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3232

Study Of Thermodynamic And Volumetric

Properties In Some Liquid Mixtures

A.Nagarjuna, G.V.Gangadhara rao, K.Govinda rao, T.Kalimulla

Abstract Densities and Speed of sound for the binary liquid mixtures of cyclohexanone with mole fractions of benzoates – Ethyl-4-hydroxy benzoate and

p-Methoxy benzoic acid have been estimated with the standard technique at 303.15, 308.15 and 313.15K. From these experimental results, different thermo-dynamic parameters such as enthalpy (H), adiabatic compressibility (βs), free length (Lf) ,molar volume (Vm) and their excess properties were determined. These excess parameters have been fitted to the Redlich–Kister type polynomial equation using the least square method. Further estimate the partial molar volumes (V ֿm, 1 ,V ֿm,2) from the results of Vm

E

.The intra/inter molecular interactions presence in the liquid mixtures was perceived by studying the deviations obtained in the excess properties.

Index

terms:

Densities, excess parameters, molecular interactions, partial molar volumes, Redlich–Kister type polynomial, speed of sound, standard

technique

——————————  ——————————

1

I

NTRODUCTION

Physico-chemical properties of fluid mixtures are important for understanding their thermo-physical behavior of liquid mixtures .This paper is used to understand the presence of

charge transfer, dipole-dipole and dipole-induced

interactions also hydrogen bonding in the mixture. Ethyl-4-hydroxy benzoate (C9 H10 O3) is the ethyl ester of p-hydroxy

benzoic acid. It is mainly used as antiseptics in cosmetics, food and medicine. It is also can be used as feed preservatives and antiseptic for bacteria. p -Methoxy benzoic acid (C8H8O3) has antiseptic property and it is

soluble in water, alcohols, and ethyl acetate because it is available in powder form. p- Methoxy benzoic acid has a boiling of about 280 o C and a melting of 184o C; it is a

metabolite of aniracetam. Ketones are trigonal

planar around the ketonic carbon, with C−C−O and C−C−C bond angles of approximately 120°.One of the most important ketone is cyclohexanone (C6H10O),it is a liquid

with a sweetish odour. Because of its low boiling point it is one of the few organic compounds that are infinitely soluble in water and it also dissolves many organic compounds. For this reason it is one of the most important industrial solvents being used as paints, varnishes, coatings, and nail-polish remover‘s e.t.c.. In the present study the experimental results of density and speed of sound were used to calculate various excess parameters also fit them into RK polynomial equation for the binary system of Cyclohexanone with benzoates at entire mole fraction range. Similar kinds of results were obtained by earlier workers carried out variety of research investigations on liquid mixtures. [1],[2],[3],[4],[5],[6],[7],[8],[9],[10],[30]

2

P

ROCEDURE FOR

P

APER

S

UBMISSION

2.1 Materials and Methods

The purity analysis of substances were reported in table 01.The binary liquid mixtures were prepared just before start the experiment for different samples with the help of mass variation. The uncertainty in the final mole fraction was estimated to be less than ±0.0001. p - Methoxy benzoic acid and ethyl-4-hydroxy benzoate can be accessible in powder type and they were soluble in water with mixture of 530 mg/lr and 885 mg/lr at room temperature. The speed of sound was measured at

303.15K, 30815K and 313.15K using ultrasonic

interferometer (M-81S, M/s Mittal Enterprises, New Delhi, India) operating at a fixed frequency of 2 MHz with an accuracy of ±0.1m/s for the binary systems of Cyclohexanone with benzoates. The uncertainty in the speed of sound was found to be ±0.76 m/s. The densities of the pure components and their multi components were measured with 10 ml specific gravity bottle

Table 01: Purity analysis of chemicals studied

inhigh accurate digital electronic balance (Baijnath Premnath SF 400A, Kanpur, U.P) with an accuracy of ±0.00001 g. The uncertainty in the measured density was ±0.003 kg/m 3. The flow time has been measured after the attainment of bath temperature by each pure compound and mixture. The precision of experimentally measured values of density and speed of sound data was compared with their literature values and uncertainties are shown in table 03

3. THEORY

The values of excess properties with mole fraction for the studied binary system at three different temperatures have been calculated by using equations (1) to (5) and they are presented in the figure 1 to 4. Excess isentropic compressibility

Chemical name

CAS numbe r

Source

Initial Mole fractio n

Final

Mole fracti on

Analy sis metho d

Ethyl-4- Hydroxy benzoate

120-47-8

Hi Media

Laboratories

Pvt. Ltd.

