HCFC-22 - American Chemical Society

J. Chem. Eng. Data 2001, 46, 193-201

193

Measurements of the Thermal Conductivity of Chlorodifluoromethane (HCFC-22) in the Temperature Range from 300 K to 515 K and at Pressures up to 55 MPa1 Bernard Le Neindre,*,† Yves Garrabos,‡ Aidar Sabirzianov,§ and Farid Goumerov§ Laboratoire d’Ingeńie´rie des Mate´riaux et des Hautes Pressions, CNRS, Institut Galileé, Universite´ Paris Nord, Av. J. B. Cle´ment, 93430 Villetaneuse, France, Institut de Chimie de la Matie`re Condenseé de Bordeaux, CNRS-UPR 9048, Universite´ de Bordeaux I, 87, Avenue du Dr Albert Schweitzer, F-33608 Pessac Cedex, France, and Universite´ d’Etat de Technologie de Kazan, 68 rue K. Marx, 420015 Kazan, Russia

We report measurements of the thermal conductivity of chlorodifluoromethane (HCFC-22) with a coaxial cylinder cell operating in the steady state. The measurements of the thermal conductivity of HCFC-22 were performed along several quasi-isotherms between 300 K and 515 K, in the gas phase, the liquid phase, and the critical region. The pressure range covered varies from 0.1 MPa to 55 MPa. On the basis of the fitting of experimental data, a background equation is provided to calculate the thermal conductivity outside the critical region as a function of temperature and density. A careful analysis of the various sources of errors leads to an estimated uncertainty of the thermal conductivity, of the order of (1.5%.

Introduction For energy conversion processes and application in the field of chemical engineering, there was a great interest in the knowledge of thermophysical properties of chlorinated refrigerants, but most of them were restrained by the Montreal Protocol. However HCFC-22 (chlorodifluoromethane) which belongs to the series of hydrochlorofluorocarbons (HCFCs) will keep its technical importance, at least in the near future due to its lower depletion potential than those of the other fully halogenated CFCs. It is used as a temporary substitute for these compounds. On the other hand, the thermophysical properties of HCFC22 were more widely studied than those of other HCFCs, and the thermodynamic and transport properties of this fluid are considered to become useful standards to evaluate the thermophysical properties of other refrigerants. Nevertheless the transport properties and particularly the thermal conductivity do not cover the full range of P-V-T data. Moreover, previous measurements of the thermal conductivity of HCFC-22 have revealed significant discrepancies from each other which are much larger than the respective accuracy claimed by the authors.

The dilute gas contribution λ0(T) was obtained by performing measurements on the gas phase at atmospheric pressure as a function of temperature. The background term

λB(T,F) ) λ0 + δλ(T,F)

(2)

was obtained by making measurements along quasiisotherms as a function of pressure in the liquid phase and in the gas phase far away from the critical region. The remaining contribution, ∆λ(T,F), represents the enhancement of the thermal conductivity due to critical fluctuations, in the supercritcal region or in the subcritical region along the saturation curve, and was obtained by performing measurements in these two regions. In this paper we present only experimental data in the liquid phase and in the gas phase far away from the critical point in order to determine the so-called thermal conductivity background. Our measurements in the critical region and in the gas phase below the critical point will be reported later. The density was calculated with a new equation of state reported by Wagner et al.1 where the critical parameters together with the estimated uncertainties are given as follows:

In a series of measurements, we have investigated the influence of temperature and pressure on the thermal conductivity of HCFC-22. The measurements were performed in order to make an analysis of the data based on the residual concept. The thermal conductivity λ(T,F) as a function of temperature T and density F may be represented as the sum of three contributions

PC ) 4.9885 ( 0.02 MPa

λ(T,F) ) λ0(T) + δλ(T,F) + ∆λ(T,F)

The sample was provided by ELF-ATOCHEM, and its purity was estimated to be better than 99.8% by the manufacturer’s analysis.

(1)

* To whom correspondence should be addressed. E-mail: leneindr@ limhp.univ-paris13.fr. † Laboratoire d’Inge ´ nie´rie des Mate´riaux et des Hautes Pressions, CNRS, Institut Galileé, Universite´ Paris Nord. ‡ Institut de Chimie de la Matie ` re Condenseé de Bordeaux, CNRSUPR 9048, Universite´ de Bordeaux I. § Universite ´ d’Etat de Technologie de Kazan.

TC ) 369.28 ( 0.2 K

FC ) 520 ( 5 kg m-3

Experimental Apparatus The thermal conductivity of HCFC-22 was measured in vertical coaxial cylinders, operating in the steady-state mode. The same device was already used in the measurement of the thermal conductivity of 1-chloro-1,1-difluoro-

10.1021/je0002078 CCC: $20.00 © 2001 American Chemical Society Published on Web 12/30/2000

194

Journal of Chemical and Engineering Data, Vol. 46, No. 2, 2001

Table 1. The Thermal Conductivity of HCFC-22 at Atmospheric Pressure

Table 3. Thermal Conductivity of HCFC-22 along the Quasi-Isotherm T ) 299.4 K

T/K

λ/mW‚ m-1‚K-1

T/K

λ/mW‚ m-1‚K-1

T /K

λ/mW‚ m-1‚K-1

295.04 295.55 298.49 299.26 301.39 315.86 319.95 331.50

9.77 9.89 10.07 10.11 10.25 11.41 11.75 12.38

337.13 346.23 362.85 372.13 373.90 375.45 379.63 384.55

13.06 13.75 14.97 15.72 15.95 16.09 16.16 16.51

385.96 415.34 435.03 453.17 454.62 473.14 493.17 514.31

16.73 19.09 20.59 21.88 21.96 23.38 24.85 26.84

Table 2. Coefficients of the Ideal Gas Part of the Isobaric Heat Capacity of HCFC-22 i

ai

θi

1 2 3 4 5

0.300 671 581 × 101 0.393 214 630 × 101 0.110 074 668 × 101 0.187 129 085 × 101 0.222 706 659 × 101

