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Role of substituent on benzene ring and their importants on thermodynamic properties

L.Venkatramana1, K.Sreenivasulu2, K.Sivakumar,2 K. Dayananda Reddy*1

1 Department of Chemistry, P.V.K.N.Govt. Degree & P.G. College, Chittoor-517001, A.P., India.

2 Department of Chemistry, S.V.Arts Degree & P.G.College (T.T.D’S), Tirupati-517502, A.P., India.

Abstract

Densities (ρ) of pure liquids and their mixtures have been measured at 298.15 K to 313.15 K and atmospheric pressure over the entire composition range for the binary mixtures of benzyl alcohol with benzene, toluene, chlorobenzene, bromobenzene and nitrobenzene by using Rudolph Research Analytical Digital densitometer (DDH-2911 model). Further, the ultrasonic sound velocities for the above said mixtures were also measured at 303.15 K and 313.15 K. The measured
density data were used to compute excess molar volumes (VE) and these were compared with
Hwang equations. Isentropic compressibility (ks) and excess isentropic compressibilities (k E ) were evaluated from experimental sound velocity and density data. Moreover, the experimental sound velocities were analyzed in terms of theoretical models namely collision factor theory (CFT) and free length theory (FLT). The experimental results were discussed in terms of intermolecular interactions between component molecules.

Keywords: Density, excess volume, sound velocity, Theoretical analysis, molecular interaction.


*Corresponding Author
K. Dayananda Reddy, Department of Chemistry, P.V.K.N.Govt. Degree & P.G. College, Chittoor-
517001, A.P., India E-mail: ramanapvkn@gmail.com

1 Introduction

For many years the chemical industry has recognized the importance of thermodynamic and physical properties in design calculations involving chemical separations, fluid flow, and heat transfer. The study of molecular interaction in the liquid mixtures is of considerable in the

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elucidation of the structural properties of the molecules. The intermolecular interactions influence the structural arrangement along with the shape of the molecules. The sign and magnitude of these properties guide us to understand possible interactions between the component molecules [1-4]. Fundamental thermodynamic and thermo physical properties are the essential sources of information that necessary for a better understanding of the non-ideal behavior of complex systems because of physical and chemical effects, which are caused by molecular interactions
,intermolecular forces etc., of unlike molecules. The knowledge of the structure and molecular interactions of liquid mixtures are very important from fundamental and engineering point of view. From a practical point of consideration, these properties are necessary for the development of thermodynamic models required in adequate and optimized processes of the chemical, petro chemical, pharmaceutical, and other industries. In addition, extensive information about structural phenomena of mixtures is of essential importance in development of theories of the liquid state and predictive method. The experimental data on macroscopic properties such as excess molar volumes, excess viscosities, surface tension and refractive index are often useful to understand the nature of homo and hetero molecular interactions, between component molecules. A survey of the literature as shown that excess volume and ultrasonic sound velocity data for the binary mixtures of benzylalcohol with benzene, chlorobenzene, nitrobenzene and benzonitrile were reported at 303.15
K [5]. In the present study, densities (ρ) of pure liquids and their mixtures namely benzylalcohol with benzene, toluene, chlorobenzene bromobenzene, and nitrobenzene were measured over the entire composition range at 298.15 K, 303.15 K, 308.15 K and 313.15 K and ultrasonic sound
velocity data at 303.15 K and 313.15 K. From these data excess volumes (VE) and excess
isentropic compressibility

(k E ) were calculated. Further, the experimental the sound velocity data

were compared with various theories namely collision factor theory (CFT) and free length theory
(FLT). The organic liquids that were chosen in the present investigation are having many industrial applications. Benzyl alcohol is a versatile compound used as a solvent for gelatin, cellulose acetate,

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shellac and for pharmaceutical aid as an antimicrobial agent [6]. Further, benzyl alcohol is also used in perfumery, in microscopy as an embedding material, and in veterinary applications [7]. Commercial use of benzene and toluene includes synthesis of different intermediate compounds during the process of manufacture of plastics, dyestuffs, detergents and insecticides [8, 9]. The major use of chlorobenzene is an intermediate in the production of commodities such as herbicides, dye stuffs and rubber. Bromobenzene is an important compound in the preparation of Grignard reagent and also an ingredient in the manufacture of phenylcyclidine [10, 11].The largest end use for nitrobenzene is in the production of aniline, p-aminophenol, nigrosine dyes, dyestuffs and resins. The present work was under taken to know the influence of various substituents on benzene ring that may influence both the sign magnitude of excess volume and isentropic compressibility

2 Experimental

2.1 Materials
All the chemicals used in the present work were of analytical reagent grade procured from
(S.D.Fine chemicals Ltd.,India and Merck and their purities were as follows: benzyl alcohol
99.7%, benzene 99.5%, toluene 99.5%,chlorobenzene 99.8%, bromobenzene 99.5% and nitrobenzene 99.7% . Prior to experimental measurements, all the liquids were purified as described in the literature [12, 13]. The purity samples were attained by fractional distillation and the purity of chemicals were checked by comparing the measured densities and ultrasonic sound velocity, which were in good agreement with literature values [5, 14-17] and these are given in Table 1. The purity of the sample was further confirmed by GLC single sharp peak. Before use, the chemicals were stored over 0.4nm molecular sieves for about 72hrs to remove water and were later degassed.
2.2 Apparatus and procedure
All the binary liquid mixtures are prepared by weighing an appropriate amount of pure liquids an electronic balance (Afoset, ER –120A, India) with a precision of ±0.1 mg by syringing each

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component into airtight stopper bottles to minimize evaporation losses. The uncertainty of the mole fraction was ± 1 × 10-4. After mixing the sample, the bubble free homogenous sample was transferred into the U-tube of the densimeter through a syringe. The density measurements were performed with a Rudolph Research Analytical digital densimeter (DDH-2911 Model), equipped with a built-in solid-state thermostat and a resident program with accuracy of temperature of
303.15 K ±0.03 K.The uncertainty density measurement liquid mixtures are ±2×10–5 gm.cm-3.
Proper calibrations at each temperature were achieved with doubly distilled, deionized water and with air as standards. A multi frequency ultrasonic interferometer (M-82 Model, Mittal Enterprise, New Delhi, India) operated at 2 MHz, was used to measure the ultrasonic velocities of the binary liquid mixtures at temperatures, at 303.15K and 313.15 K by using a digital constant temperature water bath. The uncertainty in the measurement of ultrasonic sound velocity is ±0.3%. The temperature stability is maintained within ± 0.01 K by circulating thermostatic water bath around the cell with a circulating pump. In order to minimize the uncertainty of the measurement, several maxima are allowed to pass and their number (50) in the present study is counted. All maxima are recorded with the highest swing of the needle on the micrometer scale. The total distance d (cm) moved by the reflector is given by d= nλ/2, where λ is the wave length. The frequency, ν, of the
crystal being accurately known (2.0 MHz), the speed of sound, u in ms-1 is calculated by using the
relation u= νλ. The working of the interferometer was tested by making measurements for pure samples of benzyl alcohol, benzene, toluene, chlorobenzene, bromobenzene and nitrobenzene and the measured sound velocities of these liquids are in good agreement which was reported in the literature [18].