Mumbai, India

Hi Media

Laboratories

Pvt. Ltd.

Mumbai, India

0.99 0.995 Vacuum drying

P-Methoxy benzoic acid

100-09-4 0.98 0.992

Vacuum drying

Gas liquid chromat ography

Cyclohexa none

108-94-1

TCI Co. Ltd,

(2)

3233

Ks E

= Ks - Ks id

Ks =

Kg

-1

ms -2 (1)

Where Ks

id

is the ideal isentropic compressibility relation recommended by Benson & Kiyohara[31].

Ks id

= ∑ {

( )

} - T (∑ ) (

∑ )

(2)

In which Ks i o

, Vio, ὰi o

, Cp,j o

are the isentropic compressibility, molar volume, isobaric thermal expansion coefficient and molar isobaric heat capacity of pure component i, T represents temperature and ɸi is volume fraction

Excess molar volume Vm

E= X

1M1+X2M2/ρ – (X1M1/ρ1 + X2M2/ρ2)

(3)

Excess free length Lf E

=Lf - KT (Ks id

)1/2 Lf= KT√ A o

(4)

KT represent a temperature dependent constant where

KT = (91.368 + 0.3565 T) * 10 - 8

Where R represents gas constant, T is absolute temperature

Excess Enthalpy HE = H-(X1H1 + X2H2) H = πi . V J. mol - 1

(5)

Where internal pressure πi = bRT *

+1/2

*

+ Pa

Where H represents the calculated value of enthalpy, Vm be the molar volume, ρ represent obtained density for the mixture and H1, H2 represents enthalpy X1, X2 represents

mole fractions ρ1, ρ2 be the densities,Vm1, Vm2 represent

molar volumes and M1, M2 represent molecular weights of

pure components 1 and 2, respectively. b stands for the cubic packing factor which is assumed to binary liquids ,K is temperature independent constant, R is the gas constant and T is the absolute temperature of binary mixtures.

The excess values were fitted to a Redlich- Kister type polynomial [22] with nonlinear Least – squares method

YE = X1 (1-X1) Σ

n

i=1 Ai(2 X1 – 1)

i-1

(6)

Standard deviation (σ) = [Σn

i=1(Y E

exp- Y E

cal)/N-m] 1/2

(7)

Where N and m are the numbers of data points and of adjustable parameters, respectively

The partial molar volumes for all the binary systems can be calculated using the formulae

V ֿm,1 =V E

m +V *

1 +X2(ծV E

m/ծX)P,T

(8)

V ֿm,2 = V E

m +V *

2 +X1(ծV E

m/ծX)P,T

(9)

The values of infinite dilution of partial and excess partial molar volumes for the binary system (VE,∞m,1,V

E,∞

m,2) can

be calculated by the following relations. VE,∞m,1= A0+A1+A2+A3+ - - - = V

∞ m,1 –V

* 1

(10)

VE,∞m,2= A0-A1+A2-A3+ - - - = V∞m,2 –V *

2

(11)

