Heat Transfer Handbook part 11 doc

BOOKCOMP, Inc. — John Wiley & Sons / Page 90 / 2nd Proofs / Heat Transfer Handbook / Bejan 90 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 [90], (48) Lines: 1596 to 1628 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [90], (48) TABLE 2.7 Thermophysical Properties of Fluids along the Saturation Line a (Continued) Water (R-718) (Continued) η (vap.) 9.9195 11.487 13.192 14.056 14.917 15.779 16.653 17.564 18.563 19.749 21.350 λ (liq.) 610.28 668.00 683.64 681.72 674.59 662.21 644.05 619.08 585.95 544.05 495.46 λ (vap.) 18.673 22.707 28.347 31.873 35.904 40.471 45.666 51.756 59.456 70.685 91.052 σ 0.0717 0.0632 0.0536 0.0483 0.0429 0.0373 0.0315 0.0256 0.0197 0.0139 0.0084 Xenon T 180.00 190.00 200.00 210.00 220.00 230.00 240.00 250.00 260.00 270.00 280.00 p 0.2216 0.3477 0.5207 0.7499 1.0446 1.4146 1.8700 2.4215 3.0807 3.8611 4.7805 ρ (liq.) 2837.0 2766.5 2692.6 2614.8 2532.0 2443.0 2346.0 2238.0 2114.4 1965.5 1764.6 ρ (vap.) 20.542 31.174 45.483 64.297 88.648 119.90 159.97 211.82 280.44 375.85 525.13 h (liq.) 5.1356 8.6275 12.193 15.858 19.653 23.614 27.795 32.271 37.165 42.717 49.568 h (vap.) 97.052 97.849 98.437 98.785 98.853 98.589 97.919 96.734 94.846 91.891 86.911 s (liq.) 0.0295 0.0482 0.0661 0.0836 0.1007 0.1177 0.1346 0.1519 0.1699 0.1894 0.2125 s (vap.) 0.5402 0.5178 0.4974 0.4785 0.4607 0.4436 0.4268 0.4098 0.3918 0.3716 0.3459 c v (liq.) 0.1613 0.1567 0.1528 0.1493 0.1463 0.1438 0.1420 0.1411 0.1418 0.1454 0.1565 c v (vap.) 0.1066 0.1102 0.1143 0.1189 0.1241 0.1297 0.1361 0.1436 0.1527 0.1649 0.1838 c p (liq.) 0.3442 0.3498 0.3579 0.3691 0.3842 0.4049 0.4342 0.4780 0.5496 0.6897 1.1092 c p (vap.) 0.1865 0.1970 0.2104 0.2274 0.2493 0.2785 0.3193 0.3806 0.4834 0.6918 1.3341 w (liq.) 599.04 570.00 540.11 509.18 476.96 443.11 407.13 368.28 325.30 275.99 215.47 w (vap.) 133.38 135.47 137.12 138.33 139.09 139.38 139.19 138.48 137.18 135.11 131.75 η (liq.) 398.17 349.91 308.34 272.06 240.00 211.31 185.32 161.41 138.96 117.20 94.450 η (vap.) 14.780 15.592 16.460 17.398 18.428 19.577 20.889 22.432 24.333 26.859 30.802 λ (liq.) 64.909 61.180 57.451 53.748 50.081 46.442 42.812 39.160 35.494 32.045 29.622 λ (vap.) 3.5348 3.7825 4.0521 4.3506 4.6887 5.0845 5.5731 6.2321 7.2516 9.1505 13.683 σ 0.0157 0.0138 0.0121 0.0104 0.0087 0.0072 0.0057 0.0042 0.0029 0.0017 0.0007 BOOKCOMP, Inc. — John Wiley & Sons / Page 91 / 2nd Proofs / Heat Transfer Handbook / Bejan 91 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 [91], (49) Lines: 1628 to 1662 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [91], (49) R-11 (Trichlorofluoromethane, CFC-11) T 200.00 225.00 250.00 275.00 300.00 325.00 350.00 375.00 400.00 425.00 450.00 p 0.00043 0.0030 0.0134 0.0435 0.1131 0.2492 0.4847 0.8570 1.4074 2.1811 3.2329 ρ (liq.) 1691.9 1639.2 1585.4 1529.9 1471.9 1410.2 1343.5 1269.9 1185.7 1084.1 943.21 ρ (vap.) 0.0358 0.2212 0.8909 2.6678 6.4840 13.590 25.648 45.010 75.450 124.37 212.96 h (liq.) 138.94 159.42 180.30 201.59 223.40 245.84 269.08 293.34 318.92 346.46 377.77 h (vap.) 353.48 365.46 377.93 390.72 403.59 416.24 428.30 439.34 448.79 455.64 457.26 s (liq.) 0.7403 0.8368 0.9247 1.0058 1.0815 1.1530 1.2214 