American International Journal of
Research in Science, Technology,
Engineering & Mathematics
Available online at http://www.iasir.net
ISSN (Print): 2328-3491, ISSN (Online): 2328-3580, ISSN (CD-ROM): 2328-3629
AIJRSTEM is a refereed, indexed, peer-reviewed, multidisciplinary and open access journal published by
I. Innovation and Research (IASIR), USA
International Association of Scientific
(An Association Unifying the Sciences, Engineering, and Applied Research)
Ultrasonic Studies on Interionic Interactions of KSCN in 2-Ethoxyethanol
+ Water Mixture at Varying Temperatures
M1. Surekha, H. R2. Shivakumar
Department of Chemistry, KVG College of Engineering
(Affiliated to Visvesvaraya Technological University),
Sullia, Karnataka State, INDIA
Abstract: Density (d), ultrasonic velocity (U) and viscosity (η) of potassium thiocyanate (KSCN) at different mole
fractions of 2-ethoxyethanol has been measured at 288.15, 298.15, 308.15 and 318.15K. An ultrasonic
interferometer working at 2 MHz was used to measure the sound velocity. Using the experimental data, adiabatic
compressibility (βad), inter molecular free length (Lf), acoustic impedance (Z), Relative association (RA), apparent
molar compressibility (ɸk), apparent molar volume (ɸv), limiting apparent molar compressibility (ɸ0k), limiting
apparent molar volume (ɸ0v), association constant (Sk and Sv) and solvation number were computed. The observed
variation of these parameters with respect to electrolyte concentration and temperature signifies the presence of
ion- solvent and solvent-solvent interactions. Masson’s and Gucker’s equation has been verified. The maxima in
ultrasonic velocity and minima in adiabatic compressibility are observed at X 2EE= 0.0136 elucidating complex
formation in this composition. The positive Sk values suggests structure breaking property of KSCN.
Keywords: Potassium thiocyanate, 2-ethoxyethanol, ultrasonic velocity, free length and solvation number.
I. Introduction
Electrolytes plays an important role in biological sciences, engineering, Geographic’s etc. [1-3]. Knowledge of
the thermo acoustic properties of the electrolytes and solvents is of high interest in view of their wide applications
in science and industrial process. During the last two decades, the ultrasonic velocities, density and viscosities of
the solutions of mixed solvents have been extremely investigated by many workers [4-7]. The acoustic parameters
are utilized in chacterizing of the structure and properties of solutions. These information are proven to be very
useful in obtaining the knowledge regarding various inter ionic interactions [8]. Potassium thiocyanate (KSCN)
is also known as sulphocyanide or rhodamide and is soluble in water and alcohol. Since it finds a number of
industrial and biological applications [9, 10] its interactions in presence of different solvent mixtures is very
importantShivakumar et al [11] reported an account of the investigation on solvation behavior of potassium
thiocyanate in DMSO, DMF and their aqueous solutions at 288 – 313K temperatures. He has used ultrasonic
parameters to explore ion- solvent and solvent – solvent interaction at varying conditions. More subtle effect arises
with highly structured solvents like water due to strong solvation reducing the effective quantity of free solvent
molecules. A good example of these effects is the hydrophobic interaction or bonding that is often evoked in
aqueous biological systems. Mixed aqueous-organic or totally organic reaction media have been utilized by
organic chemist to synthesize many valuable drugs and other compounds by reaction paths that involves ionic
intermediate or products. 2-ethoxyehanol (1-ethoxy-2-hydroxyl; ethane) is used as a co-solvent since the
substituted alcohols play very important role in solvation process. It belongs to alkoxy ethanol groups, which are
the perfect solvents of many substances. 2-ethoxyethanol is widely used as an ingredient in cleaning
agent/disinfectants/cosmetics [12]. In literature the information available regarding the acoustic behaviourof
KSCNin 2-ethoxy ethanol + water mixtures are very scanty. In this investigation we attempted to reveal the
interionic interactions taking place in the system involving KSCN in 2-ethoxyethanol+water at 288.15, 298.15,
308.15 and 318.15K.
II. Experimental
2-ethoxyethanol (analytical grade, Merck) was used without further purification. Doubly distilled water was used
for preparing various molefractions (ranging from 0.0000 to 1.0000) of 2-ethoxyethanol.The recrystallized
electrolyte potassium thiocyanate (Merck - AR) was dried at 100-120°C in vacuum for 24 hour prior to use.
Potassium thiocyanate (KSCN) is weighed in electrical digital balance (ER-180,Afcoset Balances, Bombay) with
a precision of ±0.3% and dissolved in solvent mixture to prepare the desired concentration. A digital multi
frequency ultrasonic interferometer (M-81S, Mittal New Delhi) at 2 MHz, with a measuring frequency tolerance
at 0.03% has been used for velocity measurement. A thermostat (Kumar Make, Bombay) with an accuracy of
AIJRSTEM 19-234; © 2019, AIJRSTEM All Rights Reserved
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Surekha et al., American International Journal of Research in Science, Technology, Engineering & Mathematics,26(1), March-May 2019,
pp. 179-187
±0.01°C was used to maintain the temperature of the cell at 288.15, 298.15, 308.15 and 318.15K. A pyknometer
(10 cc capacity) is used to determine the density of all the solutions.