V ֿm,1 ,V ֿm,2 bePartial molar volumes, V *

1 , V *

2 are Molar

volumes of pure compounds and the coefficients A0,A1,A2

were calculated with RK polynomial equation

Table 2 List of symbols/Notations

S.NO SYMBOL/ NOTATION DESCRIPTION UNIT

1. X1, X2 Mole fractions of a mixture No units

2. ρ Density of a mixture Kg/ m3

3. ρ1,ρ2, Densities of pure components kg /m

3

4. U (ρ) The uncertainty in the measured

density kg /m

3

5. Lf Free length of a mixture A0

6. Lf E

Excess free length of a mixture A0

7. U Speed of sound of a mixture m/s

8. U0 Speed of sound of Benzyl benzoate m/s

9. U (u) The uncertainty in the speed of sound

was ±0.9 m/s

10. H Enthalpy of a mixture J/mol

11. H1,H2 Enthalpy of pure liquids J/mol

12. KT Temperature dependent constant Kelvin

13. M1, M2 Molar mass of pure components Kg /mol

14. Ks io Isentropic compressibility for the

mixture m

2

/N

15. Ks

E Excess isentropic compressibility for

the mixture m

2

/N

16. Ksid

Ideal mixture was calculated from the relation recommended by Benson & Kiyohara

No units

17. Vio Molar volume for the mixture m3 /mol

18. VM E

Excess molar volume for the mixture m3 /mol

19. ̅m,1, ̅m,2 Partial molar volumes m3 /mol

20. V*1 , V *

2 Molar volumes of pure compounds. m

3

/mol

21. V∞m,1,V

m,2 infinite dilution of partial molar

volumes for the binary system m

3

/mol

22. VE,∞m,1,V E,∞

m,2

infinite dilution of excess partial molar

volumes for the binary system m

3

/mol

23. αi o

Isobaric thermal expansion coefficient K/K

24. Cp,jo Molar isobaric heat capacity of pure component i J /mol /K

25. ɸi Volume fraction for the mixture No units

26. T Absolute temperature for the mixture Kelvin

27. YE Redlich-Kister Polynomial equation No units

28. Ai

Where Ai = A0, A1, A2, A3 are the

coefficients obtained from R-K polynomial equation

No units

29. σ Standard deviation estimated from RK

polynomial data No units

30. b cubic packing factor which is assumed

to binary liquids Kg/cc

31. R Ideal gas constant Cal/K/mol

32. лi Internal pressure in a mixture Pas

Table 03: Comparison of experimental densities (ρ) and

speed of sound (U) of pure liquids with literature Values

Chemical Temp

(K)

Density(ρ) (

kg/m3)

Expt Lit

Speedof sound(U) ( m/s)

Expt Lit

Cp(J/

mol/K ) Ethyl-4-hydroxy benzoate 303.15

K 1.1035 - - - 1523.0

---

304.03b

P-Methoxy benzoic acid

303.15 K 1.1896 - - - 1559.6 --- 204.0b

Cyclohexa

none 303.15 K

0.93 18 0.936 5a 1406 .6 140 7.7a 200.4 b

Standard uncertainties ‗U‘ are U(X1+X2)

=0.0001, U (ρ) = 0.003 kg/m3

, U (u) = 0.76 m/s

a

(3)

3234

4 Results and discussion

4.1 Estimation excess thermodynamic parameters From fig 1 βs

E

may be explained high negative values rather than other terms of two opposing effects like breaking of molecular order of liquid mixture, packing of large sized molecules and dipolar interaction as well as hydrogen bonds between unlike components[11],[12],[13],[14]. From

figures 2 and 3 also shows negative values of Vm

E

and Lf E

in the mixture shows negative values for entire mole fraction range. The negative variation signifies strong interactions between the components and it confirms that there exist like molecules and polar components in H-bond formation, also other chemical effects like dispersion and dipolar forces in the components of liquid mixtures [15],[16],[17],[18]

0.0 0.2 0.4 0.6 0.8 1.0

-1.0 -0.8 -0.6 -0.4 -0.2 0.0

S E X

1

0

12 / m 2. N

-1

X1

303.15 K 308.15 K 313.15 K

Cyclohexanone + ethyl-4-hydroxy benzoate

Fig 1(a)

0.0 0.2 0.4 0.6 0.8 1.0

-1.2 -0.9 -0.6 -0.3 0.0

S E X

1

0

12 / m 2. N

-1

X1

303.15 K 308.15 K 313.15 K Cyclohexanone +p-Methoxybenzoic acid

Fig 1(b)

Fig 1(a-b) Variation of excess adiabatic compressibility with respect to mole fraction of Cyclohexanone with Ethyl-4hydroxy benzoate/p-Methoxy benzoic acid at three different temperatures