1.2876 1.3524 1.4175 1.4867 s (vap.) 1.8130 1.7525 1.7153 1.6936 1.6822 1.6774 1.6763 1.6769 1.6771 1.6744 1.6633 c v (liq.) 0.5569 0.5687 0.5790 0.5886 0.5984 0.6085 0.6191 0.6307 0.6439 0.6611 0.6891 c v (vap.) 0.4135 0.4469 0.4790 0.5090 0.5367 0.5624 0.5871 0.6119 0.6383 0.6685 0.7082 c p (liq.) 0.8101 0.8273 0.8427 0.8605 0.8826 0.9105 0.9461 0.9935 1.0636 1.1918 1.5893 c p (vap.) 0.4748 0.5096 0.5441 0.5781 0.6123 0.6489 0.6919 0.7488 0.8358 1.0024 1.5284 w (liq.) 1099.1 996.42 900.09 810.44 725.77 644.16 563.73 482.57 398.34 307.60 203.77 w (vap.) 117.77 124.15 129.86 134.61 138.07 139.87 139.68 137.09 131.61 122.37 107.74 η (liq.) 1752.4 1028.3 702.05 516.70 396.78 312.19 248.58 198.16 156.21 119.39 83.759 η (vap.) 7.6997 8.5563 9.4064 10.244 11.077 11.931 12.857 13.960 15.481 18.227 λ (liq.) 118.01 109.32 101.20 93.558 86.285 79.291 72.483 65.765 59.050 52.286 46.661 λ (vap.) 5.5342 6.4895 7.4898 8.5279 9.6226 10.801 12.138 13.754 16.074 20.850 σ 0.0311 0.0275 0.0241 0.0207 0.0175 0.0143 0.0113 0.0085 0.0058 0.0034 0.0013 R-113 (1,1,2-Trichloro-1,2,2-trifluoroethane, CFC-113) T 260.00 280.00 300.00 320.00 340.00 360.00 380.00 400.00 420.00 440.00 460.00 p 0.0076 0.0208 0.0482 0.0989 0.1840 0.3166 0.5113 0.7840 1.1522 1.6354 2.2568 ρ (liq.) 1652.1 1605.8 1558.6 1510.0 1459.3 1405.9 1348.5 1285.7 1215.0 1131.6 1023.5 ρ (vap.) 0.6670 1.6931 3.7087 7.2565 13.018 21.851 34.881 53.693 80.766 120.59 183.51 h (liq.) 188.29 206.16 224.37 242.98 262.01 281.52 301.58 322.27 343.77 366.38 390.82 h (vap.) 350.90 362.90 375.16 387.54 399.91 412.16 424.11 435.57 446.26 455.69 462.82 continued BOOKCOMP, Inc. — John Wiley & Sons / Page 92 / 2nd Proofs / Heat Transfer Handbook / Bejan 92 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 [92], (50) Lines: 1662 to 1695 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [92], (50) TABLE 2.7 Thermophysical Properties of Fluids along the Saturation Line a (Continued) R-113 (1,1,2-Trichloro-1,2,2-trifluoroethane, CFC-113) (Continued) s (liq.) 0.9561 1.0223 1.0850 1.1449 1.2025 1.2580 1.3118 1.3643 1.4160 1.4676 1.5207 s (vap.) 1.5815 1.5821 1.5876 1.5967 1.6081 1.6208 1.6342 1.6475 1.6600 1.6706 1.6772 c v (liq.) 0.6368 0.6535 0.6712 0.6885 0.7053 0.7214 0.7372 0.7531 0.7700 0.7895 0.8159 c v (vap.) 0.5605 0.5867 0.6118 0.6360 0.6598 0.6833 0.7069 0.7309 0.7560 0.7834 0.8165 c p (liq.) 0.8855 0.9014 0.9196 0.9396 0.9617 0.9868 1.0165 1.0540 1.1063 1.1925 1.3875 c p (vap.) 0.6063 0.6342 0.6619 0.6904 0.7206 0.7541 0.7929 0.8413 0.9087 1.0201 1.2754 w (liq.) 828.94 759.92 692.84 628.04 565.13 503.50 442.41 380.97 317.99 251.65 179.46 w (vap.) 111.03 114.38 117.08 118.97 119.89 119.66 118.07 114.87 109.72 102.05 90.902 η (liq.) 1217.5 859.37 645.95 504.29 403.15 326.93 266.92 217.88 176.32 139.65 105.13 η (vap.) 8.3780 9.0218 9.6611 10.288 10.918 11.561 12.237 12.986 13.879 15.069 16.948 λ (liq.) 76.719 72.151 67.853 63.782 59.900 56.168 52.545 48.991 45.465 41.934 38.567 λ (vap.) 6.8569 7.7005 8.5700 9.4607 10.385 11.348 12.370 13.485 14.754 16.351 18.804 σ 0.0216 0.0193 0.0170 0.0148 0.0126 0.0105 0.0085 0.0066 0.0048 0.0031 0.0016 R-114 (1,2-Dichloro-1,1,2,2-tetrafluoroethane, CFC-114) T 280.00 300.00 