3 Results and discussion

The measured densities of pure liquids and their mixtures were given in Table 2 for all the binary mixtures of benzylalcohol with benzene, toluene, chlorobenzene, bromobenzene and nitrobenzene

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at temperature range from 298.15 to 313.15 K. The excess molar volume (VE) of all the binary mixtures were calculated from the measured densities using the following equation.
VE/cm3.mol-1 = [x1M1 + x 2M2]/ρm – [x 1M1/ρ1+ x 2M2/ρ2] (1)
where, xi is the mole fraction of component i(i=1,2) in the mixture; Mi is the molar mass ρ and ρi are the measured density of the mixture and the pure component i, respectively. The computed VE data was also given in Table 2 along with predicted in terms of Hwang equation [19].The methods and calculation of VE in terms of Hwang equation were described earlier [20-22]. The VE data for all the binary systems of benzylalcohol with benzene, toluene, chlorobenzene, bromobenzene and
nitrobenzene were graphically represented in Figures 1-5.
An examination of curves in figures 1-5 shows that, excess volume (VE) data for the binary mixtures benzylalcohol with benzene, toluene, chlorobenzene, bromobenzene and nitrobenzene are negative over the entire composition range at all temperatures. In general, the sign of excess volume (VE) depends on the relative magnitude of contractive and expansive effects that arise on mixing of the component liquids. The factor that causes contraction in volume on mixing are: “Strong specific interactions, generally a kind of chemical interactions, strong physical interactions such as dipole-dipole or dipole-induced dipole interactions and accommodation of molecules of one component in to the interstitial of the structural network of molecules of the other component”. On the other hand, dissociation of one component or both of one components and when the molecular size of the component molecules are very large, which does not favor for fitting of the molecules with each other hand formation of weaker solute-solvent bond than solute-solute and solvent-solvent bonds and these forces are contributing expansion of volume on mixing the
components.

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An examination of curves in figures from 1-5 indicate that the factors which are responsible for contraction in volume are dominant over the entire composition range for all the binary mixtures. The algebraic excess volume data of all the binary mixtures will fall in the order:
benzene < toluene < chlorobenzene < bromobenzene < nitrobenzene
The above order indicates that extent of negative magnitude of negative excess volume increases due to nature of different substituents that are present on benzene ring.
An examination of VE data in Table 2 for the binary systems benzene and toluene shows that,
more negative VE values is observed in latter case. This is due to introduction of methyl group on benzene ring [23]. So, the electron density on benzene ring increases there by these interactions becomes stronger and this should lead to more negative values of VE benzyl alcohol with toluene. Further, the more negative excess volume data of chlorobenzene when compared to bromobenzene may explained as follows: Chlorobenzene is more reactive than bromobenzene because of the chlorine atom is bonded with sp3 hybridized carbon atom and thereby it can be removed easily. Hence, the rate of reaction of chlorobenzene becomes faster [24-26] when compared to bromobenzene.
The experimental results in the present investigations support this contention. Chlorine atom in chlorobenzene is an electron withdrawing atom, which tries to attract the π-electrons of the benzene ring, there by the electron density of the aromatic ring decreases. As result, the benzene ring in chlorobenzene becomes relatively poor electron donor towards electron seeking proton of any group [27].Hence chlorobenzene interacts strongly with benzylalcohol leading to more vE values.
Further bromobenzene is less reactive when compared to chlorobenzene because of its double bond
character between carbon and bromine atom and also it may be attributed its heavier size. Further,

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the less negative VE of bromobenzene when compared to chlorobenzene may be postulated in terms of the presence of vacant 3d-orbital in bromine atom of bromobenzene.So that it act as an electron acceptor towards π-electrons of aromatic compounds [28,29]. The more negative VE data for the binary system benzyl alcohol with nitrobenzene when compared to benzene, toluene, chlorobenzene and bromobenzene may be due to its high dipole moment and dielectric constant. Nitrobenzene is supposed to be a relatively complex molecule and its non-ideality arises due to rotation of nitro group freely along the C-N axis where it gives more flexibility to the interaction arising due to the two highly polar N→O bonds [24]. Further, the more negative VE data for the mixture benzylalcohol with nitrobenzene when compared to other mixtures of present investigation may also due to the following reasons: i) Nitro group withdraw the electron cloud from the benzene ring while chloro and bromo groups release the electron cloud to the benzene ring and ii) viscous nature of nitrobenzene[14].
Data for mole fraction (x1) of benzylalcohol density of pure liquids and their liquid mixtures and
experimental sound velocities (u), are included in columns 1-3 of Table 3. Isentropic
compressibilities (κs) and excess isentropic compressibilities (k E )
, were also included in columns
4 and 7 of Table 3.The excess isentropic compressibility data were also represented graphically in
Figures 6-10.The isentropic compresibilities (κS) and excess isentropic compresibilities

(k E )

were
calculated by using the following equations
κS= u-2ρ-1 (2)

The corresponding excess isentropic compressibilities (k E ) were obtained from the relation [30]

κ E κ

κid

(3)
where κ id
is the ideal value of the isentropic compressibility and was calculated from the
following equation [30].

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κ id κ

TV α 2 / C

 

2

x V  α

/ x C 

(4)

2

s i i1

s.i i i

p.i


T
 

2

i1

 2

i i i i

 i1

2

i i1

p.i


Here, Cpi and αi are the molar heat capacity and the thermal expansion coefficient of the ith component respectively. The value of Cpi and αi obtained and evaluated from literature [17,31] and given in Table 4.

An examination of curves in Figures 6-10 suggest that excess isentropic compressibility data (k E )

for the binary mixtures of benzylalcohol with benzene, toluene, chlorobenzene, bromobenzene and nitrobenzene are negative over the entire composition range at 303.15 K and 313.15 K. This may be interpreted in terms of two opposing effects: i) loss of dipolar association and difference in size and shape of the component molecules; and ii) dipole-dipole, dipole-induced dipole, electron- donor-acceptor interactions and interstitial accommodation of benzylalcohol lattice. The former effect contributes to an increase in free length, described by Jacobson [32]. This leads to negative deviation in sound speed and positive deviation in excess compressibility. The latter effect, on the other hand, leads to positive deviation in sound speed and negative deviation in excess compressibility. The sign and magnitude of the actual deviation depends on the relative strengths of the two opposing effects. As already reported by Benson and Kiyohara [30] the sign and magnitude of the excess isentropic compressibility, that arises through charge transfer, dipole induced dipole and dipole-dipole interactions interstitial accommodation and orientation ordering lead to a more compact structure which contributes to negative excess isentropic compressibility. Our experimental results were also supports this contention.
The algebraic values of κ E values for all the binary systems fall in the order:
Benzene < Toluene < Chlorobenzene < Bromobenzene < Nitrobenzene
The above order indicates that the extent of stronger interactions increases as the free spaces between benzene and substituted benzenes.