0.482 421 333 × 101 0.113 929 640 × 102 0.282 862 148 × 101 0.155 580 861 × 101

T/K

P/MPa

F/kg‚m-3

λ/mW‚m-1‚K-1

299.02 299.42 299.42 299.41 299.90 299.40 299.40 299.40 299.39 299.39 299.38 299.37 299.86 299.37 299.36 299.35 299.35 299.34 299.33 299.33 299.33 299.32 299.31 299.30 299.30 299.29

1.065 1.492 1.982 2.50 3.00 3.50 4.00 4.50 5.00 6.00 7.00 8.00 8.50 9.00 9.30 10.00 11.00 12.00 12.00 14.00 15.00 16.00 17.00 18.00 19.00 19.89

1187.7 1188.8 1191.8 1194.9 1195.8 1200.7 1203.4 1206.2 1208.9 1214.1 1219.1 1223.9 1224.6 1228.6 1230.0 1233.1 1237.4 1241.7 1241.7 1249.8 1253.6 1257.4 1261.2 1264.8 1268.3 1271.4

82.79 82.33 82.50 82.84 83.33 83.69 84.03 84.39 84.74 85.27 85.81 86.54 87.07 87.10 87.85 88.23 88.81 89.40 89.99 90.38 90.99 91.40 92.23 92.86 93.50 93.93

Figure 1. Relative deviations of theoretical values calculated by eqs 4 and 6 from our experimental data at atmospheric pressure with σ ) 0.4652 nm and /k ) 285.7 K.

Figure 3. Excess of thermal conductivity of HCFC-22.

Figure 2. Relative deviations of calculated values by eq 3 from experimental data at atmospheric pressure: 9, this work; b, Makita et al.;10 2, Hammerschmidt;11 1, Watanabe et al.;9 [, Vargaftik et al.8

ethane (HCFC-142b),2 pentafluoroethane (HFC-125),3 and 1,1,1,2-tetrafluoroethane (HFC-134a).4 A detailed description of the cell, the method of measurement, and corrections are available.5

Figure 4. Relative deviations of calculated values by the background equation from the experimental data of Assael et al.:12 9, T ) 252 K; b, T ) 273 K; 2, T ) 293 K; 1, T ) 313 K; [, T ) 333K.

Dilute-Gas Thermal Conductivity

temperature in Table 1. The experimental data were fitted to a linear equation

The results of the measurement of the thermal conductivity at atmospheric pressure are listed as a function of

λ0 ) -12.9 + 0.07666T

(3)

Journal of Chemical and Engineering Data, Vol. 46, No. 2, 2001 195 Table 4. Thermal Conductivity of HCFC-22 along the Quasi-Isotherm T ) 300.8 K


T/K

P/MPa

F/kg‚m-3

λ/mW‚m-1‚K-1

T/K

P/MPa

F/kg‚m-3

λ/mW‚m-1‚K-1

300.91 300.90 300.90 300.89 300.89 300.89 300.88 300.88 300.88 300.87 300.87 300.86 300.86 300.86 300.86 300.85 300.85 300.84 300.84 300.84 300.83 300.83 300.83 300.83 300.83 300.82 300.82 300.82 300.82 300.82 300.81 300.81 300.81 300.81 300.81 300.80 300.80 300.80 300.80 300.80 300.79 300.79 300.79 300.79 300.79 300.78 300.78 300.78 300.78 300.78 300.78 300.78 300.77 300.77

2.00 3.00 4.00 5.00 6.00 7.00 8.00 9.00 10.00 11.00 12.00 13.00 14.00 15.00 16.00 17.00 18.00 19.00 20.00 21.00 22.00 23.00 24.00 25.00 26.00 27.00 28.00 29.00 30.00 31.00 32.00 33.00 34.00 35.00 36.00 37.00 38.00 39.00 40.00 41.00 42.00 43.00 44.00 45.00 46.00 47.00 48.00 49.00 50.00 51.00 52.00 53.00 54.00 55.00

1185.8 1191.9 1197.8 1203.4 1208.7 1213.8 1218.7 1223.5 1228.0 1232.5 1236.8 1241.0 1245.1 1249.0 1252.8 1256.7 1260.2 1263.9 1267.4 1270.8 1274.1 1277.4 1280.6 1283.8 1286.9 1289.9 1292.8 1295.7 1298.6 1301.4 1304.1 1306.8 1309.5 1312.1 1314.8 1317.4 1319.9 1322.3 1324.8 1327.2 1329.5 1331.9 1334.2 1336.5 1338.7 1340.9 1343.1 1345.3 1347.4 1349.6 1351.7 1353.7 1355.8 1357.8

84.13 84.78 85.44 86.11 86.79 87.48 88.19 88.90 89.63 89.99 90.74 91.49 92.26 93.04 93.44 94.24 94.64 95.47 95.88 96.30 97.15 97.58 98.02 98.90 99.34 99.80 100.25 100.71 101.17 101.64 102.11 102.58 103.06 103.55 104.04 104.53 105.03 105.53 106.04 106.55 107.07 107.59 107.59 108.12 108.65 109.19 109.73 110.28 110.28 110.83 111.39 111.39 111.95 112.52

302.57 302.57 302.56 302.56 302.56 302.55 302.55 302.55 302.54 302.54 302.54 302.53 302.53 302.52 302.51 302.51 302.50 302.50 302.50 302.50 302.49 302.49 302.49 302.49 302.48 302.47 302.48

19.84 21.00 22.00 23.00 24.00 25.00 24.82 26.00 27.00 28.00 29.00 30.00 32.00 33.00 34.00 35.00 36.00 37.00 38.00 39.00 40.00 41.00 42.00 43.00 44.00 45.00 45.70

1261.9 1265.9 1269.4 1272.7 1276.0 1279.1 1278.6 1282. 1285.4 1288.3 1291.4 1294.3 1299.9 1302.6 1305.4 1308.1 1310.7 1313.3 1315.8 1318.4 1320.9 1323.3 1325.7 1328.1 1330.4 1332.7 1334.3

94.95 95.39 95.83 96.28 96.74 97.42 97.66 98.12 98.59 98.83 99.31 99.79 100.78 101.02 101.77 102.28 102.79 103.31 103.57 104.10 104.62 105.16 105.43 105.70 106.24 106.79 107.08

Figure 5. Relative deviations of calculated values by the background equation from the experimental data of Kim et al.:13 9, T ) 233 K; b, T ) 248 K; 2, T ) 273 K; 1, T ) 298 K; [, T ) 323 K.

