A Volumetric and Viscosity Study for the Binary Mixtures
of Acetaldehyde with
n
-butanol over the Entire Range of
All Compositions at 298.15, 308.15 and 318.15 K.
S. B. Maulage, R. G. Machale, S.V. Gayakwad and S. D. Naikwade
Mrs. K.S.K. Arts, Science & Commerce College, Beed. (M.S.) INDIA.
email:[email protected].
(Received on: February 21, Accepted: February 28, 2017)
ABSTRACT
Densities and viscosities of the binary mixtures of Acetaldehyde with n -butanol over the entire range of all compositions have been measured as a function of mole fraction at 298.15, 308.15 and 318.15 K. From this experimental data viscosity deviations (Δŋ), molar volumes Vm, excess molar volumes VE and excess free energies of activation of viscous flow ΔG*E have been determined. Viscosity deviations, excess molar volumes and excess free energies of activation of viscous flow were calculated and correlated Redlich-Kister polynomial equation. The molecular interactions existing between the components were also discussed.
Keywords: Density, Viscosity, Viscosity deviation, Excess molar volume, Binary system, Acetaldehyde.
INTRODUCTION
Viscosity and volumetric study of binary systems of Acetaldehyde with n-butanol at 298.15, 308.15 and 318.15 K have been taken into consideration for the present paper. Study of effect of temperature on the viscosity of a liquid is important and has been studied by some researchers1. However, study of the effect of temperature on viscosity and density of binary
liquid mixtures of Acetaldehyde with n-butanol is rarely reported. Therefore, the main objective of this study was to produce the data on the effect of temperature on the viscosity of binary liquid mixtures. Furthermore, the volumetric studies of binary liquid mixtures and their analysis in terms of interpretative models constitute a very interesting subject2. The
S. B. Maulage, et al., J. Chem. & Cheml. Sci. Vol.7(2), 164-169 (2017)
consisting of aldehydes and alcohols are of great importance in the field of industries such as in Petrochemical, Pharmaceutical and Dye8,9. A thorough knowledge of transport properties of
non-aqueous solutions is essential in many chemical and industrial applications10. The studies
of excess properties such as deviation in viscosity, excess molar volume, excess Gibbs free energy of activation of viscous flow molecular interactions of binary mixtures are useful in understanding the nature of intermolecular interactions between two liquids11-12. Binary liquid
mixtures due to their unusual behavior have attracted considerable attention due to their importance from both theoretical and practical point of view because these mixtures are used in titration, calorimetry and reaction calorimetry, among other uses14.
In this present paper, density (ρ) and viscosity (ŋ) of binary mixtures of Acetaldehyde and n-butanol are reported at various temperatures 298.15, 308.15 and 318.15 K. Deviation in viscosity (Δŋ), molar volume (Vm), excess molar volume (VE) and excess Gibbs free energy
of activation of viscous flow (ΔG*E) have been calculated from the density ((ρ), and viscosity
(ŋ), data. Calculated deviation in viscosity and excess functions were fitted to the Redlich-Kister polynomial equation and the results analyzed in terms of molecular interactions.
MATERIALS AND METHODOLOGY
The chemicals such as Acetaldehyde and methanol, ethanol n-propanol and n-butanol used for the current investigation were obtained from SD fine chemicals India. All chemicals used were of analytical grade (AR) of minimum purity of 99.9 %. The purities of the chemicals were cross checked by density determination at different temperatures. The densities of pure components and binary mixtures were measured by using a single-arm pycometer which was calibrated at the working temperatures with doubly distilled water. The sensitivity of the pycnometer corresponded to a precision in density of 1x10–3 gm cm–3. The binary liquid mixtures of different known concentrations were prepared in stopper measuring flasks. The
weight of the sample was measured using electronic digital balance with an accuracy of ± 0.0001 gm. An Ubbelohde viscometer (of 20 ml capacity) was used in the viscosity
measurement and efflux time was determined using a digital clock to within ± 0.01 Sec. The experimental temperature was controlled using kinematic viscosity bath with an accuracy of ± 0.10K.
RESULTS AND DISCUSSION
The density, viscosity of different binary mixtures of Acetaldehyde with n-butanol at 298.15, 308.15 and 318.15 K and calculated data of deviation in viscosity (Δŋ), molar volume (Vm), excess molar volume (VE) and excess Gibbs free energy of activation of viscous flow
Table-1: The density, viscosity, deviation in viscosity (Δŋ), excess molar volume (VE) & excess
Gibbs free energy of activation of viscous flow (ΔG*E) at 298.15 K.
