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Chapter 6 Acoustic Non-linearity Parameter B/A of Binary Liquid Mixtures-I1
6.1 Introduction
The study of acoustic non-linearity parameter B/A in five binary liquid
mixtures at two different temperatures using Tong and Dong theory has formed
the subject matter of Chapter 5. This chapter (Chapter 6) deals with the
evaluation of B/A in seven binary liquid mixtures using four different theories
and making use of the ultrasonic velocity values at high pressures reported in the
literature [l-51. The variation of B/A with mole fraction of one component was
studied. Also, the excess parameters viz., excess B/A and excess adiabatic
compressibility were computed and were made use of in explaining the molecular
interactions existing in the liquid mixtures. Seghal [6] has reported a set of
relations involving the parameter BIA for the determination of the molecular
properties such as internal pressure, cohesive energy, effective Van der Waal's
constants, distance of closest approach of molecules, diffusion coefficient and
rotational correlation time of pure liquids. In the present work, these relations
applicable to pure liquids were extended to the case of binary liquid mixtures.
The molecular properties of five binary liquid mixtures at room temperature, those
of one binary liquid mixture at two temperatures and one binary liquid mixture at
three different temperatures were studied.
The binary liquid mixture systems chosen for the present study and the
high-pressure ultrasonic velocities of which are reported in the literature[l-51 are
1. Benzene + Aniline
2. Chlorobenzene + Aniline
3. Cblorobenzene + Bromobenzene
4. Toluene + o-Xylene
5. Toluene + Aniline
6. Benzonitrile + Nitrobenzene
7. Benzene + Nitrobenzene
6.2 Theory
In the first method to calculate BIA, Beyer's thermodynamic equation [7]
was used. This equation is
where C is the sound velocity, p the density, P the coefficient of thermal
expansion, T the absolute temperature and C, the specific heat at constant
pressure. The factors are the variations of sound velocity with
pressure and temperature respectively. The contribution of the second term in
equation[l] to BIA is very small and hence it is neglected. The values of - (FIT for the systems benzene + aniline, benzene + nitrobenzene, chlorobenzene +
aniline and chlorobenzene + bromobenzene are obtained from the literature[l-31.
For the other three systems (21, was calculated as follows
Nomura et al. [8] have derived a relation between ultrasonic speed C and
isothermal compressibility KT as
Integration of equation[6.2] between the limits of atmospheric
pressure(0.1 MPa) and any higher pressure p gives
In KT[p] = l n K ~ [o. 1 MPa] -2 in C[p] + 2 In [O. 1MPaI-
KT [p-0. I MPa] ------------------ (6.3)
Isothermal compressibility at different pressures of binary mixtures was
calculated using equation 6.3. A graph of I & @ ) against pressure p was drawn, which
was a stmight line and h m the slope the value of [aK f ' lap] was calculated.
Substituting the value of [aK r' 113 p] in equation 6.2 ( a ~ I ap)T was calculated.
In the second method to determine BIA, Tong Dong equation [9] for
evaluation of B/A values of pure liquids was extended to binary liquid mixtures [lo].
The details of Tong Dong theory is given in Section 5.2 of Chapter 5. The
temperature and pressure coefficients of sound velocity were theoretically
calculated using Tong and Dong method [ I 11 as follows.
The symbols have same meaning as that in Section 5.2 of Chapter 5.
These values were substituted in equation 1 together with other thermo dynamical
parameters for binary mixtures to get B/A values. This is the third method.
Haurmi Endo [12] obtained the following equation for calculating B/A
values of pure liquids using adiabatic compressibility, Ks.
Knowing isothermal compressibility K=(p) at different pressures kom
equation 6.5, adiabatic compressibility at different pressures Ks@) can be obtained
using the equation = y . The ratio of specific heat y was obtained by
using the method of Khanwalkar [13]. y is assumed to be a constant with change in
pressure. A graph of I&@)-' against pressure p was plotted which was a straight line
and kom the slope of the graph - was obtained.
The excess non-lineanity parameter, (B/A)~ for binary liquid mixtures is given
by [lo1
(B/A)~ = (BIA),,, - (B/A),d ------------------ (6.7)
where (BIA),,, is the non-linearity parameter of the mixture and is that
obtained from the ideal mixture relation
(B/A)id=x~ (B/A)t + xz(B/A)2 ------------------ (6.8)
where X I and x2 are respectively the mole fractions of the first and second liquids .