The temperature dependence of the thermal conductivity of the dilute gas can be represented by an expression derived from the kinetic theory of gases. The thermal conductivity is related to the reduced effective collision cross section Ωλ*, which contains all the contributions from translational, rotational, vibrational, and electronic degrees of freedom. As there is a lack of reliable experimental data on vibrational collision number, we used for the calculation of the thermal conductivity in the zero density the practical engineering form6

Mayinger and Nabizadeh7 from a regression analysis of the viscosity data of HCFC-22 at atmospheric pressure (/k ) 285.70 K and σ ) 0.4652 nm). The ideal specific heat at constant pressure was calculated with the equation proposed by Wagner et al.1 5

CP0 ) R(1 + a1 + τ2[

∑a (θ ) i

2

i

e-θiτ[1 - e-θiτ]-2]) (5)

i)2

where τ ) TC/T and R ) 0.096 155 96 kJ kg-1 K-1. The values of coefficients ai and θi are given in Table 2. The reduced effective thermal conductivity collision cross section Ωλ* was estimated using a functional expansion 3

λ0(T) )

0.177568(T/M)0.5CP0/R 2

σ Ωλ*

(4)

where CP0 is the ideal isobaric heat capacity. The scaling factors σ and /k, which correspond to the Lennard-Jones 12-6 potential parameters, were previously determined by

Ωλ* )

∑A (1/T*) j

j

(6)

j)1

where A1 ) 0.444 358, A2 ) 0.327 867, and A3 ) 0.193 683 5, as a function of the reduced temperature

T* ) kT/

(7)

196




T/K

P/MPa

F/kg‚m-3

λ/mW‚m-1‚K-1

T/K

P/MPa

F /kg‚m-3

λ/mW‚m-1‚K-1

309.52 309.51 309.50 309.49 309.48 309.47 309.46 309.45 309.44 309.43 309.43 309.42 309.41 309.40 309.40 309.39 309.38 309.38 309.37 309.36 309.36 309.35 309.35 309.34 309.34 309.33 309.33 309.32 309.32 309.31 309.31 309.31 309.30 309.29 309.29 309.29 309.29 309.28 309.28 309.27 309.27 309.27 309.27 309.26 309.26 309.26 309.26 309.25 309.25

2.00 3.00 4.00 5.00 6.00 7.00 8.00 9.00 10.00 11.00 12.00 13.00 14.00 15.00 16.00 17.00 18.00 19.00 20.00 21.00 22.00 23.00 24.00 25.00 26.00 27.00 28.00 29.00 30.00 31.00 32.00 33.00 34.00 35.00 36.00 37.00 38.00 39.00 40.00 41.00 42.00 43.00 44.00 45.00 46.00 47.00 48.00 49.00 50.00

1149.5 1156.9 1163.9 1170.4 1176.7 1182.7 1188.3 1193.9 1199.1 1204.1 1208.9 1213.7 1218.3 1222.7 1227.0 1231.1 1235.3 1239.2 1243.0 1246.7 1250.5 1253.9 1257.5 1260.9 1264.3 1267.6 1270.7 1273.9 1276.9 1280.0 1282.9 1285.9 1288.8 1291.6 1294.3 1297.1 1299.8 1302.4 1305.0 1307.6 1310.1 1312.7 1315.0 1317.5 1319.9 1322.2 1324.5 1326.8 1329.1

78.94 79.87 80.81 81.78 82.61 83.46 84.14 84.84 85.73 86.27 87.00 87.75 88.50 89.27 90.06 90.86 91.67 91.87 92.50 93.13 93.76 94.41 95.07 95.73 96.18 96.86 97.32 98.02 98.49 98.96 99.44 99.92 100.41 100.85 101.40 101.91 102.41 102.93 103.44 103.97 104.23 104.76 105.03 105.57 105.84 106.11 106.39 106.66 107.22

317.74 317.73 317.72 317.72 317.71 317.71 317.70 317.70 317.69 317.68 317.68 317.67 317.67 317.66 317.65 317.65 317.65 317.64 317.64 317.64 317.63 317.63 317.63 317.63 317.62 317.62 317.62 317.61 317.61 317.61 317.61 317.61 317.60 317.60 317.60 317.60 317.59 317.59 317.59 317.59 317.58 317.58 317.58 317.58 317.58

2.00 3.00 4.00 5.00 6.00 7.00 8.00 9.00 10.00 11.00 12.00 13.00 14.00 15.00 16.00 17.00 18.00 19.00 20.00 21.00 22.00 23.00 24.00 25.00 26.00 27.00 28.00 29.00 30.00 31.00 32.00 33.00 34.00 35.00 36.00 37.00 38.00 39.00 40.00 41.00 42.00 43.00 44.00 45.00 46.00

1111.2 1120.4 1128.8 1136.7 1144.1 1151.0 1157.6 1164.0 1169.9 1175.7 1181.1 1186.5 1191.6 1196.5 1201.2 1205.9 1210.3 1214.7 1218.9 1222.9 1226.9 1230.9 1234.7 1238.4 1242.0 1245.5 1248.9 1252.3 1255.7 1259.0 1262.0 1265.2 1268.3 1271.3 1274.3 1277.3 1280.0 1282.9 1285.7 1288.4 1291.0 1293.7 1296.3 1298.8 1301.3