320.00 330.00 340.00 350.00 360.00 370.00 380.00 390.00 400.00 p 0.1145 0.2275 0.4102 0.5350 0.6862 0.8670 1.0811 1.3323 1.6246 1.9630 2.3530 ρ (liq.) 1508.8 1449.0 1384.6 1350.1 1313.5 1274.5 1232.4 1186.1 1134.0 1073.5 998.95 ρ (vap.) 8.7845 16.788 29.651 38.550 49.568 63.201 80.128 101.34 128.36 163.86 213.09 h (liq.) 206.60 226.22 246.49 256.91 267.54 278.42 289.59 301.10 313.05 325.60 339.09 h (vap.) 341.38 353.56 365.44 371.18 376.73 382.04 387.03 391.61 395.62 398.84 400.80 s (liq.) 1.0238 1.0912 1.1562 1.1880 1.2194 1.2505 1.2815 1.3125 1.3436 1.3754 1.4086 s (vap.) 1.5052 1.5157 1.5279 1.5343 1.5405 1.5466 1.5522 1.5571 1.5609 1.5632 1.5629 c v (liq.) 0.6839 0.7019 0.7215 0.7317 0.7421 0.7527 0.7637 0.7753 0.7878 0.8018 0.8189 c v (vap.) 0.6250 0.6523 0.6804 0.6950 0.7102 0.7262 0.7431 0.7615 0.7818 0.8047 0.8317 c p (liq.) 0.9661 0.9945 1.0300 1.0511 1.0754 1.1043 1.1400 1.1867 1.2530 1.3589 1.5650 BOOKCOMP, Inc. — John Wiley & Sons / Page 93 / 2nd Proofs / Heat Transfer Handbook / Bejan 93 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 [93], (51) Lines: 1695 to 1730 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [93], (51) c p (vap.) 0.6833 0.7193 0.7624 0.7883 0.8189 0.8562 0.9035 0.9673 1.0600 1.2106 1.5052 w (liq.) 617.82 545.01 472.58 436.26 399.72 362.81 325.38 287.21 248.03 207.45 164.86 w (vap.) 116.64 117.29 116.25 115.00 113.19 110.75 107.63 103.71 98.885 92.999 85.834 η (liq.) 343.29 272.64 218.66 195.98 175.46 156.71 139.36 123.11 107.63 92.535 77.218 η (vap.) 10.092 10.793 11.506 11.878 12.268 12.689 13.158 13.704 14.376 15.264 16.560 λ (liq.) 64.871 60.564 56.352 54.262 52.173 50.077 47.963 48.825 43.667 41.544 39.809 λ (vap.) 9.2879 10.359 11.507 12.125 12.780 13.475 14.238 15.108 16.157 17.541 19.640 σ 0.0129 0.0107 0.0085 0.0074 0.0064 0.0054 0.0045 0.0035 0.0027 0.0018 0.0011 R-115 (Chloropentafluoroethane, CFC-115) T 180.00 200.00 220.00 240.00 260.00 280.00 300.00 310.00 320.00 330.00 340.00 p 0.0038 0.0162 0.0512 0.1303 0.2820 0.5412 0.9480 1.2209 1.5489 1.9398 2.4037 ρ (liq.) 1744.4 1677.4 1608.8 1537.2 1460.6 1376.4 1279.5 1223.5 1159.4 1082.0 978.74 ρ (vap.) 0.3895 1.5196 4.4456 10.647 22.183 42.028 75.066 99.259 131.38 175.92 244.04 h (liq.) 115.98 132.53 149.80 167.90 186.92 207.02 228.47 239.86 251.85 264.73 279.15 h (vap.) 259.35 269.56 280.23 291.10 301.89 312.24 321.65 325.74 329.18 331.56 331.93 s (liq.) 0.6278 0.7150 0.7972 0.8756 0.9513 1.0251 1.0980 1.1346 1.1718 1.2104 1.2521 s (vap.) 1.4244 1.4002 1.3900 1.3890 1.3935 1.4009 1.4086 1.4117 1.4135 1.4129 1.4073 c v (liq.) 0.5034 0.5368 0.5739 0.6103 0.6454 0.6797 0.7151 0.7343 0.7558 0.7820 0.8174 c v (vap.) 0.4522 0.4958 0.5384 0.5806 0.6230 0.6660 0.7111 0.7352 0.7613 0.7912 0.8290 c p (liq.) 0.8125 0.8442 0.8824 0.9253 0.9746 1.0351 1.1198 1.1821 1.2746 1.4387 1.8463 c p (vap.) 0.5072 0.5529 0.6000 0.6506 0.7081 0.7789 0.8799 0.9559 1.0710 1.2797 1.8218 w (liq.) 871.69 771.03 674.85 584.54 498.43 414.26 329.28 285.28 239.30 190.47 138.88 w (vap.) 103.84 108.30 111.73 113.72 113.87 111.69 106.57 102.61 97.474 90.861 82.340 η (liq.) 883.93 580.60 414.58 309.63 236.71 182.31 139.13 120.23 102.44 85.077 66.950 η (vap.) 7.4741 8.3095 