(BiA)l and (B/A)* are the B/A values of the first and second pure liquids
respectively.
The various molecular parameters of binary liquid mixtures were
calculated using Sehgal's relations given below
Internal pressure n,= pc2 ( B I A + ~ )
MC2 Cohesive energy M = (6.10)
(BIA+l)
pc2v,2 Van der Waal's Constants a = -
(BiA+l)
Distance of closest approach of molecules
Difision coefficient
Correlation time T' = - ( B I A + 1) ----- (6.15) I where M is the molecular weight of the binary mixture calculated by ideal mixture
relation. M = XIMI+X~MZ in which XI and xz are the mole W o n s and MI, Mz are the
molecular weight of the first and second pure liquid respectively. VI is the molar
volume given by Vl = where p is the density of the mixture, k is the Boltzman's P
constant, R the universal gas constant and .q is the viscosity of the mixture. The
viscosity of the mixture was calculated by using the equation[l4] qx = x , ~ , f : + x , ~ , f:
where qland qz are the viscosities of the two pure liquids. The above molecular
parameters given in equations 6.9-6.15 were determined by substituting molecular
weight, density, viscosity, molar volume and BJA values ofbinary liquid mixtures.
6.3 Results and Discussions
The non-linearity parameter BIA of seven binary liquid mixtures
calculated using the four different methods are given in table 6.1.
It is seen that (table 6.1) BIA values of all the mixtures calculated using
the second and fourth methods agree with the values obtained by using Beyer's
method (equation 6.1) which is considered to be the most accurate one [I 53.
Table 6.1 Mole fraction (x) of second component, adiabatic compressibility ( K ) and non-linearity parameter (BIA) of binary mixtures determined using Beyer(a), Tong Dong(b), Tong Dong & Beyer(c) and Haurmi Endo(d) methods
Benzene + Nitrobenzene at 293.15K
512.0 10.81 13.97 17.60 460.2 10.84 16.22 20.00 420.7 10.53 14.66 18.04 383.8 10.44 14.74 17.97
Benzene + Nitrobenzene at 303.15K
7126 11.54 10.79 13.81 617.0 10.99 11.73 14.64 574.4 10.78 12.31 14.88 487.5 10.63 13.62 15.64 449.2 10.59 12.65 15.03 405.0 10.54 12.98 15.22
Benzene + Nitrobenzene at 313.15K 769.3 11.69 9.80 12.34 665.9 10.93 10.54 12.98 59 1.5 10.71 10.98 13.35 519.4 10.78 12.22 14.59 475.7 10.63 11.57 13.81 429.6 10.85 11.64 13.82
Benzene + Aniline at 298.15K 675.4 11.60 11.43 14.47 615.8 11.34 11.87 14.68 562.5 11.25 12.18 14.79 511.9 10.85 12.6 15.06 471.1 10.86 12.97 15.31 431.7 9.94 13.28 15.53 404.5 10.66 13.47 15.64 368.1 10.63 13.63 15.64
Cblorobenzene + Aniline at 298.15K 5h4.4 11.45 12.98 16.13 512.1 11.02 12.92 15.58 490.6 11.23 12.96 15.45 462.3 11.18 13.02 15.36 430.7 11.20 13.14 15.36 405.1 10.53 13.31 15.43 368.1 10.63 13.63 15.64
Chlorobenzene + Bromobenzene at 303.15K 733.6 11.19 12.09 14.66 706.3 11.22 11.88 14.36 685.0 11.13 11.68 14.08 665.8 11.05 11.63 13.94 655.0 11.19 11.66 13.91 644.3 11.21 11.75 13.94
Benwnitrile + Nitrobenzene at 298.1 5K 498.16 11.37 12.74 479.43 11.50 12.97 473.58 11.55 13.04 470.30 11.57 13.08 468.50 11.59 13.12 463.11 11.64 13.20 457.69 11.69 13.27 451.93 11.92 13.36 446.25 11.79 13.44 440.51 11.85 13.52 435.04 11.90 13.61 432.36 11.93 13.65 430.66 12.02 13.61 419.85 12.08 13.85 410.28 12.21 14.04 392.72 12.47 14.41
Benzonihile + Nitrobenzene at 303.15K 513.03 11.40 12.05 493.13 1 1.44 12.24 487.01 11.45 12.3 483.62 11.46 12.33 481.76 11.46 12.36 476.63 11.47 12.41 470.85 11.48 12.48 464.73 11.49 12.54 459.45 11.51 12.57 453.74 11.52 12.65 447.44 11.53 12.73 444.66 11.54 12.76 442.71 11.54 12.78 432.69 11.56 12.91 422.13 11.58 13.05 403.87 11.63 13.30