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Experimental ultrasonic sound velocities were analyzed in terms of collision factor theory (CFT) [33], free length theory (FLT) [34,35] and these were also included in Table 3 along with experimental ultrasonic sound velocities. The pure component data namely, the molar volume (Vm), molar volume at absolute zero (V0), molar available volume (Va), free length (Lf), surface area (Y), collision factor(S), average molecular radius (rm), actual volume of molecules per mole (B) and molecular sound velocity(R) that were used to calculate the above said theories were collected from the literature [36]. The methods and details of calculation of theories were discussed earlier [37, 38].
The details of various theories and relevant equations are given as follows:
A comparison between experimental sound velocities and theoretical values suggest that the model proposed by Schaaff’s CFT gives better estimation of sound velocity data. The methods of calculation of these theories were described in earlier. The merits of these theories were compared in terms of relative root mean deviation by using the following formula [39].
RMSD = (5) The RMSD for all the binary systems values given in Table 5 shows that Schaaff’s CFT model
gives better estimation in sound velocity for the binary mixtures under the investigation.
The experimental VE values and κSE data in have been fitted to Redlich-Kister type polynomial equation[40].

E x x n

a x

x i

y  1 2

i 0 i

1 2

(6)
Where YE= VE or κ E
the subscription ‘i’ in the equation takes value from 0 to 2 ; Ai is the
adjustable parameter of the function and are determined using the least-squares method. The
corresponding standard deviations σ(YE) have been computed using the relation.
σ(YE) =[ Σ(YE

E

cal

)2/(m-n)]1/2 (7)

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where ‘m’ is the total number of experimental points and ‘n’ is the number of coefficients in
equation 6, and the standard deviations of all the binary mixtures have been presented in Table 6.

5.Conclusion

In the present work excess volume data of binary mixture of bezylalcohol with benzene, toluene, bromobenzene, chlorobenzene and nitrobenzene were observed the entire composition range from at 298.15 K to 313.15 K and the property is negative in all the binary mixtures.This shows that strong intermolecular interactions are prevailing in liquid mixtures. Since the nitro group of nitrobenzene is more powerful electron withdrawing group when compared to bromobenzene,
chlorobenzene, more negative VE data were observed in the binary system benzylalcohol with
nitrobenzene. Further κ E
data in all the binary mixtures shows that the property is negative at
303.15 K and 313.15 K, which arises due to changes of free volume in the real mixtures and presence of π-electrons in benzylalcohol resulting in the formation of weak intermolecular complexes leading to positive deviation in sound velocity and negative excess isentropic compressibility.

References

[1] V Syamala, K Sivakumar and P Venkateswarlu, J.Chem.Thermodyn., 38, 1553 (2006) [2]A Ivan, M Ismael, and JA Gonzol, J. Chem. Eng. Data. 55, 5400 (2010)
[3] M Radhamm, P Venkatesh, and MV Prabhakara Rao, J.Chem.,Thermodyn., 40,492 (2008) [4]MV Rathnam, M Sudhir, and MS Kumar, J.Chem.Eng.Data, 55,5946(2010)
[5]A Ali, and M Tariq, J. Mol. Liqs.,128 50 (2006)
[6]W Martindale, The Extra Pharmacopoeia 3rd Edn., Pharmaceutical Press, London (2002). [7]The Merck Index, Merck and Co.Inc, Wiley Interscience, 13th Edn., New York (2001).
[8] D.R.Lide, C.R.C.Hand book of chemistry, 81stEdn, (Boca Raton, New York) (2001).
[9] J.A. Dean, Lange’s Hand book of chemistry, 13th Edn, (McGraw Hill, New York) (1987).
[10] Kirk-Othmer Encyclopedia of Chemical Technology, Wiley Inter science, 5th Edn, 793(2004)

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[11] Kirk-Othmer, Encyclopedia of Chemical Technology Wiley Inter science, 5th Edn,224(2004) [12] J A.Riddick, W Bunger and TK Sankano, 4th Edn.,Wiley Interscience, New York(1986). [13]S Timmermans, J.Physico-chemical constants of pure organic compounds, Elsevier,
Amsterdam,(1950)
[14]CL Prabhavathi, K Sivakumar, P Venkateswarulu, and GK Raman, Phys.Chem.Liq.,38,
705(2000)
[15]A Ali, A KNain, D Chand and R Ahmad, J. Mol.Liq, 128, 32 (2006)
[16]J Nayak, I Aralaguppi and TM Aminabhavi, J.Chem. Eng. Data, 48, 628(2003) [17]KS Reddy, R Venkateswralu and GK Raman, Indian J.Chem.Technol., 27, 221(1995) [18]Jaganath and A.P Dixit J. chem. Eng. Data, 29, 313(1984)
[19]CA Hwang, JC Holstc, KR Hall and GA Mansoori, Flu. phase Equ., 62, 173(1991) [20]WE AcreeWilliams, AI Zvaizene and PR Naidu, Phys.Chem.Liq, 27, 69(1994) [21]K Sivakumar and PR Naidu, J. Chem. Eng. Data, 39,2(1994)
[22]V Syamala, P Venkateswarlu, G Prabhakar, and K Sivakumar, J. Phys. Chem. Liq.,44,127 (2006)
[23] S Maken, Ankur Gaur and N Varma, J. Ind. Eng. Chem., 13,1098(2007) [24]S Thirumaran and K Indhu, Rasayan. J. Chemistry, 2, 760(2009)
[25]S Thirumaran and N Karthikeyan, Int. J. Chem.Research, 3,83(2011)
[26]S Thirumaran and E Jayakumar, Indian. J.Pure & App. Phys., 47, 265(2009)
[27]R Acharya, Paikra, and GC Mohanty, Indian J. pure & Appl.Phys.,41, 855(2003). [28]R Tanaka and GC Benson, J.Chem.Eng.Data, 21, 320(1976)
[29]R Tanaka and GC Benson, J.Chem.Eng.Data, 23, 75(1978)
[30]GC Benson, and O Kiyohara, J. Chem. Thermodyn.,11,1061(1979
[31]J Jovanovic, A Knezevic-Stevanovic, D Grozdanic, J. Serb. Chem. Society. 76 (3),417(2011) [32]B Jacobson, Acta. Chem. Scand., 8, 1485 (1952).

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[33]W Schaffs, Zeitschrift Fur Medizinische Physik .115, 69 (1940) [34]B Jacobson, J. Chem.Phys. 20, 927(1952)
[35]B Jacobson, Acta. Chem. Scand. 8, 1485(1952)
[36]V Syamala, D Rajasekhar, K Sivakumar and P Venkateswarlu, Chin.J.Chem., 25,1(2007) [37]V Syamala,P Venkateswralu and K Sivakumar, J.Chem.Eng.Data, 51, 928(2006)
[38]H Iloukhani, and Z Rostami, J.Sol. Chem ,32 451(2003)
[39]S Mohammad, HAE AlTuwaim, K Alkhaldi, S Adel, and A Abubaker, J.Chem.Thermodyn., 48, 39(2012)
[40]O Redlich, AT Kister,Indian J.Chem.Research. 40, 345(1948)

Figure captions

Figure.1 Variation of excess volume (VE) of the binary liquid mixture of benzylalcohol(1)
with benzene (2) at 298.15 K (▲), 303.15 K (▼), 308.15 K (●) and 313.15 K (■). Figure.2 Variation of excess volume (VE) of the binary liquid mixture of benzylalcohol (1) with toluene (2) at 298.15 K (▲), 303.15 K (▼), 308.15 K (●) and 313.15 K (■).
Figure.3 Variation of excess volume (VE) of the binary liquid mixture of benzylalcohol (1)
with bromobenzene (2) at 298.15 K (▲), 303.15 K (▼), 308.15(●) and 313.15 K (■).
Figure.4 Variation of excess volume (VE) of the binary liquid mixture of benzylalcohol (1)
with chlorobenzene (2) at 298.15 K (▲), 303.15 K (▼), 308.15(●) and 313.15 K (■).
Figure.5 Variation of excess volume (VE) of the binary liquid mixture of benzylalcohol (1)
with nitrobenzene (2) at 298.15 K (▲), 303.15 K (▼), 308.15(●) and 313.15 K (■).