9.1393 9.9536 10.782 11.658 12.674 13.297 14.067 15.112 16.776 λ (liq.) 91.430 83.457 76.095 69.224 62.726 56.481 50.364 47.312 44.256 41.293 39.563 λ (vap.) 5.1681 6.2202 7.3494 8.5499 9.8470 11.289 12.986 14.022 15.315 17.123 20.245 σ 0.0193 0.0166 0.0140 0.0115 0.0090 0.0067 0.0046 0.0035 0.0026 0.0017 0.0008 continued BOOKCOMP, Inc. — John Wiley & Sons / Page 94 / 2nd Proofs / Heat Transfer Handbook / Bejan 94 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 [94], (52) Lines: 1730 to 1763 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [94], (52) TABLE 2.7 Thermophysical Properties of Fluids along the Saturation Line a (Continued) R-116 (Hexafluoroethane, FC-116) T 180.00 200.00 210.00 220.00 230.00 240.00 250.00 260.00 270.00 280.00 290.00 p 0.0419 0.1317 0.2128 0.3271 0.4824 0.6866 0.9483 1.2771 1.6854 2.1908 2.8203 ρ (liq.) 1669.5 1582.0 1537.3 1490.1 1439.1 1382.8 1319.4 1247.0 1163.4 1060.3 881.57 ρ (vap.) 3.9752 11.637 18.328 27.699 40.517 57.843 81.290 113.61 160.16 233.17 380.08 h (liq.) 100.42 118.94 128.53 138.45 148.77 159.58 170.94 182.96 195.76 209.77 227.86 h (vap.) 222.95 232.88 237.76 242.54 247.17 251.58 255.64 259.13 261.65 262.42 258.44 s (liq.) 0.5658 0.6630 0.7096 0.7554 0.8008 0.8461 0.8917 0.9378 0.9849 1.0341 1.0953 s (vap.) 1.2465 1.2328 1.2297 1.2285 1.2286 1.2295 1.2305 1.2308 1.2289 1.2222 1.2007 c v (liq.) 0.6433 0.6589 0.6701 0.6828 0.6965 0.7107 0.7247 0.7377 0.7496 0.7642 0.7935 c v (vap.) 0.5151 0.5648 0.5917 0.6194 0.6474 0.6754 0.7029 0.7297 0.7553 0.7782 0.7928 c p (liq.) 0.9172 0.9427 0.9720 1.0088 1.0535 1.1083 1.1760 1.2613 1.3855 1.6746 4.1002 c p (vap.) 0.5872 0.6513 0.6890 0.7309 0.7779 0.8328 0.9010 0.9954 1.1497 1.4589 3.6372 w (liq.) 542.56 509.57 479.05 442.11 400.49 356.12 311.45 268.70 226.45 176.28 107.44 w (vap.) 107.94 110.51 110.91 110.58 109.36 107.03 103.37 98.137 91.227 82.842 72.721 η (liq.) 412.30 288.78 245.42 209.55 179.11 152.66 129.14 107.81 88.060 68.961 46.463 η (vap.) 8.4436 9.4174 9.8763 10.330 10.784 11.251 11.759 12.372 13.256 14.894 19.069 λ (liq.) 75.336 67.094 63.241 59.495 55.816 52.169 48.525 44.893 41.403 38.798 53.980 λ (vap.) 6.5676 7.8096 8.4927 9.2285 10.038 10.939 11.938 13.109 14.691 17.614 27.103 σ 0.0130 0.0103 0.0090 0.0077 0.0064 0.0052 0.0040 0.0029 0.0018 0.0009 0.0001 R-12 (Dichlorodifluoromethane, CFC-12) T 125.00 150.00 175.00 200.00 225.00 250.00 275.00 300.00 325.00 350.00 375.00 p 1.6 × 10 −6 0.000092 0.0014 0.0100 0.0430 0.1331 0.3273 0.6839 1.2694 2.1593 3.4527 ρ (liq.) 1805.2 1739.6 1674.3 1608.0 1539.6 1467.5 1390.1 1304.3 1205.0 1080.3 883.06 ρ (vap.) 0.0002 0.0089 0.1174 0.7307 2.8376 8.1095 18.930 38.700 73.003 133.91 269.11 h (liq.) 73.862 94.438 114.83 135.52 156.77 178.78 201.74 225.90 251.69 280.08 314.63 BOOKCOMP, Inc. — John Wiley & Sons / Page 95 / 2nd Proofs / Heat Transfer Handbook / Bejan 95 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 [95], (53) Lines: 1763 to 1798 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [95], (53) h (vap.) 286.44 296.19 306.91 318.39 330.28 342.18 353.63 364.09 372.80 378.21 374.56 s (liq.) 0.3405 0.4907 0.6164 0.7269 0.8269 0.9193 1.0063 1.0894 1.1705 1.2522 1.3438 s (vap.) 2.0411 