X1 ρ ŋ Δŋ Vm VE ΔG*E
0 0.8058 2.5223 0 41.2368 0 2101.85 0.0976 0.8036 2.4509 0.4896 42.6376 -0.0103 2776.46 0.1958 0.8014 2.3695 0.8095 43.907 -0.0151 3070.89 0.2837 0.7992 2.3068 1.0515 45.4036 -0.0167 3230.958 0.3937 0.7970 2.2349 1.1875 47.3152 -0.0184 3288.958 0.4934 0.7948 2.1623 1.1867 48.8649 -0.0199 3285.053 0.5937 0.7926 2.0891 1.1489 50.6109 -0.0192 3234.051 0.6944 0.7904 2.0177 1.0412 52.4864 -0.0189 2987.192 0.7957 0.7882 1.9456 0.8462 54.6817 -0.0163 2804.536 0.8976 0.7860 1.8742 0.4328 56.9914 -0.0102 2370.192 1 0.7851 1.8081 0 59.5316 0 1689.798
Table: 2: The density, viscosity, deviation in viscosity (Δŋ), excess molar volume (VE) and excess
Gibbs free energy of activation of viscous flow (ΔG*E) at 308.15 K.
X1 ρ ŋ Δŋ Vm VE ΔG*E
0 0.7981 1.9488 0 42.1333 0 2219.175 0.0976 0.7957 1.9232 0.3264 43.5341 -0.0124 2981.785 0.1958 0.7932 1.8962 0.6839 44.8035 -0.0172 3173.215 0.2837 0.7908 1.8689 0.9259 46.3001 -0.0188 3334.283 0.3937 0.7884 1.8427 1.1019 48.2117 -0.0205 3357.283 0.4934 0.7859 1.8158 1.0611 49.7614 -0.022 3363.378 0.5937 0.7835 1.7876 1.0233 51.5074 -0.0226 3392.376 0.6944 0.7811 1.7611 0.9156 53.3829 -0.021 3155.517 0.7957 0.7786 1.7329 0.7206 55.5782 -0.0184 2962.861 0.8976 0.7762 1.7066 0.3072 57.8879 -0.0123 2428.517 1 0.7735 1.6858 0 60.4281 0 1758.123
Table: 3: The density, viscosity, deviation in viscosity (Δŋ), excess molar volume (VE) and excess
Gibbs free energy of activation of viscous flow (ΔG*E) at 318.15 K.
X1 ρ ŋ Δŋ Vm VE ΔG*E
0 0.7906 1.4879 0 43.0965 0 2332.16 0.0976 0.7871 1.4935 0.1794 44.4973 -0.0155 3094.77 0.1958 0.7836 1.4996 0.5369 45.7667 -0.0203 3311.236 0.2837 0.7801 1.5058 0.7789 47.2633 -0.0228 3447.268 0.3937 0.7767 1.5127 0.9116 49.1749 -0.0244 3470.268 0.4934 0.7732 1.5186 0.9141 50.7246 -0.0259 3498.325 0.5937 0.7697 1.5249 0.8763 52.4706 -0.0252 3505.361 0.6944 0.7662 1.5311 0.7686 54.3461 -0.0241 3354.235 0.7957 0.7627 1.5371 0.5736 56.5414 -0.0215 3075.846 0.8976 0.7593 1.5421 0.1702 58.8511 -0.0154 2541.502 1 0.7558 1.5472 0 61.3913 0 1871.108
S. B. Maulage, et al., J. Chem. & Cheml. Sci. Vol.7(2), 164-169 (2017)
viscous flow have been evaluated from experimental density and viscosity using equations 1 and 2 respectively.
(1)
(2)
Where, let x1and x2be the mole fractions calculated from mass fractions. M1and M2are molar
masses, ρ1 and ρ2 are densities, ŋ1 and ŋ2 are the viscosities of pure components 1 and 2
respectively. ρmand ŋmare the density and viscosity of the mixture.
The excess Gibbs free energy of activation of viscous flow was obtained from equation 3.
(3)
Where R is the universal constant of gases, T is the absolute temperature, V1 and V2 are the
molar volumes of component 1 and 2, x1and x2represents the mole fraction of component 1
and 2. Vm is obtained from equation 4 below.