Figure.6 Variation of excess isentropic compressibility (k E ) of the binary liquid mixture of

benzylalcohol (1) with benzene (2) at 303.15 K (▼) and 313.15 K (■).

Figure.7 Variation of excess isentropic compressibility (k E ) of the binary liquid mixture of

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benzylalcohol (1) with toluene (2) at 303.15 K (▼) and 313.15 K (■).

Figure.8 Variation of excess isentropic compressibility (k E ) of the binary liquid mixture of benzylalcohol (1) with bromobenzene (2) at 303.15 K (▼) and 313.15 K (■).

Figure.9 Variation of excess isentropic compressibility (k E ) of the binary liquid mixture of

benzylalcohol (1) with chlorobenzene (2) at 303.15 K (▼) and 313.15 K (■).

Figure.10 Variation of excess isentropic compressibility (k E ) of the binary liquid mixture of

benzylalcohol (1) with nitrobenzene (2) at 303.15 K (▼) and 313.15 K (■).

Table 1

Densities ( ρ) and sound velocity (u) of pure components at 303.15 K

Component ρ (g cm-3) u (ms-1)

Present work Literature Present work Literature

Benzyl alcohol 1.03760 1.03700[5] 1514 1511[5] Benzene 0.86855 0.86850[14] 1274 1276[14] Toluene 0.85264 0.85260[15] 1277 1278[15] Bromobenzene 1.48156 1.48150[14] 1140 1138[14]
Chlorobenzene 1.09553 1.09550[16] 1250 1252[14]
Nitrobenzene 1.19345 1.19341[17] 1446 1444[17]

References:Ref:[5], Ref:[14], Ref:[15], Ref:[16], Ref:[17]

Table 2

Mole fraction of benzylalcohol (x1), densities (ρ), excess volumes (VE) and predicted excess molar volumes (Hwang) at T= 298.15 K to 313.15 K for the binary mixtures of benzylalcohol with
benzene and substituted benzenes
x1 ρ

(gm.cm-3)

VE(Experimental) VE(Hwang)

cm3 mol-1
Benzyl alcohol (1)+Benzene (2) T=298.15 K

0.0743

0.88816

-0.003

-0.006

0.1198

0.89688

-0.016

-0.013

0.1624

0.90490

-0.025

-0.021

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0.2323

0.91781

-0.038

-0.035

0.2837

0.92712

-0.047

-0.046

0.3566

0.94005

-0.057

-0.059

0.4828

0.96171

-0.068

-0.073

0.5904

0.97946

-0.069

-0.074

0.6784

0.99351

-0.064

-0.066

0.7390

1.00295

-0.058

-0.057

0.7997

1.01218

-0.047

-0.046

0.8574

1.02080

-0.035

-0.033

0.8936

1.02613

-0.027

-0.024

0.9362

1.03232

-0.017

-0.015

0.9587

1.03551

-0.006

-0.009

T=303.15 K

0.0743

0.88290

-0.006

-0.009

0.1198

0.89170

-0.021

-0.018

0.1624

0.89977

-0.030

-0.026

0.2323

0.91280

-0.045

-0.041

0.2837

0.92220

-0.055

-0.052

0.3566

0.93524

-0.065

-0.065

0.4828

0.95710

-0.076

-0.079

0.5904

0.97502

-0.077

-0.082

0.6784

0.98922

-0.073

-0.075

0.7390

0.99873

-0.065

-0.067

0.7997

1.00808

-0.055

-0.055

0.8574

1.01682

-0.045

-0.042

0.8936

1.02219

-0.035

-0.032

0.9362

1.02842

-0.022

-0.020

0.9587

1.03165

-0.011

-0.013

T=308.15 K

0.0743

0.87768

-0.015

-0.018

0.1198

0.88652

-0.029

-0.028

0.1624

0.89468

-0.040

-0.037

0.2323

0.90779

-0.053

-0.049

0.2837

0.91725

-0.062

-0.058

0.3566

0.93041

-0.073

-0.068

0.4828

0.95246

-0.084

-0.080

0.5904

0.97057

-0.087

-0.085

0.6784

0.98491

-0.082

-0.085

0.7390

0.99454

-0.076

-0.080

0.7997

1.00399

-0.065

-0.072

0.8574

1.01281

-0.054

-0.059

0.8936

1.01826

-0.046

-0.049

0.9362

1.02458

-0.034

-0.032

0.9587

1.02785

-0.024

-0.022

T=313.15 K

0.0743

0.87768

-0.015

-0.024

0.1198

0.87242

-0.022

-0.025

0.1624

0.88137

-0.040

-0.035

0.2323

0.88957

-0.050

-0.048

0.2837

0.90280

-0.065

-0.063

IJSER © 2013 http://www.ijser.org

International Journal of Scientific & Engineering Research, Volume 4, Issue 7, July-2013 1809