III. Results and Discussions
Thermodynamic properties such asadiabatic compressibility (βad), inter molecular free length (Lf), acoustic
impedance (Z), Relative association (RA), apparent molar compressibility (ɸk), apparent molar volume (ɸv),
limiting apparent molar compressibility (ɸ0k), limiting apparent molar volume (ɸ0v) and solvation number (Sn)
have been calculated for potassium thiocyanate in aqueous and mixed solvent mixture at different
temperatures.The following equations were used for the calculations [13]
U =λxF
…….. (1)
βad = 1/U2d
……..(2)
Lf = K√ βad
…….. (3)
Z =Uxd
…….. (4)
RA = (d/d0) (U0/U)1/3
……..(5)
Φk = 1000(d0 βad - dl β0ad)/dld0 + M βad / dl …….. (6)
Φv = M/d0 – 1000(d-d0)/Cd0
…….. (7)
…….. (8)
Sn = (n1/n2)(1- βad / β0ad)
where dl, d0 and U, U0 are the densities and ultrasonic velocities of solution and solvent respectively. λ is the
wavelength and F is the frequency of ultrasonic wave. M is the molecular weight of the solute, β0ad and βad are
the adiabatic compressibilities of solvent and solution, K is the Jacobson constant, n 1 and n2 are the number of
moles of the solvent and solute respectively.
Ultrasonic velocity (U):
The computed values of ultrasonic velocity (U) for Potassium thiocyanate in different 2-ethoxyethanol + water
mixtures at 288.15, 298.15, 308.15 and 318.15 K presented in Table 1. It is observed that the variation of ultrasonic
velocity with respect to concentration of KSCN depends on mole fraction of 2-ethoxyethanol. The increase in
ultrasonic velocity with increase in concentration of the solute in the solution implies greater association of the
molecules [14]. It is observed that the ultrasonic velocity increases initially with addition of co-solvent and found
maximum at X2EE = 0.0136 and later decreased at co-solvent rich region. This may be due to enhancement of
water structure by the added co-solvent increasing the effective ionic size [15]. The maxima at X2EE= 0.0136 have
been attributed to the formation of hydrophobic aggregation resulting in labile clusters [16].Beyond this mole
fraction sound velocity decreases indicating the weak solvent- solvent interaction. Lowering of ultrasonic velocity
may be due to decrease in the dielectric constant of solvent mixture. A gradual increase in the velocity with rise
in temperature was observed up to X2EE= 0.0052 as rise in the thermal energy weakens the ion-solvent interactions.
However beyond this mole fraction reverse trend was observed.
Adiabatic Compressibility (βad) and density:
The change in the structural arrangement of molecules in a mixture is given by adiabatic compressibility. The
variation of βadwith concentration of KSCN in 2-ethoxyethanol and water mixture is presented in Table 1. The
adiabatic compressibility is found to decrease with increase in concentration of KSCN in different compositions
of 2-ethoxyethanol + water mixtures. This may be attributed to increasing electrostrictive compression of water
around the molecules[17]Minima in βad and maxima in ultrasound velocity was found at X2EE= 0.0136, indicating
strong solvent-solvent interaction. Density values for different concentrations of potassium thiocyanate in 2ethoxyethanol + water mixtures at 288.15, 298.15, 308.15 and 318.15 K are presented in Table 2. Increase in
density with increase in concentration of the solute is suggests the presence of solute-solvent attraction through
hydrogen bonding and ion-solvent interactions in the solutions [18]. On the other hand, increasing tendency of
density may be interpreted as structure making tendency of the solvent due to the added solute. Decrease in density
with increase in temperature indicate decline in cohesive forces. Maxima in density was observed at X2EE= 0.0052.
Further addition of co-solvent results in rise in overall volume and therefore gradual decrease in density is
observed.
Inter molecular free length (Lf):
Nature of the molecular interaction are studied by intermolecular free length [19] and is calculated using the
equation 3.Inter molecular free length for KSCN in 2- ethoxyethanol +water mixtures 288.15, 298.15, 308.15 and
318.15 K is calculated using the adiabatic compressibility data and presented in the Table 1. Inter molecular free
length decreases linearly with increase in concentration of KSCN in different mole fractions of 2-ethoxyethanol.
This may be due to decrease in compressibility with increase in concentration of the solute, which in turn indicates
significant interaction between solute-solvent and solvent-solvent [20].Lowest Lf values was found at X2EE=
0.0136. This proves that the frame structure of solvent mixture remains stable, not affected by the added solute.
As expected rise in temperature increases intermolecular distance between the surfaces of two molecules [21]
weakeningthe ion-solvent and solvent-solvent interactions.