74.66 75.68 76.65 77.73 78.27 79.09 79.92 81.07 81.94 82.88 83.42 84.39 85.02 85.65 86.64 87.30 87.98 88.70 89.33 90.07 90.78 91.51 91.88 92.25 93.00 93.42 94.12 94.55 95.34 95.74 96.14 96.55 97.38 98.25 98.60 99.07 99.50 99.93 100.38 100.82 101.27 101.75 102.13 102.63 103.09

Figure 1 shows a deviation plot between theoretical values calculated by eq 4 and our experimental data. The deviation was found to be less than (2% from 375 K to 550 K. The agreement with the theory is very satisfactory. In fact, the theory is only valid for reduced temperatures T* > 1, while 375 K corresponds to the reduced temperature T* ) 1.3. The comparison with other sources of data shows that the specific heat is known with an accuracy of (1% and that the agreement can be improved at high temperatures if the potential parameters are obtained by a simultaneous fit of viscosity and thermal conductivity data. Figure 2 shows the relative deviations at atmospheric pressure between the tabulated values of Vargaftik,8 the data reported in JAR Tables,9 and a set of experimental data measured by Makita et al.10 and Hammerschmidt.11 Over most of the experimental range, the deviations are larger than the experimental uncertainty. However, there is always a small temperature range where the agreement is good. This temperature range is different for each author.

Figure 6. Relative deviations of calculated values by the background equation from the experimental data of Tsvetkov et al.14 along the saturation curve.

The best agreement was found with the measured values of Makita et al.10 Dense Fluid Thermal Conductivity To determined the excess function or the residual term of the thermal conductivity δλ(F,T), we have performed

Journal of Chemical and Engineering Data, Vol. 46, No. 2, 2001 197

Figure 7. Relative deviations of calculated values by the background equation from the experimental data of Yata et al.15 along the saturation curve. Table 8. Thermal Conductivity of HCFC-22 along the Quasi-Isotherm T ) 337 K T/K

P/MPa

F/kg‚m-3

λ/mW‚m-1‚K-1

337.14 337.13 337.12 337.11 337.10 337.90 337.08 337.08 337.70 337.06 337.06 337.05 337.05 337.04 337.03 337.03 337.02 337.02 337.01 337.00 337.00 337.00 337.00 336.99 336.99 336.99 336.98 336.98 336.98 336.98 336.97 336.97 336.96 336.96 336.96 336.95 336.95 336.95 336.95 336.95 336.94 336.94 336.94 336.94

3.00 4.00 5.00 6.00 7.00 8.00 9.00 10.00 11.00 12.00 13.00 14.00 15.00 16.00 17.00 18.00 19.00 20.00 21.00 22.00 23.00 24.00 25.00 26.00 27.00 28.00 29.00 30.00 31.00 32.00 33.00 34.00 35.00 36.00 37.00 38.00 39.00 40.00 41.00 42.00 43.00 44.00 45.00 46.00

1014.2 1030.3 1044.1 1056.4 1067.3 1077.4 1086.6 1095.3 1103.3 1110.9 1118.1 1124.9 1131.5 1137.7 1143.6 1149.4 1154.8 1160.1 1165.2 1170.2 1175.0 1179.6 1184.1 1188.6 1192.8 1197.0 1201.0 1204.9 1208.9 1212.6 1216.3 1219.9 1223.4 1226.9 1230.3 1233.6 1236.8 1240.0 1243.1 1246.2 1249.3 1252.3 1255.2 1258.1

65.98 67.12 68.30 69.53 70.80 71.89 73.01 73.70 74.65 75.38 76.36 77.11 77.89 78.68 79.48 80.30 81.13 81.98 82.56 83.44 84.04 84.64 85.26 85.88 86.52 87.16 87.49 88.15 88.81 89.15 89.83 90.53 91.23 91.58 92.30 93.03 93.77 94.15 94.53 94.91 95.30 95.68 96.07 96.46

measurements in the liquid phase and in the gas phase far away from the critical region along 14 quasi-isotherms at 299.4 K, 300.8 K, 302.5 K, 309.4 K, 317.7 K, 337 K, 356.5 K, 375.8 K, 393.8 K, 413.3 K, 453 K, 473 K, 493 K, and 514.2 K. Experimental results are listed in Tables 3-17. The excess function of the thermal conductivity, shown in

Figure 8. Relative deviations of calculated values by the background equation from the tabulated data of Vargaftik et al.8 Table 9. Thermal Conductivity of HCFC-22 along the Quasi-Isotherm T ) 356.5 K T/K

P/MPa

F/kg‚m-3

λ/mW‚m-1‚K-1

356.58 356.57 356.56 356.55 356.54 356.53 356.51 356.50 356.50 356.48 356.47 356.47 356.46 356.45 356.44 356.44 356.43 356.42 356.42 356.42 356.41 356.41 356.40 356.39 356.39 356.39 356.38 356.38 356.38 356.37 356.37 356.36 356.36 356.36 356.35 356.35 356.35 356.34 356.34 356.34 356.34 356.34 356.33

4.00 5.00 6.00 7.00 8.00 9.00 10.00 11.00 12.00 13.00 14.00 15.00 16.00 17.00 18.00 19.00 20.00 21.00 22.00 23.00 24.00 25.00 26.00 27.00 28.00 29.00 30.00 31.00 32.00 33.00 34.00 35.00 36.00 37.00 38.00 39.00 40.00 41.00 42.00 43.00 44.00 45.00 46.00

866.1 910.3 938.93 960.8 978.8 994.2 1007.9 1020.1 1031.3 1041.6 1051.1 1060.0 1068.4 1076.2 1083.7 1090.9 1097.7 1104.1 1110.4 1116.3 1122.1 1127.7 1133.0 1138.2 1143.2 1148.1 1152.8 1157.4 1161.9 1166.3 1170.5 1174.6 1178.6 1182.6 1186.4 1190.3 1193.9 1197.5 1201.0 1204.6 1207.9 1211.3 1214.5