ISSN 2229-5518

0.3566

0.91234

-0.074

-0.071

0.4828

0.92561

-0.085

-0.082

0.5904

0.94788

-0.098

-0.093

0.6784

0.96614

-0.098

-0.097

0.7390

0.98061

-0.093

-0.094

0.7997

0.99035

-0.086

-0.089

0.8574

0.99988

-0.074

-0.079

0.8936

1.00880

-0.062

-0.065

0.9362

1.01424

-0.047

-0.053

0.9587

1.02064

-0.035

-0.035

Benzylalcohol (1)+Toluene (2) T=298.15 K

0.1066

0.88221

-0.016

-0.020

0.1585

0.89138

-0.030

-0.030

0.2116

0.90077

-0.043

-0.041

0.2651

0.91026

-0.055

-0.050

0.3151

0.91913

-0.063

-0.058

0.3593

0.92698

-0.069

-0.064

0.4171

0.93725

-0.075

-0.071

0.5177

0.95517

-0.080

-0.079

0.6169

0.97288

-0.078

-0.079

0.7147

0.99036

-0.069

-0.073

0.7675

0.99980

-0.061

-0.066

0.8111

1.00762

-0.054

-0.059

0.8644

1.01717

-0.043

-0.046

0.9062

1.02467

-0.033

-0.035

0.9556

1.03354

-0.021

-0.018

T=303.15 K

0.1066

0.87666

-0.020

-0.024

0.1585

0.88591

-0.035

-0.036

0.2116

0.89540

-0.050

-0.047

0.2651

0.90496

-0.061

-0.056

0.3151

0.91392

-0.070

-0.065

0.3593

0.92185

-0.077

-0.075

0.4171

0.93223

-0.083

-0.079

0.5177

0.95034

-0.088

-0.087

0.6169

0.96825

-0.087

-0.088

0.7147

0.98593

-0.078

-0.083

0.7675

0.99550

-0.071

-0.076

0.8111

1.00340

-0.062

-0.068

0.8644

1.01308

-0.051

-0.055

0.9062

1.02066

-0.040

-0.042

0.9556

1.02963

-0.025

-0.022

T=308.15 K

0.1066

0.87294

-0.026

-0.030

0.1585

0.88219

-0.042

-0.043

0.2116

0.89167

-0.056

-0.054

0.2651

0.90123

-0.068

-0.064

0.3151

0.91018

-0.077

-0.073

0.3593

0.91809

-0.083

-0.077

0.4171

0.92847

-0.089

-0.084

IJSER © 2013 http://www.ijser.org

International Journal of Scientific & Engineering Research, Volume 4, Issue 7, July-2013 1810

ISSN 2229-5518

0.5177

0.94658

-0.096

-0.092

0.6169

0.96448

-0.095

-0.095

0.7147

0.98216

-0.086

-0.091

0.7675

0.99172

-0.078

-0.085

0.8111

0.99962

-0.070

-0.077

0.8644

1.00930

-0.059

-0.063

0.9062

1.01687

-0.046

-0.048

0.9556

1.02583

-0.030

-0.026

T=313.15 K

0.1066

0.86833

-0.035

-0.034

0.1585

0.87761

-0.050

-0.051

0.2116

0.88713

-0.065

-0.063

0.2651

0.89671

-0.075

-0.073

0.3151

0.90570

-0.084

-0.082

0.3593

0.91368

-0.094

-0.088

0.4171

0.92412

-0.102

-0.095

0.5177

0.94231

-0.108

-0.103

0.6169

0.96030

-0.106

-0.107

0.7147

0.97809

-0.098

-0.102

0.7675

0.98770

-0.089

-0.096

0.8111

0.99568

-0.084

-0.088

0.8644

1.00539

-0.069

-0.073

0.9062

1.01300

-0.055

-0.056

0.9556

1.02196

-0.033

-0.030

Benzylalcohol (1)+ Bromobenzene(2) T=298.15 K

0.1277

1.43250

-0.029

-0.032

0.1722

1.41302

-0.043

-0.043

0.2221

1.39109

-0.056

-0.055

0.2627

1.37321

-0.066

-0.064

0.3032

1.35534

-0.075

-0.072

0.4133

1.30651

-0.090

-0.089

0.5233

1.25745

-0.098

-0.098

0.6544

1.19859

-0.094

-0.095

0.7249

1.16678

-0.086

-0.087

0.7669

1.14776

-0.078

-0.080

0.8091

1.12862

-0.070

-0.071

0.8430

1.11321

-0.061

-0.062

0.8743

1.09896

-0.052

-0.053

0.9137

1.08099

-0.040

-0.038

0.9503

1.06423

-0.023

-0.023

T=303.15 K

0.1277

1.42605

-0.033

-0.036

0.1722

1.40671

-0.047

-0.047

0.2221

1.38496

-0.061

-0.060

0.2627

1.36723

-0.072

-0.069

0.3032

1.34949

-0.081

-0.077

0.4133

1.30103

-0.098

-0.095

0.5233

1.25232

-0.106

-0.105

0.6544

1.19385

-0.102

-0.103

0.7249

1.16226

-0.095

-0.096

IJSER © 2013 http://www.ijser.org

International Journal of Scientific & Engineering Research, Volume 4, Issue 7, July-2013 1811

ISSN 2229-5518

0.7669

1.14334

-0.086

-0.088

0.8091

1.12431

-0.076

-0.078

0.8430

1.10900

-0.068

-0.069

0.8743

1.09482

-0.057

-0.059

0.9137

1.07695

-0.044

-0.044

0.9503

1.06030

-0.028

-0.027

T=308.15 K

0.1277

1.41974

-0.038

-0.043

0.1722

1.40058

-0.055

-0.055

0.2221

1.37901

-0.071

-0.068

0.2627

1.36139

-0.081

-0.078

0.3032

1.34376

-0.089

-0.085

0.4133

1.29564

-0.107

-0.102

0.5233

1.24725

-0.115

-0.112

0.6544

1.18915

-0.110

-0.112

0.7249

1.15774

-0.102

-0.105

0.7669

1.13895

-0.094

-0.098

0.8091

1.12003

-0.084

-0.088

0.8430

1.10482

-0.076

-0.078

0.8743

1.09071

-0.065

-0.067

0.9137

1.07294

-0.051

-0.051

0.9503

1.05638

-0.034

-0.032

T=313.15 K

0.1277

1.41354

-0.049

-0.050

0.1722

1.39446

-0.062

-0.064

0.2221

1.37303

-0.077

-0.078

0.2627

1.35556

-0.089

-0.087

0.3032

1.33807

-0.099

-0.096

0.4133

1.29031

-0.119

-0.113

0.5233

1.24222

-0.126

-0.124

0.6544

1.18451

-0.123

-0.122

0.7249

1.15328

-0.114

-0.115

0.7669

1.13459

-0.104

-0.107

0.8091

1.11577

-0.093

-0.097

0.8430

1.10064

-0.084

-0.087

0.8743

1.08661

-0.072

-0.075

0.9137

1.06894

-0.057

-0.056

0.9503

1.05244

-0.037

-0.035

Benzylalcohol (1)+ Chlorobenzene (2)T=298.15 K

0.1016

1.09491

-0.035

-0.037

0.1512

1.09212

-0.052

-0.052

0.2028

1.08918

-0.066

-0.065

0.2274

1.08779

-0.073

-0.071

0.3037

1.08340

-0.089

-0.086

0.3526

1.08057

-0.097

-0.094

0.4042

1.07757

-0.103

-0.100

0.5044

1.07171

-0.112

-0.108

0.6042

1.06580

-0.111

-0.109

0.7037

1.05984

-0.102

-0.103

0.7446

1.05734

-0.093

-0.097

IJSER © 2013 http://www.ijser.org

International Journal of Scientific & Engineering Research, Volume 4, Issue 7, July-2013 1812