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Page 180
Surekha et al., American International Journal of Research in Science, Technology, Engineering & Mathematics,26(1), March-May 2019,
pp. 179-187
Specific acoustic impedance (Z):
Specific acoustic impedance [22]is the product of ultrasonic velocity (U) and density (d) and is calculated using
the equation 4. The Z values computed for KSCN in 2-ethoxyethanol +water mixtures at different compositions
are reported in Table 2. A gradual increase in Z value with concentration of KSCN is observed which can be
attributed to the effective solute- solvent interactions [23]. It increases the intermolecular distance between the
molecules which in turn enhances the impedance in the ultrasonic propagation [24] and becomes maximum at
X2EE= 0.0136 suggesting highest solvent-solvent interaction at that mole fraction. Increase in temperature
effectively changes structure of the molecules causing decrease in impedance values in co-solvent rich region but
opposite trend is seen in water rich region i.e., at x2pr =0.0000 and 0.0023.
Relative Association (RA):
Relative association values for potassium thiocyanate in different compositions of 2-ethoxyethanol + water
mixtures are computed using the equation 5 and are shown in Table 2. The increasing trend of RA value with
solute concentration shows the ion-solvent interaction [22]. There is no much effect of temperature on RAvalues
of KSCN in water and 2- ethoxyethanol + water system studied.
Table 1. Experimentally determined ultrasonic velocity (U: ms-1), adiabatic compressibility (βad: m2/N) and intermolecular free
length (Lf: m) for KSCN in 2 - ethoxyethanol + water mixtures with respect to concentration (C: Mol dm-3) at different
temperatures
TEMPERATURE
C
288.15K
298.15K
308.15K
318.15K
U 1010βad 1010Lf U 1010βad 1010 Lf U 1010βad 1010 Lf U 1010βad 1010 Lf
X2EE=0.0000
0.01 1476 4.584 0.406 1500 4.450 0.415 1520 4.339 0.419 1538 4.261 0.428
0.02 1482 4.526 0.404 1506 4.394 0.412 1522 4.308 0.417 1540 4.239 0.426
0.03 1484 4.487 0.402 1504 4.384 0.412 1520 4.300 0.417 1540 4.218 0.425
0.04 1486 4.459 0.401 1510 4.327 0.409 1526 4.245 0.414 1544 4.176 0.423
0.05 1486 4.437 0.400 1516 4.272 0.407 1528 4.216 0.413 1544 4.154 0.422
0.06 1488 4.403 0.398 1524 4.214 0.404 1534 4.163 0.410 1546 4.120 0.420
0.07 1496 4.336 0.395 1524 4.212 0.404 1536 4.137 0.409 1548 4.100 0.419
0.08 1502 4.282 0.393 1532 4.133 0.400 1540 4.097 0.407 1550 4.067 0.418
0.09 1504 4.253 0.391 1544 4.051 0.396 1544 4.058 0.405 1552 4.039 0.416
0.1 1508 4.212 0.389 1536 4.076 0.397 1548 4.023 0.403 1558 3.999 0.414
X2EE = 0.0023
0.01 1528 4.270 0.392 1544 4.190 0.403 1560 4.120 0.408 1580 4.040 0.416
0.02 1532 4.220 0.390 1550 4.140 0.400 1564 4.080 0.406 1582 4.010 0.415
0.03 1534 4.200 0.389 1550 4.120 0.399 1566 4.050 0.405 1584 3.980 0.413
0.04 1536 4.170 0.387 1554 4.080 0.397 1568 4.020 0.403 1584 3.960 0.412
0.05 1540 4.130 0.386 1558 4.060 0.396 1574 3.970 0.401 1590 3.910 0.410
0.06 1544 4.080 0.383 1562 4.010 0.394 1578 3.930 0.399 1590 3.890 0.409
0.07 1552 4.020 0.380 1566 3.970 0.392 1584 3.890 0.397 1592 3.870 0.407
0.08 1560 3.960 0.378 1568 3.940 0.390 1588 3.850 0.395 1600 3.810 0.404
0.09 1560 3.540 0.377 1576 3.880 0.387 1590 3.830 0.394 1600 3.800 0.404
0.1 1568 3.890 0.374 1580 3.850 0.386 1590 3.100 0.354 1608 3.750 0.401
X2EE = 0.0052
0.01 1602 3.897 0.375 1608 3.867 0.387 1612 3.848 0.395 1620 3.810 0.404
0.02 1602 3.897 0.375 1610 3.858 0.386 1614 3.839 0.394 1620 3.810 0.404
0.03 1608 3.867 0.373 1612 3.848 0.386 1616 3.829 0.394 1622 3.801 0.404
0.04 1608 3.867 0.373 1614 3.839 0.385 1618 3.820 0.393 1622 3.801 0.404
0.05 1614 3.839 0.372 1616 3.829 0.385 1620 3.810 0.393 1624 3.792 0.403
0.06 1614 3.839 0.372 1618 3.820 0.384 1620 3.810 0.393 1624 3.792 0.403