59.49 60.55 61.66 62.80 63.83 64.86 66.12 67.24 68.40 69.40 70.63 71.48 72.36 73.23 74.14 75.07 76.03 76.76 77.51 78.27 79.04 79.84 80.57 81.19 81.74 82.58 83.15 83.73 84.33 84.92 85.52 86.14 86.76 87.39 88.03 88.68 89.34 90.01 90.35 90.69 91.03 91.38 91.72

Figure 3, was found to be temperature independent and was represented by a sixth-order polynomial of the form

δλ ΛC

6

)

∑b

i

i)1

() F

FC

i

(8)

where FC ) 520 kg‚m-3 is the critical density, the coef-

198




T/K

P/MPa

F/kg‚m-3

λ/mW‚m-1‚K-1

T/K

P/MPa

F/kg‚m-3

λ/mW‚m-1‚K-1

375.88 375.86 375.83 375.81 375.80 375.78 375.78 375.76 375.75 375.74 375.73 375.72 375.71 375.70 375.70 375.70 375.68 375.68 375.67 375.67 375.66 375.66 375.65 375.65 375.65 375.64 375.63 375.63 375.62 375.62 375.62 375.61 375.61 375.61 375.60 375.60 375.60 375.60 375.59 375.59

7.00 8.00 9.00 10.00 11.00 12.00 13.00 14.00 15.00 16.00 17.00 18.00 19.00 20.00 21.00 22.00 23.00 24.00 25.00 26.00 27.00 28.00 29.00 30.00 31.00 32.00 33.00 34.00 35.00 36.00 37.00 38.00 39.00 40.00 41.00 42.00 43.00 44.00 45.00 46.00

792.4 841.5 874.6 900.0 920.9 938.7 954.4 968.4 981.1 992.7 1003.4 1013.4 1022.7 1031.5 1039.8 1047.7 1055.2 1062.4 1069.2 1075.8 1082.1 1088.1 1094.0 1099.6 1105.1 1110.4 1115.5 1120.5 1125.3 1130.0 1134.6 1139.1 1143.4 1147.7 1151.8 1155.9 1159.8 1163.7 1167.5 1171.2

54.25 55.89 57.49 58.89 60.07 61.43 62.54 63.69 64.89 65.94 67.03 68.16 69.13 70.12 70.94 71.78 72.63 73.50 74.40 75.09 75.79 76.50 77.23 77.97 78.46 79.23 80.00 80.53 81.33 81.88 82.43 82.99 83.55 84.12 84.71 85.30 85.60 86.20 86.81 87.43

393.90 393.89 393.88 393.87 393.87 393.86 383.86 393.85 393.85 393.84 393.84 393.83 393.83 393.83 393.83 393.83 393.82 393.82 393.82 393.82 393.82 393.82 393.82 393.81 393.81 393.81 393.81 393.81 393.80 393.80 393.80 393.79

15.00 16.00 17.00 18.00 19.00 20.00 21.00 22.00 23.00 24.00 25.00 26.00 27.00 28.00 29.00 30.00 31.00 32.00 33.00 34.00 35.00 36.00 37.00 38.00 39.00 40.00 41.00 42.00 43.00 44.00 45.00 46.00

897.6 913.8 928.3 941.6 953.8 965.1 975.6 985.5 994.8 1003.6 1011.9 1019.8 1027.4 1034.6 1041.6 1048.2 1054.7 1060.9 1066.8 1072.6 1078.2 1083.6 1086.8 1094.0 1098.9 1103.7 1108.4 1113.0 1117.5 1121.8 1126.1 1130.3

61.12 62.49 63.64 64.82 66.05 67.00 67.98 68.99 69.67 70.38 71.09 71.82 72.56 73.32 73.71 74.09 74.89 75.69 76.10 76.52 77.36 77.36 78.22 79.10 79.10 79.55 80.00 80.46 81.40 81.39 81.86 82.34

ficients bi in eq 8 are b1 ) 0.533 878, b2 ) -0.103 528 74, b3 ) 1.328 889 7, b4 ) -1.100 191, b5 ) 0.387 148 1, and b6 ) - 0.045 501 816, and ΛC ) 17.4 mW‚m-1‚K-1. In the liquid range, we have compared, as a function of density, the values calculated by our background equation (λB) with the experimental data measured by Assael et al.12 (Figure 4) and Kim et al.13 (Figure 5). The agreement is very good since the mean deviations are within the experimental uncertainties ((1.5%). This good agreement shows that our background equation can be used to calculated the thermal conductivities of HCFC-22 at lower temperatures. Along the saturation curve, similar comparisons, as a function of temperature, are shown with the experimental data of Tsvetkov et al.14 (Figure 6) and those of Yata et al.15 (Figure 7). The mean deviations with the data of Yata et al.15 are within the experimental uncertainties ((1.5%). The deviations are slightly larger with the data of Tsvetkov et al.14 The relative deviations with the tabulated data of Vargaftik et al.8 are displayed in Figure 8. The agreement is poor except in a limited temperature range around 300 K. Thermal Conductivity in the Critical Region Around the critical density the well-know enhancement of the thermal conductivity was observed. This critical enhancement of the thermal conductivity ∆λ(T,F) was carefully measured along several quasi-isotherms. Some preliminary results are reported along the critical isochore

Table 12. Thermal Conductivity of HCFC-22 along the Quasi-Isotherm T ) 413.3 K T/K

P/MPa

F/kg‚m-3

λ/mW‚m-1‚K-1

413.35 413.34 413.34 413.33 413.32 413.31 413.31 413.32 413.31 413.30 413.30 413.29 413.29 413.29 413.29 413.28 413.28 413.28 413.28 413.27 413.27 413.36 413.27 413.26 413.26 413.26 413.26 413.26 413.25 413.25 413.25 413. 25