ISSN 2229-5518

0.8028

1.05382

-0.083

-0.085

0.8474

1.05106

-0.069

-0.073

0.9016

1.04769

-0.050

-0.053

0.9529

1.04450

-0.031

-0.028

T=303.15 K

0.1016

1.08961

-0.039

-0.041

0.1512

1.08691

-0.057

-0.057

0.2028

1.08405

-0.071

-0.071

0.2274

1.08270

-0.079

-0.077

0.3037

1.07844

-0.095

-0.093

0.3526

1.07570

-0.105

-0.102

0.4042

1.07279

-0.112

-0.109

0.5044

1.06710

-0.122

-0.118

0.6042

1.06134

-0.122

-0.121

0.7037

1.05553

-0.113

-0.114

0.7446

1.05311

-0.106

-0.109

0.8028

1.04963

-0.092

-0.096

0.8474

1.04695

-0.079

-0.082

0.9016

1.04364

-0.058

-0.060

0.9529

1.04049

-0.035

-0.032

T=308.15 K

0.1016

1.08442

-0.049

-0.048

0.1512

1.08179

-0.065

-0.065

0.2028

1.07901

-0.078

-0.081

0.2274

1.07770

-0.085

-0.087

0.3037

1.07361

-0.105

-0.103

0.3526

1.07094

-0.113

-0.111

0.4042

1.06815

-0.123

-0.118

0.5044

1.06264

-0.133

-0.127

0.6042

1.05707

-0.134

-0.131

0.7037

1.05143

-0.125

-0.125

0.7446

1.04907

-0.117

-0.120

0.8028

1.04569

-0.103

-0.107

0.8474

1.04307

-0.088

-0.092

0.9016

1.03986

-0.067

-0.068

0.9529

1.03674

-0.039

-0.037

T=313.15 K

0.1016

1.07920

-0.056

-0.054

0.1512

1.07668

-0.075

-0.074

0.2028

1.07398

-0.087

-0.091

0.2274

1.07274

-0.097

-0.098

0.3037

1.06875

-0.115

-0.115

0.3526

1.06620

-0.126

-0.123

0.4042

1.06348

-0.135

-0.130

0.5044

1.05815

-0.147

-0.140

0.6042

1.05274

-0.148

-0.143

0.7037

1.04725

-0.138

-0.138

0.7446

1.04494

-0.129

-0.132

0.8028

1.04165

-0.114

-0.118

0.8474

1.03909

-0.098

-0.103

IJSER © 2013 http://www.ijser.org

International Journal of Scientific & Engineering Research, Volume 4, Issue 7, July-2013 1813

ISSN 2229-5518

0.9016

1.03594

-0.075

-0.076

0.9529

1.03287

-0.044

-0.042

Benzyl alcohol(1)+ Nitrobenzene(2)T=298.15 K

0.0409

1.19191

-0.031

-0.030

0.0996

1.18304

-0.066

-0.065

0.1481

1.17558

-0.084

-0.086

0.1988

1.16774

-0.098

-0.103

0.2561

1.15219

-0.113

-0.116

0.3509

1.13667

-0.129

-0.129

0.4356

1.12110

-0.136

-0.132

0.5275

1.11289

-0.135

-0.129

0.6459

1.10522

-0.121

-0.118

0.7207

1.09737

-0.104

-0.105

0.7613

1.08926

-0.095

-0.097

0.8257

1.08205

-0.081

-0.079

0.8562

1.07335

-0.069

-0.069

0.8934

1.06522

-0.053

-0.054

0.9409

1.05200

-0.034

-0.033

T=303.15 K

0.0409

1.18705

-0.036

-0.032

0.0996

1.17815

-0.063

-0.069

0.1481

1.17081

-0.086

-0.091

0.1988

1.16307

-0.104

-0.109

0.2561

1.14767

-0.123

-0.123

0.3509

1.13226

-0.138

-0.136

0.4356

1.11685

-0.15

-0.141

0.5275

1.10869

-0.148

-0.140

0.6459

1.10110

-0.136

-0.131

0.7207

1.09331

-0.120

-0.119

0.7613

1.08520

-0.106

-0.111

0.8257

1.07804

-0.092

-0.092

0.8562

1.06937

-0.077

-0.081

0.8934

1.06133

-0.064

-0.065

0.9409

1.04818

-0.043

-0.040

T=308.15 K

0.0409

1.18218

-0.039

-0.035

0.0996

1.17335

-0.066

-0.074

0.1481

1.16613

-0.095

-0.099

0.1988

1.15848

-0.116

-0.119

0.2561

1.14316

-0.132

-0.135

0.3509

1.12793

-0.154

-0.151

0.4356

1.11261

-0.164

-0.156

0.5275

1.10454

-0.165

-0.155

0.6459

1.09696

-0.149

-0.145

0.7207

1.08921

-0.132

-0.132

0.7613

1.08116

-0.118

-0.122

0.8257

1.07398

-0.098

-0.101

0.8562

1.06541

-0.087

-0.089

0.8934

1.05740

-0.072

-0.071

0.9409

1.04428

-0.045

-0.043

IJSER © 2013 http://www.ijser.org

International Journal of Scientific & Engineering Research, Volume 4, Issue 7, July-2013 1814

ISSN 2229-5518

T=313.15 K

0.0409

1.17735

-0.045

-0.040

0.0996

1.16867

-0.080

-0.086

0.1481

1.16148

-0.107

-0.115

0.1988

1.15393

-0.132

-0.137

0.2561

1.13876

-0.151

-0.155

0.3509

1.12364

-0.174

-0.172

0.4356

1.10842

-0.183

-0.177

0.5275

1.10038

-0.182

-0.173

0.6459

1.09282

-0.163

-0.157

0.7207

1.08509

-0.142

-0.141

0.7613

1.07710

-0.129

-0.129

0.8257

1.06994

-0.105

-0.105

0.8562

1.06137

-0.088

-0.091

0.8934

1.05341

-0.073

-0.072

0.9409

1.04036

-0.044

-0.043

Table 3

Molefraction(x1) of benzylalcohol, densities (ρ), sound velocities(u), isentropic compressibilities
s ), excess isentropic compressibilities

(k E )

and theoretical sound velocity values of
benzylalcohol (1) with benzene and substituted benzenes(2) at 303.15K and 313.15 K.

(Exp)

Benzylalcohol (1)+Benzene (2) T=303.15 K

s

(m.s-1)
0.0743 0.88290 1299 671 1297 1301 -13.8
0.1198 0.89170 1313 651 1305 1311 -24.8
0.1624 0.89977 1327 631 1324 1327 -34.5
0.2323 0.91280 1348 603 1327 1338 -45.7
0.2837 0.92220 1366 581 1338 1351 -54.3
0.3566 0.93524 1388 555 1353 1369 -60.9
0.4828 0.95710 1423 516 1381 1397 -64.1
0.5904 0.97502 1452 486 1406 1422 -61.6
0.6784 0.98922 1471 467 1428 1442 -54.1
0.739 0.99873 1483 455 1443 1456 -47.3
0.7997 1.00808 1494 444 1459 1469 -39.2

IJSER © 2013 http://www.ijser.org

International Journal of Scientific & Engineering Research, Volume 4, Issue 7, July-2013 1815