0.07 1616 3.829 0.371 1620 3.810 0.384 1620 3.810 0.393 1626 3.782 0.403
0.08 1620 3.810 0.370 1622 3.801 0.384 1623 3.796 0.392 1632 3.755 0.401
0.09 1620 3.810 0.370 1624 3.792 0.383 1624 3.792 0.392 1634 3.745 0.401
0.1 1622 3.801 0.370 1624 3.792 0.383 1628 3.773 0.391 1636 3.736 0.400
X2EE = 0.0136
0.01 1660 3.604 0.360 1642 3.704 0.379 1616 3.844 0.394 1600 3.950 0.412
0.02 1662 3.586 0.359 1644 3.680 0.377 1616 3.829 0.394 1604 3.917 0.410
0.03 1662 3.577 0.359 1650 3.637 0.375 1620 3.792 0.392 1608 3.883 0.408
0.04 1664 3.546 0.357 1654 3.605 0.373 1622 3.767 0.390 1608 3.866 0.407
0.05 1664 3.524 0.356 1652 3.600 0.373 1624 3.744 0.389 1614 3.820 0.405
0.06 1666 3.502 0.355 1652 3.586 0.373 1626 3.719 0.388 1614 3.803 0.404
0.07 1668 3.481 0.354 1656 3.553 0.371 1628 3.694 0.387 1618 3.771 0.402
0.08 1672 3.449 0.352 1656 3.536 0.370 1632 3.658 0.385 1620 3.744 0.401
0.09 1674 3.427 0.351 1658 3.515 0.369 1634 3.637 0.384 1620 3.732 0.400
0.1 1676 3.404 0.350 1658 3.502 0.368 1634 3.620 0.383 1620 3.713 0.399
X2EE = 0.0301
0.01 1598 3.920 0.376 1572 4.080 0.397 1556 4.190 0.412 1524 4.410 0.435
0.02 1600 3.900 0.375 1576 4.040 0.395 1556 4.180 0.411 1524 4.420 0.435
0.03 1604 3.860 0.373 1580 4.010 0.394 1558 4.150 0.410 1530 4.340 0.432
0.04 1604 3.840 0.372 1582 3.980 0.392 1560 4.120 0.408 1532 4.310 0.430
0.05 1608 3.810 0.370 1586 3.940 0.390 1560 4.100 0.407 1532 4.290 0.429
0.06 1610 3.780 0.369 1586 3.930 0.390 1560 4.080 0.406 1532 4.280 0.429
AIJRSTEM 19-234; © 2019, AIJRSTEM All Rights Reserved
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Surekha et al., American International Journal of Research in Science, Technology, Engineering & Mathematics,26(1), March-May 2019,
pp. 179-187
0.07
0.08
0.09
0.1
1612
1616
1620
1624
3.760
3.720
3.690
3.660
0.368
0.366
0.364
0.363
1588
1594
1594
1594
0.01
0.02
0.03
0.04
0.05
0.06
0.07
0.08
0.09
0.1
1496
1498
1506
1508
1508
1510
1510
1526
1528
1530
4.580
4.540
4.470
4.430
4.410
4.380
4.360
4.250
4.220
4.190
0.406
0.404
0.401
0.399
0.398
0.397
0.396
0.391
0.390
0.388
1470
1476
1476
1480
1480
1484
1488
1488
1492
1496
0.01
0.02
0.03
0.04
0.05
0.06
0.07
0.08
0.09
0.1
1332
1360
1362
1380
1388
1390
1392
1398
1404
1408
5.890
5.700
5.650
5.470
5.390
5.330
5.290
5.210
5.140
5.080
0.460
0.453
0.451
0.444
0.440
0.438
0.436
0.433
0.430
0.428
1314
1330
1332
1334
1336
1354
1360
1368
1374
1376
3.900 0.388 1560
3.850 0.386 1562
3.840 0.385 1566
3.820 0.384 1574
X2EE = 0.0765
4.770 0.430 1438
4.710 0.427 1444
4.690 0.426 1448
4.640 0.424 1452
4.620 0.423 1458
4.570 0.421 1460
4.530 0.419 1460
4.500 0.417 146
4.460 0.415 1468
4.420 0.414 1472
X2EE =1.0000
6.190 0.489 1304
6.010 0.482 1306
5.960 0.480 1308
5.900 0.478 1308
5.860 0.476 1312
5.660 0.468 1326
5.580 0.465 1330
5.480 0.460 1336
5.400 0.457 1340
5.360 0.455 1344
4.070
4.040
4.000
3.950
0.406
0.404
0.402
0.400
1536
1540
1542
1546
4.230
4.200
4.170
4.130
0.426
0.424
0.423
0.421
5.030
4.970
4.910
4.860
4.810
4.770
4.740
4.720
4.650
4.600
0.451
0.448
0.446
0.443
0.441
0.439
0.438
0.437
0.434
0.431
1400
1402
1412
1420
1422
1426
1434
1436
1446
1448
5.350
5.320
5.220
5.130
5.090
5.040
4.960
4.920
4.830
4.800
0.479
0.478
0.473
0.469
0.467
0.465
0.461
0.459
0.455
0.454
6.340
6.290
6.230
6.190
6.120
5.950
5.850
5.800
5.730
5.660
0.506
0.504
0.502
0.500
0.498
0.491
0.486
0.484
0.481
0.478
1268
1268
1272
1278
1284
1298
1300
1300
1306
1312
6.760
6.730
3.650
6.550
6.440
6.270
6.210
6.180
6.080
5.990
0.539
0.537
0.396
0.530
0.526
0.519
0.516
0.515
0.511
0.507
4.74
Table 2.Experimentally determined density (d: kg.m-3), specific acoustic impedance (Z: kgm2s-1) and relative association (RA:
mol/dm3) for KSCN in 2- ethoxyethanol + water mixtures with respect to concentration (C) at different temperatures.