15.00 16.00 17.00 18.00 19.00 20.00 21.00 22.00 23.00 24.00 25.00 26.00 27.00 28.00 29.00 30.00 31.00 32.00 33.00 34.00 35.00 36.00 37.00 38.00 39.00 40.00 41.00 42.00 43.00 44.00 45.00 46.00

797.5 820.6 840.8 858.8 875.0 889.7 903.2 915.7 927.4 938.3 948.5 958.2 967.4 976.1 984.3 992.3 999.8 1007.1 1014.1 1020.8 1027.3 1033.6 1039.6 1045.5 1051.1 1056.7 1062.0 1067.2 1072.3 1077.2 1082.0 1086.7

55.51 56.84 57.95 59.40 60.61 60.92 62.19 63.18 63.86 64.90 65.97 66.71 67.46 67.85 68.62 69.42 69.83 70.65 71.49 71.92 72.35 73.24 74.14 74.60 75.08 76.02 76.51 77.00 77.49 78.00 78.51 79.02

(Table 18) and compared to an equation assuming the classical divergence with the critical exponent equal to -0.65

∆T ) 1.7∆T-0.65

(9)

Journal of Chemical and Engineering Data, Vol. 46, No. 2, 2001 199 Table 13. Thermal Conductivity of HCFC-22 along the Quasi-Isotherm T ) 433.8 K

Table 15. Thermal Conductivity of HCFC-22 along the Quasi-Isotherm T ) 473 K

T/K

P/MPa

F/kg‚m-3

λ/mW‚m-1‚K-1

T/K

P/MPa

F/kg‚m-3

λ/mW‚m-1‚K-1

432.80 432.80 432.79 432.78 432.77 432.77 432.76 432.75 432.74 432.74 432.74 432.74 432.73 432.73 432.72 432.72 432.72 432.72 432.71 432.71 432.71 432.70 432.70 432.70 432.70 432.70

15.00 16.00 17.00 18.00 19.00 20.00 21.00 22.00 23.00 24.00 25.00 26.00 27.00 28.00 29.00 30.00 31.00 32.00 33.00 34.00 35.00 36.00 37.00 38.00 39.00 40.00

691.9 722.4 748.9 772.1 792.9 811.5 828.4 843.9 858.2 871.5 883.9 895.5 906.4 916.70 926.49 935.79 944.59 953.10 961.09 968.89 976.29 983.49 990.4 997.1 1003.5 1009.7

50.71 52.03 53.41 54.87 56.14 57.21 58.31 59.45 60.64 61.57 62.52 63.16 64.16 64.84 65.90 66.62 66.99 67.35 68.10 68.49 69.27 70.06 70.46 71.29 71.70 72.12

473.14 473.13 473.12 473.10 473.08 473.06 473.03 473.00 472.97 472.93 472.90 472.87 472.83 472.81 472.78 472.76 472.74 472.72 472.71 472.70 472.69 472.68 472.67 472.66 472.65 472.64 472.64 472.63 472.63 472.63 472.62 472.61 472.61 472.60 472.60 472.60 472.59 472.59 472.58 472.58 472.58 472.57 472.57 472.57 472.57 472.56 472.56

0.10 1.00 2.00 3.00 4.00 5.00 6.00 7.00 8.00 9.00 10.00 11.00 12.00 13.00 14.00 15.00 16.00 17.00 18.00 19.00 20.00 21.00 22.00 23.00 24.00 25.00 26.00 27.00 28.00 29.00 30.00 31.00 32.00 33.00 34.00 35.00 36.00 37.00 38.00 39.00 40.00 41.00 42.00 43.00 44.00 45.00 46.00

2.29 22.7 46.8 72.5 100.0 129.5 161.1 195.0 231.2 269.5 309.8 351.2 393.0 434.1 473.7 511.0 545.7 577.6 606.8 633.5 657.9 680.2 700.8 719.8 737.5 753.9 769.2 783.5 797.0 809.7 821.8 833.2 844.0 854.4 864.2 873.7 882.7 891.4 899.7 907.8 915.5 923.0 930.2 937.2 943.9 950.5 956.8

23.39 23.64 24.02 24.56 25.09 25.86 26.91 28.10 29.52 31.09 32.73 34.56 36.70 38.54 40.35 42.19 44.06 45.80 47.20 48.67 49.88 51.16 52.10 53.08 54.10 55.17 56.26 57.17 58.11 59.08 60.09 60.86 61.65 62.47 63.30 63.87 64.74 65.36 66.24 67.18 67.82 68.48 69.14 69.81 70.16 70.51 70.86

Table 14. Thermal Conductivity of HCFC-22 along the Quasi-Isotherm T ) 453 K T/K

P/MPa

F/kg‚m-3

λ/mW‚m-1‚K-1

453.18 453.16 453.15 453.13 453.10 453.09 453.04 452.99 452.95 452.90 452.85 452.82 452.77 452.75 452.72 452.70 452.68 452.66 452.65 452.64 452.63 452.62 452.61 452.61 452.60 452.60 452.59 452.58 452.56 452.57 452.57 452.56 452.56 452.55 452.55 452.54 452.54 452.54 452.53 452.53 452.53 452.52 452.52 452.52 452.52 452.51 452.51

0.10 1.00 2.00 3.00 4.00 5.00 6.00 7.00 8.00 9.00 10.00 11.00 12.00 13.00 14.00 15.00 16.00 17.00 18.00 19.00 20.00 21.00 22.00 23.00 24.00 25.00 26.00 27.00 28.00 29.00 30.00 31.00 32.00 33.00 34.00 35.00 36.00 37.00 38.00 39.00 40.00 41.00 42.00 43.00 44.00 45.00 46.00