ISSN 2229-5518

0.8574

1.01682

1501

437

1474

1482

-29.0

0.8936

1.02219

1508

430

1484

1491

-23.9

0.9362

1.02842

1514

424

1496

1500

-16.4

0.9587

1.03165

1518

421

1502

1505

-12.9

T=313.15 K

0.0743

0.87242

1305

673

1294

1316

-16.6

0.1198

0.88137

1321

650

1302

1326

-29.7

0.1624

0.88957

1336

630

1320

1342

-40.4

0.2323

0.90280

1357

602

1328

1355

-51.7

0.2837

0.91234

1374

580

1346

1372

-59.3

0.3566

0.92561

1396

554

1381

1401

-65.9

0.4828

0.94788

1435

512

1403

1426

-71.6

0.5904

0.96614

1465

482

1421

1446

-69.1

0.6784

0.98061

1484

463

1432

1460

-61.0

0.739

0.99035

1495

451

1447

1474

-53.1

0.7997

0.99988

1503

442

1461

1487

-42.9

0.8574

1.00880

1511

434

1468

1495

-32.9

0.8936

1.01424

1512

431

1480

1504

-24.1

0.9362

1.02064

1515

427

1484

1509

-14.7

0.9587

1.02397

1515

425

1472

1514

-8.8

Benzylalcohol (1)+Toluene (2) T=303.15 K

0.1066

0.87666

1307

668

1306

1309

-21.6

0.1585

0.88591

1325

643

1315

1320

-32.1

0.2116

0.89540

1345

617

1325

1332

-42.2

0.2651

0.90496

1364

594

1335

1343

-49.0

0.3151

0.91392

1383

572

1345

1354

-56.2

0.3593

0.92185

1400

553

1353

1364

-59.9

0.4171

0.93223

1418

553

1365

1377

-66.1

0.5177

0.95034

1451

500

1387

1399

-68.4

0.6169

0.96825

1477

473

1410

1422

-67.3

0.7147

0.98593

1495

454

1434

1445

-58.7

0.7675

0.99550

1500

446

1448

1457

-51.7

0.8111

1.00340

1504

441

1460

1468

-42.8

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0.8644

1.01308

1508

434

1474

1481

-32.2

0.9062

1.02066

1506

432

1486

1491

-21.8

0.9556

1.02963

1505

429

1500

1503

-8.6

T=313.15 K

0.1066

0.86833

1317

663

1290

1316

-22.9

0.1585

0.87761

1336

638

1299

1327

-36.0

0.2116

0.88713

1356

613

1309

1339

-47.1

0.2651

0.89671

1374

591

1320

1351

-57.0

0.3151

0.90570

1393

569

1329

1362

-65.3

0.3593

0.91368

1409

551

1338

1371

-70.6

0.4171

0.92412

1428

531

1350

1384

-76.4

0.5177

0.94231

1459

499

1372

1407

-81.0

0.6169

0.96030

1485

477

1394.