TEMPERATURE
288.15K
298.15K
308.15K
318.15K
C
10-3d 10-5Z
0.01
0.02
0.03
0.04
0.05
1.0013
1.0060
1.0120
1.0157
1.0207
0.06
0.07
0.08
0.09
0.1
RA
10-3d 10-5Z
14.83
14.95
15.03
15.13
1.0008
1.0041
1.0097
1.0129
0.9987
1.0034
1.0085
1.0136
1.0185
1.0258
1.0306
1.0351
1.0395
1.0440
15.20
15.33
15.46
15.59
15.67
15.76
1.0179
1.0225
1.0255
1.0286
1.0325
1.0360
0.01
0.02
0.03
0.04
0.05
0.06
0.07
0.08
0.09
0.1
1.0040
1.0088
1.0124
1.0163
1.0221
1.0292
1.0327
1.0378
1.0422
1.0458
15.34
15.45
15.53
15.61
15.74
15.89
16.03
16.18
16.26
16.39
1.0051
1.0090
1.0122
1.0157
1.0206
1.0268
1.0285
1.0318
1.0362
1.0380
1.0002
1.0046
1.0095
1.0144
1.0187
1.0233
1.0279
1.0327
1.0367
1.0404
0.01
0.02
0.03
0.04
0.05
0.06
0.07
0.08
0.09
0.1
1.0074
1.0115
1.0156
1.0208
1.0261
1.0299
1.0338
1.0384
1.0422
1.0463
16.14
16.20
16.33
16.41
16.56
16.62
16.71
16.82
16.88
16.97
0.9951
0.9992
1.0020
1.0071
1.0111
1.0148
1.0182
1.0219
1.0257
1.0293
1.0020
1.0063
1.0111
1.0150
1.0200
1.0246
1.0286
1.0330
1.0371
1.0418
0.01
0.02
0.03
1.0068 16.72 1.0038 1.0013
1.0095 16.82 1.0061 1.0054
1.0122 16.89 1.0088 1.0098
1.0217
1.0223
1.0309
1.0355
1.0399
RA
10-3d 10-5Z
X2EE= 0.0000
15.02 1.0008 0.9976
15.15 1.0041 1.0020
15.2 1.0097 1.0066
15.32 1.0129 1.0115
1.0159
15.45 1.0179
15.59 1.0225 1.0209
15.67 1.0255 1.0246
15.83 1.0286 1.0291
16.02 1.0325 1.0336
15.98 1.0360 1.0373
X2EE= 0.0023
15.44 1.0044 0.9980
15.57 1.0075 1.0027
15.65 1.0124 1.0073
15.76 1.0165 1.0117
15.87 1.0199 1.0160
15.98 1.0236 1.0207
16.09 1.0273 1.0252
16.18 1.0317 1.0299
16.33 1.0339 1.0339
16.43 1.0368 1.0377
X2EE= 0.0052
16.11 0.9931 0.9991
16.20 0.9974 1.0030
16.30 1.0021 1.0078
16.38 1.0060 1.0120
16.48 1.0109 1.0163
16.58 1.0151 1.0209
16.66 1.0182 1.0259
16.76 1.0221 1.0307
16.84 1.0262 1.0347
16.92 1.0308 1.0385
X2EE= 0.0136
16.44 1.0031 0.9961
16.53 1.0068 1.0002
16.66 1.0099 1.0049
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RA
10-3d
15.16
15.27
15.32
15.43
1.0050
1.0087
1.0136
1.0170
15.53
15.66
15.73
15.84
15.97
16.08
1.0208
1.0243
1.0274
1.0307
1.0341
1.0366
0.9922
0.9948
0.9996
1.0044
1.0099
15.57
15.68
15.77
15.86
15.99
16.10
16.24
16.36
16.44
16.50
16.11
16.19
16.29
16.37
16.46
16.54
16.62
16.72
16.80
16.91
10-5Z
RA
15.27
15.36
15.44
15.54
1.0016
1.0038
1.0086
1.0126
1.0156
1.0178
1.0234
1.0278
1.0302
15.63
15.67
15.79
15.87
15.96
16.08
1.0181
1.0234
1.0252
1.0304
1.0344
1.0355
1.0024
1.0063
1.0105
1.0144
1.0175
1.0213
1.0245
1.0283
1.0319
1.0357
0.9926
0.9955
1.0023
1.0064
1.0107
1.0163
1.0189
1.0240
1.0284
1.0316
15.68
15.75
15.88
15.94
16.07
16.16
16.22
16.38
16.45
16.59
1.0001
1.0026
1.0091
1.0132
1.0162
1.0219
1.0241
1.0275
1.0319
1.0334
0.9982
1.0017
1.0061
1.0099
1.0137
1.0183
1.0233
1.0277
1.0312
1.0342
0.9933
0.9961
1.0043
1.0075
1.0134
1.0165
1.0193
1.0275
1.0298
1.0332
15.76
16.09
16.14
16.29
16.34
16.46
16.51
16.57
16.77
16.83
16.90
0.9956
0.9984
1.0063
1.0095
1.0150
1.0181
1.0204
1.0274
1.0293
1.0322
16.09 1.0000 0.9888 15.82
16.16 1.0042 0.9922 15.91
16.28 1.0080 0.9961 16.02
0.9947
0.9972
1.0003
Page 182
Surekha et al., American International Journal of Research in Science, Technology, Engineering & Mathematics,26(1), March-May 2019,
pp. 179-187
0.04
0.05
0.06
0.07
0.08
0.09
0.1
1.0185
1.0249
1.0288
1.0326
1.037
1.0412
1.0459
16.99
17.06
17.16
17.23
17.35
17.44
17.53
1.0146
1.0210
1.0245
1.0279
1.0314
1.0352
1.0394
1.014
1.0179
1.0217
1.0263
1.0312
1.0348
1.0388
0.01
0.02
0.03
0.04
0.05
0.06
0.07
0.08
0.09
0.1
0.9977
1.0021
1.0067
1.0122
1.0162
1.0206
1.0239
1.0283
1.0324
1.0362
15.94
16.03
16.15
16.24
16.34
16.34
16.50
16.62
16.73
16.83
1.0011
1.0050