0.0 0.2 0.4 0.6 0.8 1.0

-0.008 -0.006 -0.004 -0.002 0.000

Lf

E X

1

0

13

/

m

Cyclohexanone + ethyl-4-hydroxy benzoate

X1

303.15 K 308.15 K 313.15 K Fig 2(a)

0.0 0.2 0.4 0.6 0.8 1.0

-0.009 -0.006 -0.003 0.000

303.15 K 308.15 K 313.15 K

Cyclohexanone + p-Methoxy benozoic acid

Lf

E X

1

0

13

/

m

X1

Fig 2(b)

Fig 2(a-b) Variation of excess free length with respect to mole fraction of Cyclohexanone with Ethyl-4hydroxy benzoate/p-Methoxy benzoic acid at three different temperatures

Fig 4 indicates positive variation of HE. The positive variations suggest that there exist weak interactions between the components of liquid mixture .It is observed that the molecular interaction between the components of liquid mixtures shows the non-ideal nature.

0.0 0.2 0.4 0.6 0.8 1.0

-1.0 -0.8 -0.6 -0.4 -0.2 0.0

Fig 2(a)

Cyclohexanone+ ehyl-4-hydroxybenzoate

303.15 K 308.15 K 313.15 K

V

E m

X 10

6/m 3.mol

-1

X 1

0.0 0.2 0.4 0.6 0.8 1.0

-1.0 -0.8 -0.6 -0.4 -0.2 0.0

V

m

E X

1

0

6 /

m

3 .mo

l

-1

X1

303.15 K 308.15 K 313.15 K

Cyclohexanone +p-Methoxy benzoic acid

(4)

3235

Fig 3(a-b) Variation of excess molar volume with respect to mole fraction of Cyclohexanone with Ethyl-4hydroxy benzoate/p-Methoxy benzoic acid at three different temperatures

Non-ideal liquid mixtures show considerable deviation from linearity in their physical behavior with respect to concentration and these have been interpreted as arising from the presence of strong or weak interactions[21],[23] .The deviations of theoretical values from the experimental one is due to the presence of molecular interaction, interstitial accommodation as molecules have different sizes and shapes and orientation of molecules etc.

0.0 0.2 0.4 0.6 0.8 1.0

0.000 0.003 0.006 0.009 0.012 0.015

H

E J

.mo

l

-1

Cyclohexanone+ ethyl-4-hydroxy benoate

303.15 K 308.15 K 313.15 K

X1

Fig 4(a)

0.0 0.2 0.4 0.6 0.8 1.0

0.000 0.005 0.010 0.015 0.020

H

E J

.mo

l

-1

X1

303.15 K 308.15 K 313.15 K Fig 4(b)

Cyclohexanone +p-Methoxybenzoic acid

Fig 4(a-b) Variation of excess enthalpy with respect to mole fraction of Cyclohexanone with Ethyl-4hydroxy benzoate/p-Methoxy benzoic acid at three different temperatures

4.2 RK polynomial equation: Authors have already reported

that the excess properties βs

E

, Lf E

, HE and Vm E

showed that

an examination in the trends of deviation dependence on X1

of these systems Cyclohexanone + benzoates, and the differences in interactions are mostly significant in mixtures are very flush in the components. From the treatment of excess thermo physical quantities for liquid mixtures

proposed by Desnoyers and Perron [20]in agreement with

the original statements of Redlich and Kister from equation (6&7), the table 4 conclude that the excess quantity (βs

E

, Lf

E

,HE and Vm E

) gives an overall view of the spring of the non-ideality in the mixtures but still can be quite evasive, especially for systems that shows strong interactions at huge suffusion.[27],[28],[29]

Table 04 Parameters (A k) and Standard Deviation (σ) for Cyclohexanone with ethyl -4-hydroxy benzoate/p-Methoxybenzoic acid at T= 303.15 K, 308.15K and 313.15K

parameter Temp(K) A0 A1 A2 σ

Cyclohexanone + ethyl-4-hydroxy benzoate

1012βS E

/(m2.N

-1

)

303.15 2.1706 -1.0728 -0.8269 0.3307

308.15 1.8284 -0.3832 -1.8109 0.2501

313.15 2.3340 -1.4372 -0.3082 0.3701

1013Lf E

/ (m)