Toluene + Aniline at 303.15K 705.21 11.99 11.67 632.62 11.74 11.61 567.50 11.54 11.37 502.20 11.42 10.99 441.03 11.36 10.53 384.03 10.52 10.04
Toluene + o-Xyline at 303.15K 705.21 12.01 11.67 696.80 12.00 11.90 682.73 12.01 12.17 672.34 12.00 12.45 660.34 11.99 12.76 649.24 11.98 13.1 1
Hence Tong Dong and Haurmi Endo methods may be considered to be more
accurate compared to the third method for the determination of B/A of binary
liquid mixtures. The large deviation of B/A values obtained using the third
approach, which is based on both Tong Dong and Beyer methods, from the values
obtained using Beyer equation (equation 1) might be resulting from the
inaccuracy of the expressions used for calculating temperature and pressure
coefficients of sound velocity (equations 6.4 and 6.5).
In benzene + aniline and benzene + nitrobenzene systems, as the mole
fractions of benzene decreases, density and sound velocity increases and hence
adiabatic compressibility decreases (table 6.1). It is found that the BIA values at
all temperatures decrease as the mole &tion of benzene is decreased. In
chlorobenzene + Aniline system also. the B/A values and adiabatic compressibility
shows a decreasing tendency as the mole fraction of chlorobenzene is decreased.
But in chlorobenzene t bromobenzene system, the variation of B/A and
compressibility with mole fraction of chlorobenzene is very small. In toluene +
aniline and toluene -t o-xylene systems, as the mole fraction of toluene is
decreased, the density and sound velocity increase and hence compressibility
decreases. It may be inferred that compressibility and BIA exhibit the same type
of variation with changes in mole fraction of one of the components of the liquid
mixtures. Therefore, just like compressibility, BIA may be considered as quantity
that determines the hardness of a liquid [12].
But in benzonitrle + nitrobenzene system, a contradictoxy observation was
observed. In this system, BIA and compressibility showed an opposite behaviour i.e.,
BIA increases while compressibility decreases with the decrease in the mole fraction of
nitrobemme. This may be explained on the basis of molecular interaction between
unlike molecules as follows.
The dipole moment of benzonitrile is 4.1 8 Debey and that of nitrobenzene is
4.22 Debey. So, a benmnitrile + nitrobenzene system is higbly polar in nature.
Therefore a strong dipole-dipole interaction is present in this system. Due to this
interaction the molecules are tightly packed and this system is an approximate
example of hard sphere binary liquid mixtures [12]. In the case of binary
mixtures of hard spheres in which the molecular diameters differ by a small
amount (molecular radius of benzonitrile is 2.129 A and that of nitrobenzene is
2.131 A), Harumi Endo [12] pointed that B/A is closely connected with the degree
of packing of hard spheres or hardness of the bulk of the liquid system. In the
present system, as the mole fraction of nitrobenzene increases, the degree of
packing increases and hence BIA increases. But the compressibility, which is
inversely depending on density and ultrasonic velocity decreases since, both
density and ultrasonic velocity increase with mole fraction of nitrobenzene.
The variation of the excess non-linearity parameter ( B I A ) ~ and the excess
compressibility I&E vs mole fraction of second component are shown in figures
6.1 and 6.2. It is seen that the variations of ( B I A ) ~ follow the same trend as that of
K:. The excess compressibility is reported to be a quantity which is proportional
to the strength of interaction between unlike molecules [16].
