a
CIO”7 m2/s)
|
T
(K)
|
a
(10 " 7 m2/s)
|
T
00
|
a
(10“s m2/s)
|
T
(K)
| |
a
(10“8 m2/$)
|
295.44
|
1.193
|
295.56
|
1.068
|
295.53
|
9.843
|
295.34
|
9.856
|
300.34
|
1.215
|
300.25
|
1.072
|
300.42
|
9.812
|
300.41
|
9.776
|
305.15
|
1,219
|
305.20
|
1.090
|
305.13
|
9.741
|
305.29
|
9.771
|
310.06
|
1.229
|
309.99
|
1.107
|
309.87
|
9.710
|
310.03
|
9.711
|
314.74
|
1.248
|
314.84
|
1.108
|
314.72
|
9.682
|
314.82
|
9.614
|
319.62
|
1.272
|
319.64
|
1.125
|
319.95
|
9.593
|
319.77
|
9,581
|
324.54
|
1.284
|
324.49
|
1.137
|
324.38
|
9.581
|
324.54
|
9.567
|
329.31
|
1.290
|
329.92
|
1.145
|
329.79
|
9.528
|
329.41
|
9.520
|
334.02
|
1.312
|
333.92
|
1.146
|
334.10
|
9.450
|
334.24
|
9.421
|
which are caused by deviations from one - dimensional heat conduction, and cancel these errors from the measured thermal diffusivity value. The relaxation time of the first-order diffracted intensity r and the modulus q of the grating vector can be determined to accuracies of about 1 % and _+0.55%, respectively. Hence, the accuracy of the measurements of thermal diffusivity is estimated to be about -t-1.5% [9, 11, 12]. As shown in Table 1, the thermal diffusivity of aqueous solutions of methanol tends to in-crease with increasing temperatures when the weight frac-tion of water in the solutions is greater than that of methanol . For solutions with 60% and 80% methanol, thermal diffusivity a decreases with increasingly higher temperature . The temperature dependence of the thermal diffusivity of aqueous solutions of methanol on the weight fraction of methanol can be explained with the fact that the thermal diffusivity of pure methanol decreases with increasing temperatures . In comparison, thermal diffusiv-ity of water has a tendency to increase in the temperature range 295 - 335 K when temperature T increases [13].
As there have been no experimental data on the ther-mal diffusivity of aqueous solutions of methanol reported up to now, we found the density and the specific heat capacity data available in [15, 16] and calculated the thermal conductivity of aqueous solutions of methanol using the thermal diffusivity data in Table 1. F r o m Figs. 6 and 7, the derived thermal conductivity values show very good agreement with the experimental results of [2, 15]. The deviations of the derived thermal conductivity values from the data in [2, 15] are within + 3%.
PRACTICAL SIGNIFICANCE/USEFULNESS
For many technical processes, knowledge of the thermal conductivity or thermal diffusivity of liquids is highly im-portant. However, few exact experimental data for these properties are available because of difficulties of conven-tional measurement techniques such as heat losses and we get the values of the coefficients c o and c 1 for the aqueous solutions of methanol by the method of least squares and show them with their variances, the statistical deviations, and correlation coefficients of the fits in Table 2.
w* c„ (10 7 m2/s) c, (10 10m2/s-K) a (%) r
Выпуск № 18 (том 2) (сентябрь, 2021) 1
INTRODUCTION 687
MEASUREMENT 688
AND 688
EXPERIMENTAL APPARATUS 688
Probing laser Signal and data processing 689
Excitation of thermal grating Detection of signal 689
RESULTS AND DISCUSSION 693
CONCLUSIONS 696
100% 2.030 ± 0.061b -3.487 ± 0.194b ±0.73b 0.989b
Table2. Results for the Least-Squares Fit of Thermal Diffusivity of Aqueous Solutions of Methanol as a Function of Temperature
Figure 6. Thermal conductivity X of aqueous solutions of methanol at 295 K as a function of weight percent wt of methanol.
Figure 7. Thermal conductivity X of aqueous solutions of methanol at 313 K as a function of weight percent wt of methanol.
The convective and radiative contributions to the heat transfer in the sample. Photon correlation spectroscopy (PCS, dy-namic Rayleigh scattering) can be used to measure the thermal diffusivity of transparent, pure liquids and their binary mixtures, avoiding all the problems of conventional measurement techniques. However, it was found that sub-stances like water and aqueous solutions, whose Landau - Placzek ratio is very large, cannot be investigated by PCS because of a large Brillouin contribution [7, 17]. The laser-induced thermal grating technique can be used for accurate determination of the thermal diffusivity of liquids. Using the relationship X = apcp, the thermal conductivity can be calculated, provided the values for p und Cp are available.
Compared with other optical meth-ods, for example, PCS, this technique has the advantage that it can be applied to all transparent or semitranspar-ent liquids and liquid mixtures. In particular, its applica-tion to high-temperature molten salts and anisotropic materials (e.g., flowing polymer melts) is most promising. In the measurement, only a very small sample volume is necessary (a few cubic millimeters), and the measuring time is very short (a few milliseconds). Because of the small temperature rise (AT < 0.2 K) in the sample during the measurements and the very short measuring time, the influence of convective heat transfer is negligible. Moreover, this measurement technique produces abso-lute values without calibration procedures. Hence, the laser-induced thermal grating technique is suitable for accurate, rapid determination of the thermal diffusivity of liquids over an extended temperature range.
CONCLUSIONS
The thermal diffusivity of aqueous solutions of methanol has been measured at atmospheric pressure and in an extended range of temperature from 295 to 335 K. The measurements were carried out using a laser-induced thermal grating technique, which is an absolute method and can be applied to all liquids and their mixtures. The derived thermal conductivity values from the measured thermal diffusivity, the density, and the available specific heat capacity data show very good agreement, within _+3%, with previous experimental results.
NOMENCLATURE a thermal diffusivity, m2/ s amplitude of the diffracted signal, V c0 coefficient, dimensionless c± coefficient, dimensionless C p isobaric specific heat, //( к g • K)
C background of the signal, V d sample thickness, m
I± intensity of the first-order diffracted beam, W / m2 n refractive index, dimensionless q modulus of the grating vector, m - 1 r correlation coefficient, dimensionless t time, s th heating pulse duration, s T temperature, K V voltage, V W± weight percentage, %
X coordinate direction, m
Greek Symbols
Д n ( t ) modulation of refractive index, dimensionless
Д T ( t ) amplitude of the transient periodic temperature field, K
AX distance between the two peaks of the diffracted intensity distributions, m
At sample time, s
в intersection angle, deg
6S diffraction angle, deg A grating constant, m
Л thermal conductivity, W / ( m * K)
Ah wavelength of heating laser beam, m Ap wavelength of probing laser beam, m p density, к g / m3 о statistical deviation, % т relaxation time, s
m maximum phase variation of the grating, dimensionless
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