303.15 7.1126 -5.8163 -2.9961 1.1245

308.15 11.0968 -9.6586 -2.5353 1.8117

313.15 12.3110 -12.5484 -3.1692 2.0385

106

VE/(m3.mol-1)

303.15 0.5758 0.1866 -0.3200 0.1384

308.15 0.6614 -0.0137 0.0292 0.1456

313.15 0.2921 0.0766 -0.2655 0.0668

HE/(J.mol-1)

303.15 0.0266 0.0065 -0.0265 0.0014

308.15 0.0421 -0.0003 0.0015 0.0010

313.15 0.0343 0.0072 -0.0068 0.0008

Cyclohexanone + p-Methoxy benzoic acid

1012βS E

/(m2.N

-1

)

303.15 -1.4711 -0.8596 0.1050 0.2588

308.15 -17347 -1.0377 0.1270 0.3098

313.15 -1.9373 -1.0147 0.2896 0.3396

1013LfE/ (m)

303.15 -17.3827 -8.7204 4.0539 2.9144

308.15 -20.5265 -9.0227 1.8669 3.5182

313.15 -23.2274 -9.7134 2.3137 3.9644

106

VE/(m3.mol-1)

303.15 2.3712 -0.1227 -1.0137 0.6402

308.15 2.7109 -0.0338 0.0471 0.8217

313.15 3.0296 0.1104 1.0045 0.9956

HE/(J.mol-1)

303.15 0.0426 0.0027 -0.0314 0.0008

308.15 0.0541 -0.0047 0.0005 0.0010

313.15 0.0467 -0.0042 -0.0125 0.0009

4.3 Estimation of Partial molar volumes

The molecular interactions present in the Cyclohexanone + benzoates are also reflected in terms of partial molar volumes .The obtained values of partial molar volumes are reported in Table 5 , also tabulated the infinite dilution values of partial molar volume and Excess partial molar volumes in table 6. By observing the below tables all the estimated values are positive, from which it concludes that weak interactions exist among the taking liquid mixtures are due to geometrical factors, hydrophilic interactions gives the higher degree of dissociation of solute-solute and solvent-solvent results in liquid mixtures[25],[26],[28]

Table 05 Partial molar volumes for Cyclohexanone with ethyl -4-hydroxy benzoate / p-Methoxy benzoic acid at

different temperatures Mole

fraction

cyclohexanone + ethyl -4-hydroxy benzoate

Mole fraction

Cyclohexanone + p-Methoxy benzoic acid V ֿm ,1x10

-5 V ֿm ,2x10

-5 V ֿm

,1x10-5 V ֿm ,2x10

-5

303.15K

0.0000 4.966 18.851 0.0000 3.637 21.389

0.1027 4.820 78.183 0.1581 4.457 97.962

0.1887 4.667 62.015 0.2236 4.273 53.068

0.2346 4.414 25.194 0.3357 4.097 52.232

0.3928 4.133 47.851 0.4657 3.876 14.318

0.4746 4.051 60.214 0.5445 3.255 15.419

0.5874 4.172 51.929 0.6930 2.774 73.431

0.6777 3.864 28.635 0.7195 4.284 19.473

0.7435 4.857 16.621 0.8173 3.101 27.124

0.9052 3.655 19.153 0.9583 4.953 21.294

1.0000 4.024 17.909 1.0000 5.276 23.027

308.15K

0.0000 4.203 18.937 0.0000 6.481 21.421

0.1027 4.128 65.891 0.1581 7.990 14.813

0.1887 4.192 13.564 0.2236 7.408 71.086

(5)