1.8357 1.7140 1.6412 1.5980 1.5729 1.5586 1.5501 1.5431 1.5326 1.5036 c v (liq.) 0.5533 0.5288 0.5275 0.5370 0.5515 0.5683 0.5862 0.6050 0.6258 0.6544 0.7208 c v (vap.) 0.3009 0.3426 0.3827 0.4208 0.4578 0.4944 0.5317 0.5706 0.6126 0.6620 0.7423 c p (liq.) 0.8371 0.8152 0.8194 0.8371 0.8631 0.8961 0.9376 0.9934 1.0802 1.2618 2.1896 c p (vap.) 0.3696 0.4115 0.4250 0.4920 0.5334 0.5794 0.6344 0.7072 0.8204 1.0658 2.5120 w (liq.) 1265.2 1143.1 1026.5 915.19 808.46 705.34 604.49 504.07 400.97 289.31 158.26 w (vap.) 102.76 111.28 119.04 125.92 131.52 135.31 136.70 135.10 129.75 119.47 102.14 η (liq.) — — 965.60 612.98 431.42 320.10 243.90 187.31 142.19 103.30 63.988 η (vap.) — — 6.8573 7.8481 8.8378 9.8222 10.816 11.866 13.091 14.819 18.726 λ (liq.) — — 115.83 104.39 93.947 84.277 75.197 66.250 58.063 49.727 46.867 λ (vap.) — — 4.3416 5.3635 6.4653 7.6492 8.9383 10.411 12.293 15.258 23.499 σ 0.0343 0.0302 0.0262 0.0223 0.0185 0.0149 0.0115 0.0083 0.0053 0.0027 0.0006 R-123 (2,2-Dichloro-1,1,1-trifluoroethane, HCFC-123) T 200.00 225.00 250.00 275.00 300.00 325.00 350.00 375.00 400.00 425.00 450.00 p 0.00025 0.0020 0.0101 0.0355 0.0978 0.2248 0.4515 0.8185 1.3722 2.1672 3.2806 ρ (liq.) 1694.4 1638.4 1581.1 1521.6 1459.1 1392.7 1320.8 1240.6 1146.8 1026.4 819.52 ρ (vap.) 0.0230 0.1660 0.7469 2.4243 6.2595 13.752 26.977 49.027 85.321 148.41 296.39 h (liq.) 130.25 153.55 177.37 201.83 227.03 253.01 279.89 307.88 337.44 369.62 409.08 h (vap.) 339.57 353.25 367.66 382.55 397.63 412.60 427.11 440.74 452.74 461.52 460.11 s (liq.) 0.7034 0.8132 0.9135 1.0067 1.0942 1.1771 1.2563 1.3327 1.4078 1.4840 1.5713 s (vap.) 1.7500 1.7007 1.6747 1.6638 1.6629 1.6681 1.6769 1.6870 1.6960 1.7002 1.6847 c v (liq.) 0.6361 0.6473 0.6649 0.6855 0.7070 0.7289 0.7514 0.7749 0.8011 0.8335 0.8881 c v (vap.) 0.4770 0.5168 0.5553 0.5932 0.6309 0.6687 0.7068 0.7458 0.7872 0.8348 0.9048 c p (liq.) 0.9253 0.9408 0.9648 0.9923 1.0219 1.0545 1.0939 1.1481 1.2375 1.4385 2.9067 c p (vap.) 0.5315 0.5720 0.6123 0.6540 0.6988 0.7488 0.8078 0.8846 1.0044 1.2728 3.3587 w (liq.) 1104.3 998.61 894.26 793.34 696.37 602.81 511.47 420.73 328.57 231.85 119.97 continued BOOKCOMP, Inc. — John Wiley & Sons / Page 96 / 2nd Proofs / Heat Transfer Handbook / Bejan 96 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 [96], (54) Lines: 1798 to 1832 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [96], (54) TABLE 2.7 Thermophysical Properties of Fluids along the Saturation Line a (Continued) R-123 (2,2-Dichloro-1,1,1-trifluoroethane, HCFC-123) (Continued) w (vap.) 110.02 116.07 121.40 125.72 128.63 129.74 128.62 124.74 117.30 104.85 84.236 η (liq.) 1795.0 1124.7 768.49 551.59 408.74 309.64 238.12 184.60 142.78 107.74 71.220 η (vap.) 6.9646 7.9822 8.9646 9.9065 10.804 11.664 12.515 13.445 14.683 16.913 23.904 λ (liq.) 105.59 98.545 90.832 83.129 75.902 69.320 63.340 57.789 52.407 46.810 40.476 λ (vap.) 3.6080 5.0248 6.4350 7.8477 9.2909 10.815 12.497 14.451 16.867 20.168 26.721 σ 0.0275 0.0242 0.0211 0.0180 0.0150 0.0121 0.0093 0.0067 0.0043 0.0021 0.0003 R-124 (1-Chloro-1,2,2,2-tetrafluoroethane, HCFC-124) T 125.00 150.00 175.00 200.00 225.00 250.00 275.00 300.00 325.00 350.00 375.00 p 9.2 × 10 −8 0.000011 0.00029 0.0030 0.0166 0.0619 0.1747 0.4050 0.8136 1.4717 2.4663 ρ (liq.) 1839.6 1774.6 1709.8 1644.3 1576.9 1506.4 1431.2 1349.0 1255.7 1143.4 987.37 ρ (vap.) 0.0000 0.0012 0.0273 0.2443 1.2235 4.1891 11.131 24.975 50.266 95.626 185.30 h (liq.) 53.743 77.013 100.64 124.81 149.68 175.36 202.01 229.85 259.21 290.76 326.38 h (vap.) 278.64 290.42 303.28 317.07 331.55 346.36 361.10 375.32 388.44 399.39 405.30 s (liq.) 0.2365 0.4062 0.5518 0.6809 0.7979 0.9060 1.0073 1.1036 1.1965 1.2884 1.3840 s (vap.) 2.0357 1.8289 1.7097 1.6422 1.6063 1.5900 1.5858 1.5885 1.5942 1.5988 1.5945 c v (liq.) 0.6433 0.6426 0.6534 0.6706 0.6915 0.7147 0.7396 0.7660 0.7948 0.8293 0.8796 c v (vap.) 0.3878 0.4326 0.4759 0.5185 0.5620 0.6082 0.6582 0.7120 0.7693 0.8326 0.9134 c p (liq.) 0.9276 0.9363 0.9550 0.9798 1.0096 1.0445 1.0863 1.1391 1.2133 1.3428 1.7183 c p (vap.) 0.4488 0.4936 0.5371 0.5807 0.6273 0.6807 0.7452 0.8258 0.9360 1.1240 1.6905 w (liq.) 1271.2 1157.4 1043.8 932.36 824.09 719.17 617.30 517.54 417.74 313.56 198.17 w (vap.) 93.870 102.10 109.63 116.42 122.21 126.48 128.63 128.00 123.82 114.94 99.240 η (liq.) — — — 1045.8 634.47 432.13 311.61 230.86 171.82 125.13 84.022 η (vap.) — — 6.7326 7.7137 8.6921 9.6539 10.604 11.575 12.648 14.035 16.477 λ (liq.) — — — 102.64 92.804 83.792 75.439 67.582 60.047 52.635 45.323 λ (vap.) — — 4.9531 6.1026 7.3533 8.7039 10.165 11.778 13.665 16.178 21.002 σ 0.0330 0.0294 0.0258 0.0224 0.0190 0.0157 0.0125 0.0094 0.0065 0.0039 0.0015 BOOKCOMP, Inc. — John Wiley & Sons / Page 97 / 2nd Proofs / Heat Transfer Handbook / Bejan 97 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 [97], (55) Lines: 1832 to 1866 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [97], (55) R-125 (Pentafluoroethane, HFC-125) T 180.00 200.00 220.00 240.00 260.00 270.00 280.00 290.00 300.00 310.00 320.00 p 0.0057 0.0247 0.0787 0.2003 0.4327 0.6064 0.8279 1.1049 1.4459 1.8604 2.3597 ρ (liq.) 1666.4 1600.2 1531.5 1458.3 1378.2 1334.4 1287.4 1236.0 1178.6 1112.4 1031.7 ρ (vap.) 0.4576 1.8130 5.3578 12.946 27.244 38.100 52.361 71.093 95.933 129.69 178.02 h (liq.) 95.143 116.24 137.89 160.34 183.84 196.07 208.69 221.77 235.43 249.87 265.50 h (vap.) 281.44 292.86 304.36 315.62 326.28 331.25 335.86 339.99 343.45 345.90 346.72 s (liq.) 0.5353 0.6464 0.7494 0.8467 0.9400 0.9857 1.0310 1.0761 1.1214 1.1676 1.2157 s (vap.) 1.5703 1.5295 1.5061 1.4937 1.4879 1.4864 1.4852 1.4838 1.4815 1.4774 1.4696 c v (liq.) 0.6746 0.6963 0.7199 0.7447 0.7710 0.7850 0.7998 0.8160 0.8343 0.8564 0.8858 c v (vap.) 0.5142 0.5594 0.6103 0.6660 0.7236 0.7528 0.7824 0.8131 0.8457 0.8820 0.9255 c p (liq.) 1.0459 1.0658 1.0994 1.1445 1.2034 1.2405 1.2855 1.3433 1.4234 1.5481 1.7857 c p (vap.) 0.5857 0.6358 0.6974 0.7725 0.8635 0.9183 0.9839 1.0676 1.1845 1.3706 1.7372 w (liq.) 909.89 800.94 701.53 606.80 513.52 466.60 419.00 370.32 320.00 267.33 211.15 w (vap.) 118.55 123.47 126.98 128.59 127.77 126.27 123.91 120.57 116.10 110.29 102.86 η (liq.) 1003.1 635.17 442.77 324.15 242.88 210.77 182.60 157.44 134.54 113.17 92.452 η (vap.) 7.7601 8.6274 9.4598 10.303 11.180 11.652 12.167 12.753 13.458 14.372 15.691 λ (liq.) 116.42 105.35 95.117 85.528 76.421 71.996 67.625 63.281 