1429

-79.7

0.7147

0.97809

1503

453

1417

1452

-69.0

0.7675

0.98770

1511

443

1430

1464

-61.2

0.8111

0.99568

1512

439

1441

1474

-51.1

0.8644

1.00539

1514

434

1455

1486

-38.7

0.9062

1.01300

1513

431

1466

1496

-27.2

0.9556

1.02196

1509

429

1480

1508

-11.6

Benzylalcohol (1)+ Bromobenzene(2) T=303.15 K

0.1277

1.42605

1187

497

1048

1187

-30.5

0.1722

1.40671

1213

483

1064

1204

-39.3

0.2221

1.38496

1242

468

1084

1223

-49.7

0.2627

1.36723

1267

456

1100

1238

-56.6

0.3032

1.34949

1291

445

1117

1253

-63.6

0.4133

1.30103

1359

416

1165

1294

-73.9

0.5233

1.25232

1414

399

1217

1335

-75.8

0.6544

1.19385

1466

390

1286

1384

-68.9

0.7249

1.16226

1486

391

1327

1411

-61.2

0.7669

1.14334

1493

392

1352

1426

-54.1

0.8091

1.12431

1498

396

1379

1442

-44.3

0.8430

1.10900

1502

400

1401

1455

-36.7

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0.8743

1.09482

1503

404

1422

1467

-27.9

0.9137

1.07695

1505

410

1450

1481

-16.3

0.9503

1.06030

1506

416

1476

1495

-7.0

T=313.15 K

0.1277

1.41354

1193

493

1039

1194

-34.2

0.1722

1.39446

1217

480

1055

1211

-48.0

0.2221

1.37303

1246

465

1075

1231

-60.5

0.2627

1.35556

1271

453

1091

1246

-67.3

0.3032

1.33807

1296

441

1107

1262

-73.9

0.4133

1.29031

1364

413

1155

1303

-84.5

0.5233

1.24222

1421

395

1206

1345

-87.5

0.6544

1.18451

1476

384

1274

1394

-80.2

0.7249

1.15328

1498

383

1313

1420

-70.0

0.7669

1.13459

1504

387

1338

1435

-63.5

0.8091

1.11577

1509

391

1364

1450

-55.2

0.843

1.10064

1510

395

1385

1462

-46.2

0.8743

1.08661

1511

400

1405

1474

-37.8

0.9137

1.06894

1512

406

1431

1488

-26.8

0.9503

1.05244

1512

413

1457

1501

-15.8

Benzyl alcohol (1)+ Chlorobenzene(2) T=303.15 K

0.1016

1.08961

1292

550

1273

1275

-21.1

0.1512

1.08691

1313

534

1285

1287

-32.1

0.2028

1.08405

1338

515

1298

1301

-43.5

0.2274

1.08270

1351

506

1304

1307

-50.1

0.3037

1.07844

1386

483

1323

1326

-62.2

0.3526

1.07570

1409

468

1335

1339

-69.6

0.4042

1.07279

1433

454

1348

1352

-76.9

0.5044

1.06710

1474

431

1374

1379

-83.9

0.6042

1.06134

1506

415

1401

1405

-82.4

0.7037

1.05553

1528

406

1428

1432

-75.1

0.7446

1.05311

1532

405

1439

1443

-67.0

0.8028

1.04963

1540

401

1456

1459

-56.3

0.8474

1.04695

1537

404

1468

1471

-45.4

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0.9016

1.04364

1533

407

1484

1486

-28.2

0.9529

1.04049

1470

445

1499

1500

-14.6

T=313.15 K

0.1016

1.07920

1306

543

1224

1258

-26.7

0.1512

1.07668

1328

527

1220

1260

-40.8

0.2028

1.07398

1355

507

1216

1262

-52.1

0.2274

1.07274

1366

500

1214

1262

-61.1

0.3037

1.06875

1402

476

1207

1265

-72.7

0.3526

1.06620

1424

463

1204

1267

-81.1

0.4042

1.06348

1448

448

1199

1269

-85.6

0.5044

1.05815

1490

426

1192

1272

-92.2

0.6042

1.05274

1523

410

1184

1275

-91.6

0.7037

1.04725

1549

398

1176

1279

-82.7

0.7446

1.04494

1555

396

1173

1280

-77.1

0.8028

1.04165

1559

395

1168

1281

-64.1

0.8474

1.03909

1557

396

1165

1283

-52.3

0.9016

1.03594

1550

402

1161

1284

-36.2

0.9529

1.03287

1541

408

1157

1285

-18.9

Benzyl alcohol (1) + Nitrobenzene(2) T=303.15 K

0.0409

1.18705

1480

385

1448

1448

-20.6

0.0996

1.17815

1512

371

1451

1452

-36.6

0.1481

1.17081

1539

361

1454

1455

-50.5

0.1988

1.16307

1561

353

1457

1459

-61.0

0.2561

1.14767

1590

345

1464

1463

-72.2

0.3509

1.13226

1618

337

1471

1469

-81.8

0.4356

1.11685

1633

336

1478

1475

-88.2

0.5275

1.10869

1639

336

1480

1481

-88.8

0.6459

1.10110

1628

343

1481

1489

-81.8

0.7207

1.09331

1613

352

1484

1494

-72.7

0.7613

1.08520

1603

359

1488

1497

-66.6

0.8257

1.07804

1583

370

1491

1501

-53.7

0.8562

1.06937

1578

376

1496

1504

-46.4

0.8934

1.06133

1565

385

1500

1506

-36.4

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0.9409

1.04818

1551

396

1508

1509

-22.5

T=313.15 K

0.0409

1.17735

1490

383

1410

1443

-26.9

0.0996

1.16867

1535

363

1391

1435

-45.1

0.1481

1.16148

1561

353

1376

1427

-59.6

0.1988

1.15393

1585

345

1360

1419

-71.1

0.2561

1.13876

1615

337

1346

1410

-82.6

0.3509

1.12364

1644

329

1319

1396

-97.8

0.4356

1.10842

1663

326

1297

1382

-103.4

0.5275

1.10038

1664

328

1268

1367

-104.8

0.6459

1.09282

1643

339

1232

1348

-97.9

0.7207

1.08509

1630

347

1211

1335

-88.8

0.7613

1.07710

1624

352

1202

1328

-78.8

0.8257

1.06994

1601

365

1186

1317

-63.7

0.8562

1.06137

1593

371

1181

1312

-57.8

0.8934

1.05341

1581

380

1173

1305

-47.4

0.9409

1.04036

1562

394

1166

1297

-30.4


Table 4 Thermal coefficient (α) and heat capacity (cp) for pure component liquids at temperatures

303.15K and 313.15 K.


Component/Temperature 303.15 313.15

Benzyl alcohol
α (kK-1) 0.7402 0.7456
Cp (J.mol-1.k-1) 224.35[17] 227.62[32] Benzene
α (kK-1) 1.1915 1.2048
Cp (J.mol-1.k-1) 137.4[17] 140.6[32] Toluene
α (kK-1) 1.2666 1.0612
Cp (J.mol-1.k-1) 153.4[17] 160.2[32] Bromobenzene
α (kK-1) 0.9048 0.8785
Cp (J.mol-1.k-1) 156.9[17] 157.3[32] Chlorobenzene

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α (kK-1)

0.9725

0.9673

Cp (J.mol-1.k-1)

150.6[17]

152.2[32]

α (kK-1)

Nitrobenzene

0.8198

0.8217

Cp (J.mol-1.k-1)

177.3[17]

173.8[32]

Table 5

RMSD of speed of sound (u) of benzylalcohol with benzene and substituted benzene at T=
303.15K and 313.15 K from different relations

RMSD 303.15 K 313.15 K



Benzyl alcohol (1) + benzene (2)

CFT

0.013

0.008

FLT

0.020

0.023

Benzyl alcohol (1) + toluene(2)

CFT

0.023

0.024

FLT

CFT

0.029

Benzyl alcohol (1) + bromobenzene(2)

0.035

0.045

0.034

FLT

0.107

0.119

CFT

Benzyl alcohol(1) + chlorobenzene(2)

0.046

0.137

FLT

0.048

Benzyl alcohol (1) + nitrobenzene(2)

0.194

CFT

0.066

0.151

FLT

0.068

0.209

Table 6

Coefficients Ai of Redlich-Kister equation 6 and the corresponding standard deviations (σ) of all
the systems

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Temperature Function A0 A1 A2 σ(VE)

Benzyl alcohol (1)+benzene (2)
289.15 K VE -0.295 -0.088 0.178 0.003
303.15 K VE -0.323 -0.111 0.114 0.003
308.15 K VE -0.325 -0.146 -0.102 0.004
313.15 K VE -0.376 -0.118 -0.131 0.003
303.15 K κsE -252.1 -252.1 -1.55 2.9
313.15 K κsE
-294.3 12.6 55.82 1.3
Benzyl alcohol (1)+Toulene(2)
289.15 K VE -0.311 -0.115 0.002 0.004
303.15 K VE -0.342 -0.135 -0.044 0.004
308.15 K VE -0.364 -0.144 -0.124 0.005
313.15 K VE -0.408 -0.153 -0.181 0.004
303.15 K κsE -284.6 -20.77 -20.77 1.9
313.15 K κsE -332.6 -44.61 88.15 1.4
Benzyl alcohol (1)+bromobenzene (2)
289.15 K VE -0.388 -0.123 0.014 0.002
303.15 K VE -0.414 -0.138 -0.025 0.002
308.15 K VE -0.440 -0.147 -0.107 0.004
313.15 K VE -0.484 -0.147 -0.145 0.003
303.15 K κsE -327.6 11.13 147.19 3.2
313.15 K κsE -357.5 -13.60 41.63 1.2
Benzyl alcohol (1)+chlorobenzene (2)
289.15 K VE -0.434 -0.111 -0.105 0.003
303.15 K VE -0.472 -0.138 -0.142 0.003
308.15 K VE -0.510 -0.144 -0.214 0.003
313.15 K VE -0.560 0.152 -0.269 0.003
303.15 K κsE -338.6 -65.97 87.86 1.2
313.15 K κsE -373.47 -67.21 24.1 1.2

Benzyl alcohol (1)+nitrobenzene (2)

289.15 K

VE

-0.523

0.086

-0.196

0.003

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303.15 K VE
308.15 K VE
313.15 K VE
303.15 K κsE
313.15 K κsE

0.00

-0.05

-0.10

0.0 0.2 0.4 0.6 0.8 1.0

X

1

Figure 1

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0.00

-0.02

-0.04

-0.06

-0.08

-0.10

-0.12

0.0 0.2 0.4 0.6 0.8 1.0

X

1

Figure 2

0.00

-0.04

-0.08

-0.12

0.0 0.2 0.4 0.6 0.8 1.0

x1

Figure 3

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0.00

-0.05

-0.10

-0.15

0.0 0.2 0.4 0.6 0.8 1.0

X

1

Figure 4

0.00

-0.05

-0.10

-0.15

-0.20

0.0 0.2 0.4 0.6 0.8 1.0

X

1

Figure 5

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0

-20

-40

-60

-80

0.0 0.2 0.4 0.6 0.8 1.0

x1

Figure 6

0

-20

-40

-60

-80

0.0 0.2 0.4 0.6 0.8 1.0

x1

Figure 7

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0

-20

-40

-60

-80

0.0 0.2 0.4 0.6 0.8 1.0

x1

Figure 8

0

-20

-40

-60

-80

-100

0.0 0.2 0.4 0.6 0.8 1.0

x1

Figure 9

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0

-20

-40

-60

-80

-100

-120

0.0 0.2 0.4 0.6 0.8 1.0

x1

Figure 10

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