Mole fraction of second component
Figure 6.1 Excess compressibility vs mole fraction of second component in the binary mixture
Mole fraction of second component
Figure 6.2 Excess BIA vs mole fraction of second components in the binary mixtures
According to Fort and Moore [17], a negative excess compressibility is an
indication of strong molecular interaction in the liquid mixtures while a positive
value indicates a weak interaction attributable to dispersion forces. Also, the
magnitude of the excess function depends on the relative strength of interaction [17].
The types of interactions between components of different mixtures are charge transfer,
hydrogen bonding dipole induceddipole and dipoledipole interactions. The origin of
molecular interactions existing in different binary liquid mixtures in the present study is
explained as follows.
In benzene + nitrobenzene system, due to the electron withdrawing nature
of NO2 group in nitrobenzene, a slight positive charge is developed in the benzene
ring and due to the resonance effect, this positive charge is delocalised which can
interact with the x electron cloud of the other benzene ring as shown below.
Also, the positive charge in nitrogen can interact with the n electron cloud
of other benzene rings resulting in a dipole-induced dipole interaction which may
be considered to be strong. This conclusion supports the results in figures 6.1 and 6.2.
In benzene + aniline system, the unshaded electron pair of nitrogen in aniline can
interact with the delocalised n orbitals of the benzene ring due to resonance. As a
result a slight positive charge is developed in the nitrogen of aniline which can
interact with the x electron of benzene as shown below.
This interaction is a sort of dipole-induced-dipole interaction which is
expected to be strong and which again supports the results shown in figures 6.1
ant1 6.2.
In chlorobenzene + aniline system, (BIA)~ and K S ~ have positive values
which indicates relatively weaker molecular interaction [I71 existing in the liquid
mixture.
Also, due to resonance effect, a slight positive charge is developed in the
nitrogen atom of aniline and the C1 atom of chlorobenzene. This causes a
repulsive interaction, which is very weak (figures 6.1 and 6.2).
In chlorobenzene + bromobenzene system also, (BIA)~ and K S ~ have
positive values. In this system, due to resonance effect, a small positive charge is
developed in the C1 atom of chlorobenzene and the Br atom of bromobenzene.
Due to these small positive charges, a weak repulsive interaction as represented
below may occur in the liquid mixture.
In benzonitrile + nitrobenzene system, the phenyl group of benzonitrile
can exhibit two phenomena-negative inductive effect and resonance [la, 191 Due
to the inductive effect, the nitrile carbon becomes more electron deficient which
facilitates molecular interaction between nitrile carbon of benzonitrile and the two
oxygens of nitrobenzene and between nitrile nitrogen of benzonitrile and nitrogen
of nitrobenzene shown below.
This is a sort of dipole-dipole interaction, which is expected to be strong.
On the other hand there is a resonance effect due to the delocalisation of electron
cloud in the phenyl group of benzonitrile [18]. Hence the electron density of
nitrile carbon can increase by delocalising the partial positive charge on the nitrile
carbon which should retard the molecular interaction between benzonitrile and
nitrobenzene. Thus these two phenomena have opposing effects. But fkom the
strong molecular interaction a seen in figures 6.1 and 6.2, it may be inferred that
negative inductive effect dominates over the resonance effect.
In toluene + aniline system, due to resonance effect, a positive charge is
developed in the nitrogen of aniline which can interact with the R electron cloud
of benzene ring in toluene as shown below. This is a kind of strong dipole-dipole
interaction which is expected to be strong.
In toluene + o-xylene system, due to positive inductive effect of the two
methyl substituents, there is an increase in the negative charge density in the
benzene ring of o-xylene compared to the charge density in the benzene ring of
toluene. Hence there is a possibility of repulsive interaction between the n electron
clouds of o-xylene and toluene as shown below. This repulsive interaction is a
sort of weak interaction between unlike molecules.
From the above discussion, it may be inferred that a negative value of
(BIA)~ indicates strong interaction and a positive value of (BIA)~ indicates a
relatively weak interaction between unlike molecules. This is in accordance with
the reported results [17] based on excess compressibility.
The molecular properties of the liquid mixtures calculated using BIA
values, are shown in table 6.2.