58.935 54.566 50.240 λ (vap.) 6.1300 7.2865 8.5383 9.9061 11.438 12.302 13.252 14.341 15.665 17.427 20.135 σ 0.0206 0.0174 0.0144 0.0114 0.0087 0.0073 0.0060 0.0048 0.0036 0.0025 0.0015 R-13 (Chlorotrifluoromethane, CFC-13) T 100.00 120.00 140.00 160.00 180.00 200.00 220.00 240.00 260.00 280.00 300.00 p 2.7 × 10 − 6 0.00013 0.0019 0.0125 0.0518 0.1550 0.3714 0.7602 1.3878 2.3316 3.7065 ρ (liq.) 1838.1 1773.3 1706.8 1637.8 1565.5 1488.9 1406.1 1313.8 1205.2 1063.8 777.60 ρ (vap.) 0.0003 0.0139 0.1691 0.9949 3.7116 10.304 23.541 47.397 88.789 164.64 388.24 h (liq.) 39.457 55.920 72.678 89.538 106.70 124.44 143.02 162.81 184.36 208.88 244.14 h (vap.) 229.98 237.21 245.04 253.25 261.55 269.66 277.27 283.96 288.96 290.35 276.51 continued BOOKCOMP, Inc. — John Wiley & Sons / Page 98 / 2nd Proofs / Heat Transfer Handbook / Bejan 98 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 [98], (56) Lines: 1866 to 1899 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [98], (56) TABLE 2.7 Thermophysical Properties of Fluids along the Saturation Line a (Continued) R-13 (Chlorotrifluoromethane, CFC-13) (Continued) s (liq.) 0.1008 0.2508 0.3799 0.4924 0.5934 0.6864 0.7742 0.8590 0.9432 1.0309 1.1470 s (vap.) 2.0060 1.7615 1.6111 1.5156 1.4536 1.4125 1.3844 1.3638 1.3455 1.3218 1.2549 c v (liq.) 0.5665 0.5346 0.5103 0.5056 0.5167 0.5376 0.5637 0.5919 0.6210 0.6525 0.7094 c v (vap.) 0.2649 0.3004 0.3359 0.3731 0.4133 0.4561 0.5005 0.5458 0.5923 0.6439 0.7231 c p (liq.) 0.7968 0.8358 0.8393 0.8481 0.8691 0.9031 0.9526 1.0262 1.1497 1.4407 7.1130 c p (vap.) 0.3445 0.3802 0.4169 0.4577 0.5058 0.5629 0.6319 0.7219 0.8650 1.2201 8.7804 w (liq.) 1032.1 1072.1 992.15 879.99 763.71 653.03 549.57 451.26 354.31 252.29 122.38 w (vap.) 101.74 109.91 117.29 123.73 128.85 132.18 133.16 131.16 125.37 114.75 98.019 η (liq.) — — 1074.8 619.60 413.61 295.83 218.78 163.36 120.15 83.240 42.014 η (vap.) — 5.5560 6.4782 7.4051 8.3561 9.2869 10.222 11.203 12.357 14.113 20.216 λ (liq.) — — 108.32 99.067 90.580 82.644 75.047 67.555 59.925 52.204 33.975 λ (vap.) — 2.9848 3.7768 4.6577 5.6304 6.7144 7.9588 9.5027 11.666 15.535 36.022 σ 0.0302 0.0265 0.0228 0.0193 0.0159 0.0126 0.0095 0.0067 0.0041 0.0018 0.0001 R-134a (1,1,1,2-Tetrafluoroethane, HFC-134a) T 180.00 200.00 220.00 240.00 260.00 280.00 300.00 320.00 340.00 360.00 370.00 p 0.0011 0.0063 0.0244 0.0725 0.1768 0.3727 0.7028 1.2166 1.9715 3.0405 3.7278 ρ (liq.) 1564.2 1510.5 1455.2 1397.7 1337.1 1271.8 1199.7 1116.8 1015.0 870.11 740.32 ρ (vap.) 0.0770 0.3898 1.3850 3.8367 8.9052 18.228 34.193 60.715 105.73 193.58 293.90 h (liq.) 83.483 107.39 131.78 156.79 182.56 209.27 237.19 266.77 298.88 336.06 360.64 h (vap.) 340.88 353.06 365.65 378.34 390.76 402.55 413.27 422.25 428.17 427.08 417.68 s (liq.) 0.4814 0.6073 0.7235 0.8321 0.9349 1.0333 1.1287 1.2226 1.3178 1.4207 1.4857 s (vap.) 1.9114 1.8356 1.7865 1.7552 1.7357 1.7236 1.7156 1.7085 1.6981 1.6735 1.6398 c v (liq.) 0.7912 0.8016 0.8193 0.8403 0.8631 0.8877 0.9144 0.9443 0.9802 1.0390 1.1146 c v (vap.) 0.5267 0.5732 0.6204 0.6700 0.7234 0.7810 0.8426 0.9093 0.9852 1.0854 1.1690 c p (liq.) 1.1871 1.2058 1.2332 1.2669 1.3082 1.3606 1.4324 1.5426 1.7507 2.4368 5.1048 