3236

0.3928 4.061 62.352 0.4657 5.817 25.180

0.4746 4.116 80.716 0.5445 3.851 26.389

0.5874 4.330 68.170 0.6930 3.489 12.756

0.6777 3.830 33.351 0.7195 4.105 20.164

0.7435 5.245 15.556 0.8173 3.098 29.619

0.9052 4.319 19.283 0.9583 6.353 22.107

1.0000 4.042 18.776 1.0000 5.313 22.587

313.15K

0.0000 4.656 19.037 0.0000 4.862 21.695

0.1027 4.317 26.288 0.1581 3.122 12.481

0.1887 4.199 24.678 0.2236 4.911 42.876

0.2346 4.226 16.830 0.3357 4.741 15.523

0.3928 4.260 71.295 0.4657 3.919 33.000

0.4746 4.179 14.148 0.5445 3.325 35.586

0.5874 4.070 44.183 0.6930 5.624 20.457

0.6777 4.247 14.477 0.7195 4.095 22.017

0.7435 3.583 20.262 0.8173 3.873 40.669

0.9052 7.773 18.902 0.9583 3.415 22.199

1.0000 4.059 18.440 1.0000 5.325 22.159

Table 06 Values of partial molar volume of the components

at infinite dilution (V∞m,1, V∞m,2) and excess partial molar

volume at infinite dilution (VE,∞m,1and VE,∞m,2) for all the

systems at three different temperatures

System Temp(K) V

m,1X

10-5

V∞m,2X

10-5

VE,∞m,1X

10-5

VE,∞m,2 X

10-5 cyclohexanone

+ ethyl -4-hydroxy benzoate

303.15 K 4.966 17.909 0.942 0.942

308.15 K 4.203 18.776 0.161 0.161

313.15 K 4.656 18.440 0.597 0.597

Cyclohexanone + p-Methoxy benzoic acid

303.15 K 3.637 30.304 1.639 1.638

308.15 K 6.481 35.216 1.168 1.166

313.15 K 4.862 31.883 0.463 0.464

5.

C

ONCLUSION

Experimental results for Cyclohexanone with benzoates from 303.15K - 313.15K using standard techniques were tabulated, thermo physical properties and their excess data were computed by the obtained data also compared using the literature, due to charge transfer forces positive /negative values given by Lf

E, β s

E, HE and V m

E for all

systems over entire mole fraction at three different temperatures .The values of standard deviation and coefficients were obtained by fitting the excess parameters into Redlich-Kister polynomial equation. The determined values of partial molar volumes (V ֿm,1 ,V ֿm,2) reflects the

conclusion drawn from Vm

E

and the results explicit volumetric properties of binary system. This deviation in between molecules may be attributed in these properties for the polar- polar and non polar-non polar interaction between the molecules entire mole faction range.

A

CKNOWLEDGMENT

Authors are thankful to their research guide Dr. Shaik Babu, Dept. of physics (DST-FIST) sponsored department, K L E F, Deemed to be University, Guntur, A.P, India for his valuable suggestions and discussions. "Dr.Shaik.Babu

would like to thank Department of Science and

Technology (DST), Govt. of India, for the award of

DST-FIST Level-1 (SR/FST/PS-1/2018/35) scheme to

Department of Physics, KLEF"

R

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N.Ouerfelli, A.Toumi‖Reduced Redlich–Kister

functions and interaction studies of Dehpa + Petrofin binary mixtures at 298.15 K‖ Phys . Chem. liqds, vol.57, no.4, pp. 536-546, 2019

[13]A.Nagarjuna, Shaik.Babu, K.Govinda rao,

(6)

N,N-3237

Dimethylaniline at Different Temperatures ‖ Asian. J. chem, vol. 30 , no.9, pp. 2008-2012, 2018

[14]A.Nagarjuna, Shaik.Babu ―Speed of Sound Studies

and behavior of Intermolecular Interactions of Benzyl Benzoate with acetone at different temperatures‖ Int. J.Engg. Sci. Inv, Special issue pp. 33-38,2018

[15]A.Nagarjuna, Shaik.Babu ―Viscometric and speed

of sound studies of the binary liquid mixtures of acetone with 2-propanol at 303.15K‖ Int. J.Engg. Sci. Inv, Special issue pp. 28-32,2018

[16]P.Nagababu, Shaik.Babu, Dheiver F. Santos,

M.Gowrisankar ― Investigation of molecular Interactions in binary mixtures of homologous series of aliphatic alcohols with 2-methyl cyclohexanone at various temperatures‖ Phys. Chem. Liqs .