2.40 23.8 49.4 77.1 107.3 140.2 176.5 216.4 260.1 307.6 358.0 409.6 460.5 508.6 552.6 591.9 626.9 657.8 685.4 710.0 732.3 752.4 770.9 787.8 803.5 818.0 831.6 844.4 856.3 867.7 878.4 888.5 898.2 907.4 916.3 924.7 932.8 940.6 948.2 955.4 962.4 969.1 975.7 982.0 988.2 994.1 999.9

21.88 22.14 22.52 23.04 23.70 24.45 25.89 27.49 29.29 31.33 33.73 35.77 38.36 40.49 42.61 44.52 46.29 48.04 49.57 51.00 52.33 53.52 54.56 55.41 56.52 57.44 58.63 59.62 60.63 61.43 62.23 63.34 64.19 65.08 65.68 66.60 67.22 67.54 68.85 69.52 70.55 71.25 71.97 72.33 72.70 73.44 74.21

where ∆T ) (T - TC)/TC. The agreement is very satisfactory except for the first point near the critical temperature, which is much lower than the calculated one. The same discrepancy was already observed for other refrigerants. This indicates that in a temperature range within one degree above the critical temperature, the measured thermal conductivity values which are integrated over a small temperature gradient are always lower than those predicted by scaling theory. Due to the lack of a scaled equation of state near the critical point, it was not possible to follow the elaborated methodology proposed by Olchowy and Sengers16 to calculate crossover functions and analyze the critical enhancement in the crossover region. Conclusion New measurements of the thermal conductivity of HCFC-22 have been presented in the temperature range from 300 K to 515 K along 14 quasi-isotherms and at pressures up to 55 MPa, with an estimated uncertainty of (1.5%. A background equation was determined which can be used to calculate the thermal conductivity from 220 K

200


Table 16. Thermal Conductivity of HCFC-22 along the Quasi-Isotherm T ) 493 K


T/K

P/MPa

F/kg‚m-3

λ/mW‚m-1‚K-1

T/K

P/MPa

F/kg‚m-3

λ/mW‚m-1‚K-1

493.17 493.17 493.16 493.14 493.13 493.11 493.10 493.07 493.04 493.02 492.99 492.97 492.94 492.92 492.90 492.87 492.86 492.84 492.83 492.82 492.80 492.79 492.78 492.77 492.77 492.76 492.75 492.75 492.74 492.73 492.73 492.72 492.72 492.71 492.71 492.70 492.70 492.70 492.69 492.69 492.68 492.68 492.68 492.68 492.67 492.67 492.67

0.10 1.00 2.00 3.00 4.00 5.00 6.00 7.00 8.00 9.00 10.00 11.00 12.00 13.00 14.00 15.00 16.00 17.00 18.00 19.00 20.00 21.00 22.00 23.00 24.00 25.00 26.00 27.00 28.00 29.00 30.00 31.00 32.00 33.00 34.00 35.00 36.00 37.00 38.00 39.00 40.00 41.00 42.00 43.00 44.00 45.00 46.00

2.17 21.7 44.5 68.6 93.9 120.8 149.1 178.9 210.2 242.9 276.8 311.6 346.8 381.9 416.5 450.0 482.0 512.4 540.9 567.6 592.5 615.7 637.3 657.5 676.3 693.9 710.5 726.0 740.7 754.5 767.6 780.1 791.9 803.2 814.0 824.3 834.2 843.6 852.7 861.5 869.9 878.0 885.9 893.4 900.8 907.9 914.8

24.85 25.13 25.52 25.93 26.44 27.09 27.94 28.85 29.94 30.98 32.24 33.59 35.07 36.77 38.20 40.10 41.55 42.97 44.34 45.66 46.89 48.35 49.55 50.62 51.56 52.52 53.53 54.35 55.42 56.31 57.23 58.17 58.90 59.64 60.41 61.19 62.00 62.82 63.39 64.25 64.84 65.43 66.04 66.66 67.29 67.94 68.26

514.32 514.32 514.31 514.30 514.29 514.27 514.26 514.24 514.23 514.21 514.19 514.18 514.16 514.14 514.12 514.10 514.08 514.06 514.05 514.04 514.03 514.01 514.00 513.99 513.98 513.97 513.97 513.96 513.96 513.96 513.95 513.94 513.94 513.93 513.93 513.92 513.92 513.91 513.91 513.91 513.90 513.90 513.89 513.89 513.89 513.89 513.89

0.10 1.00 2.00 3.00 4.00 5.00 6.00 7.00 8.00 9.00 10.00 11.00 12.00 13.00 14.00 15.00 16.00 17.00 18.00 19.00 20.00 21.00 22.00 23.00 24.00 25.00 26.00 27.00 28.00 29.00 30.00 31.00 32.00 33.00 34.00 35.00 36.00 37.00 38.00 39.00 40.00 41.00 42.00 43.00 44.00 45.00 46.00

2.07 20.7 42.3 64.9 88.5 113.1 138.8 165.5 193.2 221.9 251.3 281.3 311.6 342.0 372.1 401.8 430.6 458.5 485.2 510.7 534.8 557.7 579.3 599.7 619.0 637.2 654.3 670.6 686.0 700.6 714.5 727.8 740.4 752.4 763.9 775.0 785.5 795.7 805.4 814.8 823.9 832.6 841.0 849.2 857.1 864.7 872.1

26.63 26.84 27.17 27.62 28.03 28.52 29.01 29.72 30.40 31.18 32.23 33.34 34.54 35.72 36.99 38.23 39.67 41.22 42.63 43.99 45.14 46.51 47.63 48.80 49.84 50.94 51.89 52.87 53.67 54.52 55.60 56.27 56.96 57.90 58.62 59.37 60.13 60.65 61.44 61.99 62.53 63.09 63.66 64.24 64.84 65.44 66.05

to 600 K with an accuracy of (2%. It is obvious that in the critical region a supplementary functional form must be added to account for the critical enhancement.16