Table 6.2 Mole W o n of second component(x), internal pressure (xi), cohesive energy (AA) Van der Waal's constants (a & b) distance of closest approach (d) diffusion coefficient 0) and rotational correlation time (7') of binary mixtures
Benzene + Nitrobenzene at 293.15K -60.132 0.954 0.0687 3.791 -75.241 1.232 0.0748 3.900 -86.071 1.456 0.0791 3.974 -97.212 1.687 0.0826 4.031 -1 12.499 2.038 0.0876 4.1 11 -127.241 2.385 0.0916 4.173
Benzene + Nitrobenzene at 303.15K -56.584 0.905 0.0675 3.768 -69.697 1.147 0.0735 3.877 -8 1.936 1.395 0.0786 3.964 -90.640 1.581 0.0819 4.020
-106.274 1.935 0.0873 4.116 -121.032 2.275 0.0914 4.169
Benzene + Nitrobenzene at 3 13.15K -52.589 0.8490 0.06566 3.735 -65.886 1.0917 0.07248 3.859 -77.268 1.3220 0.07769 3.950 -88.761 1.5560 0.08171 4.017 -101.360 1.8520 0.08690 4.099 -112.677 2.1310 0.09090 4.163
Benzene + Aniline at 298.1513 -58.947 0.939 0.0680 3.785 -66.116 1.056 0.0708 3.829 -73.128 1.173 0.0728 3.866 -83.282 1.340 0.0751 3.906 -09.648 1.464 0.0766 3.931 -107.494 1.742 0.0790 3.972 -107.925 1.756 0.0793 3.978 -119.467 1.957 0.0809 4.004
Chlorobenzene + Aniline at 298.15K -79.699 1.488 0.0849 4.068 7.086E-09 -88.827 1.601 0.0841 4.055 4.158E-09 -90.550 1.606 0.0831 4.040 3.363E-09 -94.862 1.654 0.0826 4.031 2.747E-09 -100.294 1.715 0.0819 4.020 2.23OE-09 -1 11.457 1.872 0.0820 4.021 1.872E-09 -1 19.098 1.990 0.0823 4.027 1.491E-09
Chlorobenzene + Bromobenzene at 303.15K -79.554 1.490 0.0849 4.0685 7.67964E-09 -81.551 1.541 0.0861 4.087 7.343E-09 -84.766 1.615 0.0873 4.107 6.649E-09 -87.400 1.677 0.0884 4.124 6.205E-09 -89.050 1.719 0.0892 4.136 5.805E-09 -9 1.746 1.782 0.0901 4.150 5.434E-09
Benzonitrile + Nitrobenzene at 298.15K -9 1.44 1.72 0.088 4.11 4.28E-09 -93.95 1.77 0.088 4.12 4E-09 -94.75 1.78 0.088 4.12 3.91E-09 -95.21 1.79 0.088 4.12 3.87E-09 -95.45 1.80 0.088 4.12 3.83E-09 -96.20 1.81 0.088 4.12 3.75E-09 -96.94 1.82 0.088 4.12 3.67E-09 -96.40 1.81 0.088 4.12 3.59E-09 -98.57 1.85 0.089 4.13 , 3.52E-09 -99.41 1.87 0.089 4.13 3.44E-09 -100.21 1.88 0.089 4.13 3.37E-09 -100.63 1.89 0.089 4.13 3.34E-09 -100.35 1.89 0.089 4.13 3.3E-09 -102.39 1.92 0.089 4.14 3.17E-09 -103.75 I .95 0.089 4.14 3.04E-09 -106.22 1.99 0.090 4.14 2.81E-09
Benzonitrile 4- Nitrobenzene at 303.15K -89.14 1.68 0.087 4.1 1 4.87E-09 -92.40 1.74 0.088 4.12 4.56E-09 -93.46 1.76 0.088 4.12 4.47E-09 -94.05 1.77 0.088 4.12 4.43E-09 -94.40 1.78 0.088 4.12 4.38E-09 -95.33 1.80 0.088 4.12 4.29E-09 -96.42 1.82 0.088 4.12 4.21E-09 -97.55 1.84 0.089 4.13 4.12E-09 -98.54 1.86 0.089 4.13 4.04E-09 -99.71 1.88 0.089 4.13 3.96E-09 - 100.97 1.90 0.089 4.13 3.89E-09 -101.53 1.91 0.089 4.14 3.85E-09 -101.98 1.92 0.089 4.14 3.81E-09 -104.11 1.96 0.089 4.14 3.67E-09 -106.50 2.00 0.090 4.14 3.52E-09 - 1 10.89 2.08 0.090 4.15 3.27E-09
Toluene + Aniline at 303.15K 109,14:':! L -6283 1.26 0.084 4.06 124.08 -70.96 1.36 0.084 4.06 140.51 -78.62 1.45 0.084 4.05 160.29 -87.80 1.58 0.083 4.04 183.41 -98.40 1.71 0.083 4.04 226.13 -118.92 2.01 0.083 4.04
. . . Toluenc + o-Xyline at 303.15K 108.96 ' ' - 6 G 3 1.26 0.084 4.06 110.38 -65.99 1.34 0.088 4.1 1 112.62 "'L68.77 1.44 0.091 4.16 114.45 -71.33 1.54 0.094 4.21 116.59 '-74.12 1.65 0.097 4.26 118.70 -76.92 1.76 0.101 4.31
In all the seven systems, the internal pressure (n,) increases with increase in mole
fraction of one of the components. Internal pressure is the resultant of the forces
of attraction and of repulsion between molecules in a liquid medium, and is a