[17]K.Govinda rao, M.Gnana kiran, Shaik.Babu,

D.Santos, ―Correlation studies of alkyl benzoates with alkanols at different temperatures‖ J.pharm. sci. res, Vol. 9, no. 5, pp. 624-628, 2017

[18]R.Trabelsi, Shaik.Babu, H.Salhi, N.Ouerfelli,

A.Toumi ―Investigations of the reduced Redlich-Kister excess properties of 1,4-dioxane+isobutyric acid binary mixtures at temperatures from 295.15K to 313.15K‖, Phys. Chem. liqds. Accepted (in press)

[19]S Thirumaran, J Ramesh ,‖Acoustic and excess

thermodynamical studies on 1-alkanols with dma in cyclohexanone at different temperatures‖, Ras. J. Chem ,Vol.2 , no.3, pp. 733-739,2009

[20]J E Desnoyers , G Perron ,‖Treatment of excess thermodynamic quantities for liquid Mixtures‖, J. sol. Chem,Vol. 26, no 8 , pp.749-755,1997

[21]R Kumar , S Jayasankar, V Kannappan , ‖Study of

molecular interactions in binary liquid mixtures‖ , IJPAP ,Vol.46, pp. 169-175,2008

[22]O Redlich , AT Kister ,‖Algebraic representation of

thermodynamic properties and the classification of solutions‖, Ind Eng Chem, Vol.40 , pp.345– 348,1948

[23]H. Salhi, Shaik. Babu, N. Al-Eidan, N.H. Mekni, N.

Al-Otaibi, K.Y. Alqahtani, N.A.Al-Omair, N.

Ouerfelli,‖On the reduced Redlich-Kister excess properties for 1,2-dimethoxyethane with propylene carbonate binary mixtures at temperatures (from 298.15 to 318.15) K‖. Med. J.Chem, Vol. 6, no.2 , pp. 33-41, 2017

[24]R C Reid, J M Prausnitz, B E Poling, ―The

Properties of Gases and Liquids‖, 5th

ed, (McGraw Hill book company, New York,1987)

[25]MF Hossain ,TK Biswas , MN Islam ,‖ Volumetric

and Viscometric studies on dodecyl

trimethylammonium bromide in aqueous and in aqueous amino acid solutions in premicellar region‖, Monat. Chem, Vol. 141,pp. 1297–1308, 2010

[26]J M McDowall, C A Vincent, ‖Viscosity behavior of

some simple electrolytes informamide solution‖. J .Chem. Soc, Faraday Transactions 1: Phys Chem in Condensed Phases, Vol. 70, pp.1862-1868,1974

[27]A.Nagarjuna, KV Yamini Kanth, G. Balaji Prakash,

Debashis Das,‖Molecularinteractions in binary liquid mixtures containing benzyl benzoate‖, Ras. J. Chem Vol.12, no. 4 , pp.1774 – 1782, 2019

[28]A. Nagarjuna, Shaik.Babu, K.Govinda rao, T.

Kalimulla, G.V Gangadhar rao, ―Thermo-

[29]acoustical and molecular interaction studies in

binary liquid mixtures at different tempera tures,‖ International journal of applied physics(SSRG-IJAP), Vol.5, no.3, pp. 11-21,2018 Sk.Suriya

shihab, K. Govinda rao, M.Gnana Kiran,

Shaik.Babu, S.Sreehari Sastry, ‖Excess

thermodynamic and acoustic properties for

equimolar mixture of methyl benzoate and alkanols with benzene at 303.15 K,‖ Ras. J.Chem, Vol.10, no. 1 pp.59-63, 2017

[30]A.Nagarjuna, Shaik.Babu, K. T.Kalimulla,G.V

Gangadhar rao, ―Investiga tion of inter molecular interactions in binary liquid mixtures‖Recent trends in Physics, chemistry and Allied sciences, Book chapter 19, pp.111-116, Sep 2019

Figure

Table 01:       Purity analysis of chemicals studied
Table  2 List of symbols/Notations
Fig 2(a)
Fig 4(a) 308.15 K 313.15 K
+2

References

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