BOOKCOMP, Inc. — John Wiley & Sons / Page 99 / 2nd Proofs / Heat Transfer Handbook / Bejan 99 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 [99], (57) Lines: 1899 to 1934 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [99], (57) c p (vap.) 0.6097 0.6586 0.7109 0.7705 0.8418 0.9296 1.0438 1.2109 1.5238 2.6064 6.8622 w (liq.) 1068.3 967.61 869.85 775.00 682.14 590.17 497.89 404.00 306.37 196.05 127.23 w (vap.) 130.05 135.98 141.01 144.73 146.75 146.63 143.88 137.86 127.57 111.25 99.370 η (liq.) 1478.6 866.56 585.96 425.63 321.76 248.50 193.32 149.30 111.95 76.801 55.825 η (vap.) 6.8981 7.7531 8.5863 9.3983 10.199 11.014 11.892 12.927 14.353 17.043 20.660 λ (liq.) 139.12 127.74 117.17 107.27 97.920 88.990 80.335 71.774 63.074 54.117 52.102 λ (vap.) 3.8934 5.4978 7.1080 8.7325 10.389 12.118 14.009 16.294 19.687 27.401 40.656 σ 0.0263 0.0230 0.0197 0.0165 0.0135 0.0106 0.0078 0.0053 0.0030 0.0010 0.0002 R-14 (Tetrafluoromethane, FC-14) T 120.00 130.00 140.00 150.00 160.00 170.00 180.00 190.00 200.00 210.00 220.00 p 0.0113 0.0304 0.0697 0.1412 0.2593 0.4405 0.7030 1.0663 1.5523 2.1864 3.0022 ρ (liq.) 1731.1 1681.6 1630.3 1576.9 1520.9 1461.3 1396.8 1325.4 1243.2 1142.5 998.53 ρ (vap.) 1.0025 2.5092 5.4125 10.433 18.464 30.643 48.512 74.366 112.10 169.77 272.45 h (liq.) 188.05 196.60 205.35 214.43 223.87 233.71 244.03 254.95 266.70 279.76 295.60 h (vap.) 334.63 338.60 342.46 346.14 349.52 352.48 354.86 356.44 356.86 355.39 349.79 s (liq.) 0.2722 0.3406 0.4052 0.4675 0.5279 0.5868 0.6448 0.7023 0.7607 0.8217 0.8918 s (vap.) 1.4937 1.4328 1.3846 1.3456 1.3132 1.2855 1.2605 1.2365 1.2115 1.1819 1.1381 c v (liq.) 0.4752 0.4596 0.4713 0.4890 0.5060 0.5212 0.5352 0.5494 0.5656 0.5870 0.6217 c v (vap.) 0.3228 0.3363 0.3514 0.3685 0.3878 0.4098 0.4349 0.4641 0.4989 0.5428 0.6059 c p (liq.) 0.8547 0.8604 0.8883 0.9224 0.9598 1.0028 1.0572 1.1335 1.2558 1.5008 2.3618 c p (vap.) 0.4193 0.4354 0.4554 0.4807 0.5132 0.5561 0.6155 0.7034 0.8505 1.1593 2.3090 w (liq.) 849.39 800.48 736.34 669.70 604.18 539.97 476.19 411.57 344.50 272.56 190.63 w (vap.) 120.58 124.35 127.42 129.66 130.96 131.18 130.22 127.94 124.21 118.82 111.42 η (liq.) 580.41 438.50 343.99 276.40 225.43 185.34 152.62 124.97 100.76 78.511 55.883 η (vap.) 6.9030 7.4762 8.0467 8.6194 9.2032 9.7925 10.420 11.125 11.987 13.178 15.320 λ (liq.) 118.21 109.59 101.36 93.465 85.871 78.518 71.345 64.302 57.364 50.825 50.943 λ (vap.) 4.1155 4.6071 5.1432 5.7360 6.3544 7.0923 7.9818 9.1167 10.713 13.357 19.379 σ 0.0170 0.0150 0.0131 0.0113 0.0095 0.0077 0.0061 0.0045 0.0031 0.0017 0.0006 continued . 111 .03 114 .38 117 .08 118 .97 119 .89 119 .66 118 .07 114 .87 109.72 102.05 90.902 η (liq.) 1217.5 859.37 645.95 504.29 403.15 326.93 266.92 217.88 176.32 139.65 105.13 η (vap.) 8.3780 9.0218 9.6 611. (vap.) 116 .64 117 .29 116 .25 115 .00 113 .19 110 .75 107.63 103.71 98.885 92.999 85.834 η (liq.) 343.29 272.64 218.66 195.98 175.46 156.71 139.36 123 .11 107.63 92.535 77.218 η (vap.) 10.092 10.793 11. 506. 674.85 584.54 498.43 414.26 329.28 285.28 239.30 190.47 138.88 w (vap.) 103.84 108.30 111 .73 113 .72 113 .87 111 .69 106.57 102.61 97.474 90.861 82.340 η (liq.) 883.93 580.60 414.58 309.63 236.71