(4)
Where ŋ1,ŋ2and ŋmare the viscosity of component 1 and 2 and mixture respectively.
Figure-1: The plot of deviation in viscosity against mole fraction at 298.15, 308.15 and 318.15 K for binary mixtures of Acetaldehyde with n-butanol.
Figure-2: The plots of excess molar volumes against mole fraction for binary mixtures of Acetaldehyde with
n-butanol at 298.15, 308.15 and 318.15 K.
The variation of excess volumes with the mole fraction (X1) of Acetaldehyde and
n-butanol at (303.15, 308.15 and 313.15) K are represented in figures-2. The excess molar volume values of the mixtures are negative and decreases when temperature increases. This shows that the excess molar volumes are always negative for all the studied temperatures. Treszczanowicz et al.,19 and Roux and Desnoyers20 suggested that VE is the resultant
contribution from several opposing effects.
CONCLUSION
The density, viscosity, deviation in viscosity, excess molar volume and excess Gibbs free energy of activation of viscous flow for the binary systems of Acetaldehyde with n -butanol at 298.15, 308.15 and 318.15 K has been reported. The deviation in viscosity of the binary systems of Acetaldehyde with n-butanol are found to be negative and decreases with temperature while excess molar volumes are positive for all binary systems. There is intermolecular interaction among the components of the binary mixtures leading to possible hydrogen bond formation of the type Ȫ---H-O between unlike molecules confirming intermolecular hydrogen bond formation between Acetaldehyde and n- butanol mixtures. Excess molar volumes (VE) and the viscosity deviations (Δŋ) were used to predict the
S. B. Maulage, et al., J. Chem. & Cheml. Sci. Vol.7(2), 164-169 (2017)
REFERENCES
1. Ewing, M.B., Levian,B.J., Marsh, K.N. Journal of Chemical Thermodynamics, 2, 689 – 691 (1970).
2. Lange’s Handbook of Chemistry 10th edition, 1525 – 1528.
3. B. R. Kumar, B. Satyanarayana, S. A. Banu, K. A. Jyoti, T. S. Jyostna, N. Satyanarayana.
Ind. J. Pure & Appl. Phys., 47, 511 (2009).
4. S. Parveen, M. Yasmin, M. Gupta, J. P. Shukla. Int. J. Thermodyn., 13(2), 59 (2010). 5. S. Singh, B. P. S. Sethi, R. C. Katyal, V. K. Rattan. J. Chem. Eng. Data., 49, 1373 (2004). 6. R. A. Clara, A. C. G. Marigliano, V. V. Campos, H. N. Solimo. Fluid Phase Equilib., 293,
151 (2010).
7. B. Gonzalez, N. Calvar, E. Gomez, A. Dominguez. J. Chem. Thermodyn., 39, 1578 (2007). 8. Suryanarayana C. V., J. Acoust Soc India, 13, 9 (1983).
9. Fletcher A., J. Phys Chem., 73, 2217 (1969).
10. B. Sathyanarayana, B. Ranjithkumar, T. S. Jyostna, N. Satyanarayana. J. Chem. Thermodyn., 39, 16 (2007).
11. Fedeles, O. Ciocirlan, O. Iulian. U. P. B. Sci. Bull. B., 71(4), 99 (2009).
12. M. L. J. Kijevcanin, V. Z. Kostic, I. R. Radovic, B. D. Djordjevic, S. P. Serbanovic. Chem. Ind. Chem Eng.,14(4), 223 (2008).
13. S. S. Patil, S. R. Mirgane. Rasayan J. Chem., 4(2), 445 (2011). 14. O. Redlich, A. T. Kister. Ind. Eng. Chem., 40(2), 345 (1948). 15. S. C. Bhatia, R. Rani, R. Bhatia. J. Mol. Liq., 159, 132 (2011). 16. S. L. Oswal, H. S. Desai. Fluid Phase Equilib., 161, 191 (1999).
17. A. G. Peshwe, B. R. Arbad, S. P. Pachaling. Int. J. Chem. Sci., 7(3), 1505 (2009). 18. V. Serheyev. Chem. Chem. Tech., 5(3), 241 (2011).
19. Roux, A., Desnoyers, J.: Association models for alcohol – water mixtures. Indian Acad. Proc., Chem. Soc. 98, 435-439 (1978).