1.0088
1.0143
1.0175
1.0215
1.0243
1.0279
1.0312
1.0341
0.9916
0.9957
0.9999
1.0039
1.0088
1.0128
1.0178
1.0217
1.0250
1.0301
0.01
0.02
0.03
0.04
0.05
0.06
0.07
0.08
0.09
0.1
0.9762
0.9818
0.9864
0.9926
0.9973
1.0016
1.0055
1.0111
1.0158
1.0202
14.60
14.71
14.85
14.97
15.04
15.12
15.18
15.43
15.52
15.61
1.0015
1.0068
1.0097
1.0156
1.0204
1.0243
1.0283
1.0304
1.0348
1.0389
0.9699
0.9747
0.9794
0.9838
0.9888
0.9932
0.9980
1.0029
1.0083
1.0119
0.01
0.02
0.03
0.04
0.05
0.06
0.07
0.08
0.09
0.1
0.9419
0.9481
0.9541
0.9594
0.9637
0.9710
0.9761
0.9813
0.9878
0.9938
13.49
12.89
12.99
13.23
13.38
13.49
13.59
13.71
13.87
13.99
1.0002
1.0023
1.0082
1.0094
1.0119
1.0191
1.0240
1.0280
1.0333
1.0386
1.0397
0.9411
0.9460
0.9522
0.9585
0.9642
0.9695
0.9752
0.9802
0.9862
16.77 1.0133 1.009
16.82 1.0176 1.0127
16.88 1.0214 1.017
17.00 1.0252 1.0213
17.08 1.0301 1.0263
17.16 1.0333 1.0297
17.22 1.0373 1.0345
X2EE= 0.0301
15.59 1.0038 0.9865
15.69 1.0071 0.9887
15.80 1.0105 0.9926
15.88 1.0141 0.9979
16.00 1.0182 1.0012
16.06 1.0222 1.0063
16.16 1.0268 1.0104
16.29 1.0295 1.0145
16.34 1.0329 1.0193
16.42 1.0379 1.0228
X2EE =0.0765
14.26 1.0021 0.9605
14.39 1.0058 0.9657
14.46 1.0106 0.9713
14.56 1.0142 0.9757
14.63 1.0194 0.9777
14.73 1.0230 0.9833
14.85 1.0270 0.9891
14.92 1.0320 0.9939
15.04 1.0367 0.9985
15.13 1.0394 1.0039
X2EE1.0000
13.66 1.0034 0.9276
12.54 1.0080 0.9320
12.60 1.0138 0.9380
12.70 1.0194 0.9445
12.80 1.0246 0.9496
13.06 1.0312 0.9551
13.19 1.0369 0.9605
13.34 1.0440 0.9662
13.47 1.0494 0.9725
13.57 1.0547 0.9782
16.37
16.45
16.54
16.62
16.75
16.83
16.90
1.0117
1.0150
1.0189
1.0228
1.0270
1.0300
1.0348
1.0005
1.005
1.0095
1.013
1.0177
1.0209
1.0263
16.09
16.22
16.29
16.39
16.49
16.54
16.63
1.0048
1.0080
1.0125
1.0152
1.0195
1.0227
1.0281
15.34
15.38
15.47
15.58
15.62
15.7
15.76
15.84
15.96
16.09
1.0045
1.0068
1.0103
1.0153
1.0187
1.0238
1.0280
1.0317
1.0357
1.0375
0.9764
0.9752
0.9835
0.9876
0.9924
0.9954
1.0013
1.0047
1.0094
1.0129
14.88
14.86
15.05
15.13
15.20
15.25
15.30
15.47
15.56
15.65
1.0035
1.0022
1.0094
1.0132
1.0181
1.0212
1.0264
1.0289
1.0333
1.0360
13.81
13.94
14.06
14.16
14.25
14.36
14.44
14.51
14.68
14.77
1.0002
1.0042
1.0091
1.0127
1.0134
1.0188
1.0248
2.2186
1.0326
1.0373
0.9529
0.9560
0.9606
0.9658
0.9714
0.9766
0.9810
0.9861
0.9905
0.9944
13.34
13.40
13.56
13.71
13.71
13.92
14.06
14.16
14.32
14.39
0.9996
1.0024
1.0048
1.0084
1.0137
1.0182
1.0209
1.0257
1.0279
1.0315
12.09
12.17
12.26
12.35
12.46
12.66
12.77
12.90
13.03
13.15
1.0045
1.0082
1.0152
1.0206
1.0256
1.0310
1.0363
1.0425
1.0498
1.0554
0.9203
0.9239
0.9293
0.9349
0.9414
0.9471
0.9522
0.9575
0.9636
0.9698
11.67
11.71
11.82
11.95
12.09
12.29
12.38
12.45
12.58
12.72
1.0058
1.0087
1.0145
1.0212
1.0300
1.0351
1.0407
1.0453
1.0509
1.0565
Apparent Molar Compressibility ( k ):
Apparent molar compressibility was calculated using the equation (6) is a function of concentration as suggested
by Gucker [25] as follows
ɸk = ɸ0k + Sk √C
(9)
Where ɸ0kis the limiting apparent molar compressibility and Skis obtained from the intercept of the linear plot
(Fig. 1) of ɸkversus √C, and association constant Sk is the experimental slope. The limiting apparent
compressibility (ɸ0k) and related constant Sk values obtained are provided in Table 3. Most of the negative values
of ɸ0k strengthen the view that there exist solute-solvent interactions in the system and the loss of compressibility
of solvent due to electrostrictive solvation [22]. The positive Sk values signify the existence of ion-ion interaction
of the system and also structure breaking property of the electrolyte.