measure of.&&tbriti&~~f.;forces of dispersion, repulsion, ionic and dipolar
interactihns that contribute to the overall cohesion of the liquid. An increase in
the inr&al.pid&e- in all the seven liquid mixtures with increase in mole
fractionsbf one component shows that the resultant molecular interactions change
in such h way ak to increase the cohesion of the liquid mixtures. The magnitude
of the change in-internal pressure with increase in the mole fraction of
nitrobenzene' in benzene + nitrobenzene, aniline in benzene + aniline,
nitrobenzene in benzonitrile + nitrobenzene and aniline in toluene + aniline
systems is quite large compared to the corresponding changes in the other two
systems. This also points to the presence of strong interactions in benzene +
nitrobenzene, benzene + aniline, benzonitrile + nitrobenzene and toluene + aniline
systems.
Coheslve energy(AA) is the measure of the total molecular cohesion and it
represents the total strength or stiffness of the solvent structure [20:. In all the
seven binary liquid mixtures, the magnitude of the cohesive energy increases with
increase in the mole fractions of one component. The magnitude of the change in
cohesive energy, as the mole fractions of one component is increased, is much
larger in benzene + nitrobenzene, benzene + aniline, benzonitrile + nitrobenzene
and toluene + aniline systems compared to that for the other two systems The
study of variation cohesive energy with temperature in the case of benzene +
nitrobenzene systems show that as temperature increases the cohesive energy
decreases.
The effective Van der Waal's constants 'a' and 'b' represent respectively
a measure of the attractive forces between molecules md,the.effective volume of
a molecule. In the present study, the constants 'a' and 'b' increased with increase
in the mole fractlon of one component. The increase in the value of constant 'a'
indicates that the attractive forces in the binary liquid mixtures increase with the
increase in mole fractlon of one component. The variation in the values of the
distance of closest approach of molecules also have the same nature of variation
as those of a and b. It was found that as temperature increased the distance of
closest approach decreased.
It was found that diffusion coefficient (D) decreased with increase in the
mole fraction of one component in all the seven binary liquid systems (table 6.2)
but rotational correlation time (t') increased. The correlation time is the average
time between molecular collisions and is the length of time for which the
132
molecule can be considered to be in a particular state of motion [21]. In the
present study, the increase in correlation time with increase in the mole fraction of
one component lead to the conclusion that molecular motions in the liquid
mixtures were less rapid which indicated the presence of attractive forces between
unlike molecules.
6.4 Conclusion
Acoustic non-linearity parameter BIA in seven binary liquid mixtures was
cahxlated using four different methods. The variation of B/A with mole fraction
of one component is discussed. It is concluded that (B/A)~ is a useful parameter
to study molecular interpctions in binary liquid mixtures. Using BIA values of
binary mixtures, the characteristic molecular parameters were calculated and the
':.sr - variations of these parameters with increase in the mole fraction of one
component were studied.
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