We are indebted to ATOCHEM for providing us HCFC22 samples. List of Symbols

k M P R T T* ) kT/

Greek Letters λ0

Acknowledgment

ai Ai bi CP0

∆T ) (T - TC)/TC reduced temperature

λB ΛC δλ

constants in eq 5 constants in eq 6 constants in eq 8 ideal isobaric heat capacity, kJ‚kg-1‚K-1 Boltzmann constant, J‚K-1 molar mass, g‚mol-1 pressure, MPa universal gas constant, kJ‚kg-1‚K-1 temperature, K reduced temperature

∆λ θi F σ τ ) TC/T Ωλ*

energy scaling factor, J thermal conductivity at atmospheric pressure, mW‚m-1‚K-1 background thermal conductivity, mW‚m-1‚K-1 excess thermal conductivity at TC, mW‚m-1‚K-1 excess function of thermal conductivity, mW‚m-1‚K-1 thermal conductivity enhancement, mW‚m-1‚K-1 constants in eq 5 density, kg‚m-3 length scaling factor, nm reduced temperature reduced collision integral

Subscripts c

critical

Journal of Chemical and Engineering Data, Vol. 46, No. 2, 2001 201 Table 18. Thermal Conductivity of HCFC-22 along the Critical Isochore T/K 369.61 369.62 370.91 370.91 371.91 371.91 372.75 372.75 373.86 373.86 375.65 375.65 378.78 383.62 383.62 388.67 388.67 394.0 413.4

∆T/K 10-4

8.94 × 9.21 × 10-4 4.41 × 10-3 4.41 × 10-3 7.12 × 10-3 7.12 × 10-3 9.40 × 10-3 9.40 × 10-3 1.24 × 10-2 1.24 × 10-2 1.72 × 10-2 1.72 × 10-2 2.57 × 10-2 3.88 × 10-2 3.88 × 10-2 5.25 × 10-2 5.25 × 10-2 6.69 × 10-2 1.19 × 10-1

F/kg‚m-3

λ/mW‚m-1‚K-1

∆λexp/mW‚m-1‚K-1

∆λcal/mW‚m-1‚K-1

100(λcal - λexp)/λexp

540.0 505.4 523.6 516.9 525.9 515.3 522.5 514.5 530.5 519.1 524.1 515.9 520.1 526.0 519.2 525.2 500.6 518.7 536.0

118.97 117.96 86.41 86.41 74.12 73.72 68.41 68.07 63.59 63.59 57.27 57.04 51.67 48.18 47.85 44.66 43.65 44.39 43.49

85.06 85.88 53.28 53.63 40.79 40.94 35.2 35.28 29.86 30.46 23.75 23.94 18.11 13.95 13.97 10.08 10.36 9.74 6.43

163.0 159.9 57.71 57.71 42.29 42.29 35.31 35.31 29.49 29.49 23.79 23.79 18.35 14.04 14.04 11.54 11.54 9.85 6.78

65.5 62.7 5.1 4.7 2.0 1.8 0.2 0.0 -0.6 -1.5 0.1 -0.3 0.5 0.2 0.1 3.3 2.7 0.2 0.8

Literature Cited (1) Wagner, W.; Marx, V.; Pruss, A. Rev. Int. Froid 1993, 16, 373389. (2) Sousa, A. T.; Fialho, P. S.; Nieto de Castro, C. A.; Tufeu, R.; Le Neindre, B. Int. J. Thermophys. 1992, 13, 363-399. (3) Le Neindre, B.; Garrabos, Y. Int. J. Thermophys. 1999, 20, 375399. (4) Le Neindre, B.; Garrabos, Y. Int. J. Thermophys. 1999, 20, 13791401. (5) Le Neindre, B.; Tufeu, R. Measurements of the Thermal Conductivity of Fluids by the Coaxial Cylinder Method. In Experimental Thermodynamics III, Measurements of the Transport Properties of Fluids; Wakeham, W. A., Nagashima, A., Sengers, J. V., Eds.; Blackwell: Oxford, 1991; pp 111-142. (6) Maitland, G. C.; Rigby, M.; Smith, E. B.; Wakeham, W. A. Intermolecular Forces: Their Origin and Determination; Clarendon Press: Oxford, 1987. (7) Mayinger, T. F.; Nabizadeh, H. Viscosity of gaseous pure refrigerants and their mixtures, Klima und Ka¨ltetagung Bremen, Nov. 1992. Dtsch. Ka¨ lte Klimatech. 1992, Ver. 19, Bd 2.

(8) Vargaftik, N. B.; Filippov, L. P.; Tarzimanov, A. A.; Totskii, E. E. Handbook of Thermal Conductivity of Liquids and Gases; CRC Press: Boca Raton, FL, 1994. (9) Watanabe, K.; et al., Chlorodifluoromethane (HCFC-22). Thermophys. Prop. Refrig. 1975, 1-123. (10) Makita, T.; Tanaka, Y.; Morimoto, Y.; Noguchi, M.; Kubota, H. Int. J. Thermophys. 1981, 2, 249. (11) Hammerschmidt, U. Int. J. Thermophys. 1995, 16, 1203-1211. (12) Assael, M. J.; Karagiannidis E. Int. J. Thermophys. 1993, 14, 183-197. (13) Kim, S. H.; Kim, D. S.; Kim, M. S.; Ro, S. T. Int. J. Thermophys. 1993, 14, 937-950. (14) Tsvetkov, O. B.; Laptev, Yu. A.; Asambaev, A. G. Int. J. Thermophys. 1996, 17, 597-606. (15) Yata, J.; Minaminayama, T.; Tanaka, S. Int. J. Thermophys. 1984, 5, 209-218. (16) Olchowy, G. A.; Sengers, J. V. Int. J. Thermophys. 1989, 10, 417426. Received for review July 12, 2000. Accepted October 11, 2000.

JE0002078

HCFC-22 - American Chemical Society

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