Table 3. Computed limiting apparent molar compressibility ((ϕ0k: m2 mol -1)) and the slope Sk for KSCN in 2 - ethoxyethanol + water
mixtures at different temperatures.
TEMPERATURE
288.15K
298.15K
308.15K
318.15K
X2EE
1015 Φ0k
0.0000
0.0023
0.0052
0.0136
0.0301
0.0765
1.0000
-223.00
-609.30
-1022.00
2989.00
-455.20
-103.20
-1664.00
1015Sk
47.50
442.30
927.80
-2503.00
357.20
-41.75
150.90
1015 Φ0k
-518.20
-530.20
-902.20
-929.00
102.40
-234.70
-2249.00
1015Sk
309.00
431.20
847.10
856.10
-131.50
140.40
416.10
1015 Φ0k
-339.50
644.80
-401.40
975.00
-973.00
-842.00
-2391.00
1015Sk
279.00
-880.00
446.00
-959.00
816.70
729.80
444.40
1015 Φ0k
-94.55
-122.90
-376.30
1021.00
150.20
-609.30
-1829.00
1015Sk
68.10
37.98
401.90
-994.90
-140.00
326.30
-53.16
Apparent Molar Volume (ϕv)
The apparent molar volume ϕv is calculated using the equation 7. The relation between apparent molar
compressibility and √C is given by least squares method as,
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Surekha et al., American International Journal of Research in Science, Technology, Engineering & Mathematics,26(1), March-May 2019,
pp. 179-187
ɸv = ɸ0v + Sv √C
(10)
The linear plotof apparent molar volume (ϕv) versus √C is shown Fig. 2. The intercept and slope obtained from
this gives limiting apparent molar volume (ϕ0v) and its related constant Sv. Computed molar volume (ϕ0v) and Sv
values are presented in the Table 4. The preferential solvation of the ions by different species in the solvent system
and type of interaction between solvent molecules are due to change in partial molar volume with respect to
change in compositions of solvent mixtures. The positive ϕ0vin all the compositions of solvent strengthen the
strong ion-solvent interactions. Negative Sv values are interpreted as a sign of weak ion-ion interaction and also
gives information about inter ionic penetration of the ions in the solvent structure [26]. Relatively lower ϕ0v values
for potassium thiocyanate in solvent mixture were found at X 2EE=0.0052, implies strong solvent–solvent
interaction. In the present work, larger ϕ0v values substantiate strong ion-solvent interactions.
Table 4. Computed limiting apparent molar volume ((ϕ0v: m2 mol -1)) and the slope Sv for KSCN in 2 - ethoxyethanol + water mixtures at
different temperatures
TEMPERATURE
288.15K
298.15K
308.15K
318.15K
X2EE
0.0000
0.0023
0.0052
0.0136
0.0301
0.0765
1.0000
106Φ0v
61.45
63.64
44.84
71.85
56.36
64.25
324.90
106Sv
-928.00
-41.19
26.02
-60.05
-9.17
-41.58
-124.40
106 Φ0v
61.38
61.78
62.16
69.34
66.25
51.57
285.60
106 Φ0v
31.87
61.90
72.17
86.15
48.65
57.81
304.00
106 Sv
-7.33
-25.58
-29.89
-40.87
-33.48
1.23
3.86
106Sv
-9.69
-23.84
-61.89
-83.83
18.62
-13.65
-49.33
106Φ0v
86.13
64.48
63.07
111.40
64.91
80.39
302.90
106Sv
-33.43
-26.29
-21.98
-153.00
-24.12
-89.38
-31.44
Solvation Number (Sn):
Solvation number (Sn) of an ion is the number of solvent molecules surrounded to that ion which loses entire
translational degree of freedom and always moves along with the ion. The theory proposed by Passynski [27] was
used for calculating solvation numbers (equation 8). The computed values of S n values for KSCN in 2ethoxyethanol+water mixture at 298.15K are presented in the Table 5. The S n values are found an initial increase
followed by later decrease as the amount of 2-ethoxyethanol is increased in the mixture. Strong solute–solvent
interaction is observed at X2EE = 0.0052 since highest Sn values found at this composition.
