. 1, pp. 66–68, 1966.
- G. Auslander, “The properties of mixtures: part I,” British Chemical Engineering, vol. 9, pp. 610–618, 1964.
- A. S. Teja and P. Rice, “Generalized corresponding states method for the viscosities of liquid mixtures,” Industrial and Engineering Chemistry Fundamentals, vol. 20, no. 1, pp. 77–81, 1981.
- A. S. Teja and P. Rice, “The measurement and prediction of the viscosities of some binary liquid mixtures containing n-hexane,” Chemical Engineering Science, vol. 36, no. 1, pp. 7–10, 1981.
- A. S. Teja and P. Rice, “A generalized corresponding states method for the prediction of the thermal conductivity of liquids and liquid mixtures,” Chemical Engineering Science, vol. 36, no. 2, pp. 417–422, 1981.
- T. R. Kubendran, S. P. Palaniappan, M. R. V. Krishnan, and G. S. Laddha, “Viscosities of binary and ternary liquid mixtures involving acetone carbon-tetrachloride and benzene,” Indian Journal of Technology, vol. 24, no. 1, pp. 22–25, 1986.
- W. Zihao and F. Jufu, “Surface Tension of Binary liquid mixtures,” in Proceedings of the Joint Meeting of Chemical Industry and Engineering Society of China and AIChE, p. 143, Beijing, China, September 1982.
- P. Rice and A. S. Teja, “A generalized corresponding-states method for the prediction of surface tension of pure liquids and liquid mixtures,” Journal of Colloid and Interface Science, vol. 86, no. 1, pp. 158–163, 1982.
- R. K. Wanchoo and J. Narayan, “Some physical properties of binary liquid systems: (2-butanone+n-propionic acid or n-butyric acid),” Physics and Chemistry of Liquids, vol. 27, no. 3, pp. 159–167, 1994.
- B. S. Lark, S. Singh, S. K. Aggarwal, and S. Makkar, “Excess volumes of n-butyric acid + various polar and nonpolar solvents,” Journal of Chemical and Engineering Data, vol. 30, no. 4, pp. 467–469, 1985.
- P. Venkateswarlu and G. K. Raman, “Excess volumes of ethanoic, propanoic, and butanoic acids with 1,2-dichloroethane and 1,2-dibromoethane,” Journal of Chemical and Engineering Data, vol. 30, no. 2, pp. 180–181, 1985.
- J. H. Hildebrand, “Motions of molecules in liquids: viscosity and diffusivity,” Science, vol. 174, no. 4008, pp. 490–493, 1971.
- R. A. Stairs, “Viscosity of binary solutions of polar liquids,” Canadian Journal of Chemistry, vol. 58, pp. 296–301, 1980.
- R. Palepu, J. Oliver, and D. Campbell, “Thermodynamic and transport properties of o-chlorophenol with aniline and N-alkylanilines,” Journal of Chemical and Engineering Data, vol. 30, no. 3, pp. 355–360, 1985.
- D. Papaioannou and C. G. Panayiotou, “Surface tensions and relative adsorptions in hydrogen-bonded systems,” Journal of Chemical and Engineering Data, vol. 39, no. 3, pp. 457–462, 1994.
- J. H. Hildebrand and R. L. Scott, The Solubility of Nonelectrolytes, Dover, New York, NY, USA, 3rd edition, 1964.