Table 5. Calculated solvation number (Sn) for KSCN in 2 – ethoxy ethanol + water mixtures at different temperatures
X2EE
C
0.0000
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1.0
-2.0
2.5
2.1
3.4
4.1
4.6
4.0
4.7
5.3
4.5
0.0023
-5.1
0.6
1.2
2.1
2.2
2.4
3.2
3.2
3.7
3.7
0.0052
0.0136
24.7
12.9
9.0
7.0
5.8
5.0
4.5
4.0
3.7
3.3
0.0301
-1.0
0.7
1.9
2.3
1.9
1.8
2.1
2.0
2.0
2.0
0.0765
-0.6
1.1
1.5
1.6
1.9
1.7
1.7
2.0
1.8
1.8
1.0000
2.1
2.3
1.8
1.9
1.7
1.7
1.7
1.7
1.7
1.7
2.3
2.7
2.1
1.9
1.6
1.9
1.9
1.8
1.8
1.7
VI. Conclusions
Various ultrasonic parameters calculated have been effectively used to explain the ion-ion, ion-solvent and
solvent-solvent interactions in the system comprising of potassium thiocyanate, 2-ethoxyethanol and water.
Ultrasonic studies revealed that the ternary system involves strong solvent-solvent interactions at X2EE = 0.0136
as a result of formation of hydrophobic aggregations. The positive S k values specify the structure breaking nature
of KSCN in 2-ethoxyethanol+water media. Highest solvation number was observed at X 2EE = 0.0052 indicating
strong solute-solvent interactions for KSCN in 2-ethoxyethanol + water system at 298.15K.
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Page 184
Surekha et al., American International Journal of Research in Science, Technology, Engineering & Mathematics,26(1), March-May 2019,
pp. 179-187
Figure1.Plot of ϕk ( m2 mol -1) Vs √C ( mol1/2 dm-3/2) for KSCN in 2- ethoxyethanol + water mixture at different Temperatures
2000
2000
X2EE= 0.0000
√C
1000
0
-10000.00
0.50
1.00
1.50
ɸk
-2000
ɸk
-3000
√C
X2EE=0.0052
1.50
-2000
0.50
1.00
4000
X2EE=0.0136
√C
2000
1.50
-4000
-6000
-8000
ɸk -10000
-12000
-14000
-16000
-18000
0
-20000.00
ɸk
0.50
1.00
1.50
-4000
-6000
-8000
-10000
-12000
X2EE=0.0301
8000
6000
4000
2000
0.50
1.00
-4000
√C
1.50
14000
12000
10000
8000
6000
ɸk 4000
2000
0
-20000.00
X2EE=0.0765
0.50
-4000
-6000
-6000
-8000
30000
1.00
-6000
-7000
0
-20000.00
0.50
-5000
-6000
ɸk
√C
-4000
-5000
10000
0
0.00
-1000
-3000
-4000
0
-20000.00
X2EE=0.0023
1000
1.00
√C
1.50
X2EE=1.0000
25000
20000
ɸk
288.15K
298.15K
308.15K
318.15K
15000
10000
5000
0
0.00
-5000
-10000
0.50
1.00
√C
1.50
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Page 185
Surekha et al., American International Journal of Research in Science, Technology, Engineering & Mathematics,26(1), March-May 2019,
pp. 179-187
Figure2. Plot of ϕv ( m3 mol -1) Vs √C ( mol1/2 dm-3/2) for KSCN in 2- ethoxyethanol + water mixture at different Temperatures
100
X2EE=0.0000
100
80
60
60
ɸv
ɸv
40
40
20
20
0
0.00
0.50
√C
1.00
0
0.00
1.50
0.10
0.20
0.30
0.40
√C
200
X2EE=0.0052
100
ɸv
X2EE=0.0023
80
80
150
60
ɸv 100
40
X2EE= 0.0136
50
20
0
0.00
0
0.00
0.10
0.20
0.30
0.10
0.20
0.40
0.40
√C
√C
120
80
X2EE=0.0301
X2EE=0.0765
100
60
ɸv
0.30
ɸv
40
80
60
40
20
0
0.00
20
0.10
0.20
0.30
0.40
0
0.00
0.10
0.20
0.40
√C
√C
400
0.30
X2EE=1.0000
300
ɸv
200
288.15K
298.15K
308.15K
318.15K
100
0
0.00
0.10
0.20
0.30
0.40
√C
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VI. Acknowledgements
The financial support for this investigation given by Visvesvaraya Technological University, Belgaum, India
under the grant Ref. No. VTU/Aca/2010-11/A-9/11329 dated 17th December 2010; VGST, Government of
Karnataka; Dr. Renuka Prasad K. V. General Secretary, AOLE, Sullia are gratefully acknowledged.
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