BOOKCOMP, Inc. — John Wiley & Sons / Page 70 / 2nd Proofs / Heat Transfer Handbook / Bejan 70 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 [70], (28) Lines: 914 to 949 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [70], (28) TABLE 2.7 Thermophysical Properties of Fluids along the Saturation Line a (Continued) Ammonia (R-717) T 200.00 220.00 240.00 260.00 280.00 300.00 320.00 340.00 360.00 380.00 400.00 p 0.0087 0.0338 0.1022 0.2553 0.5509 1.0617 1.8728 3.0802 4.7929 7.1402 10.305 ρ (liq.) 728.12 705.76 681.75 656.22 629.08 599.97 568.19 532.44 490.26 436.07 344.56 ρ (vap.) 0.0891 0.3188 0.8969 2.1154 4.3817 8.2507 14.510 24.395 40.187 67.368 131.09 h (liq.) 18.997 104.71 192.70 282.79 374.99 469.71 567.90 671.27 783.03 910.32 1085.0 h (vap.) 1492.9 1528.9 1561.7 1589.9 1612.3 1627.7 1634.2 1629.2 1607.8 1558.3 1431.9 s (liq.) 0.0960 0.5042 0.8866 1.2461 1.5860 1.9098 2.2221 2.5287 2.8384 3.1686 3.5949 s (vap.) 7.4653 6.9780 6.5907 6.2735 6.0051 5.7697 5.5542 5.3462 5.1294 4.8739 4.4622 c v (liq.) 2.9264 2.8894 2.8545 2.8213 2.7898 2.7624 2.7430 2.7388 2.7636 2.8531 3.1772 c v (vap.) 1.5649 1.6196 1.7054 1.8232 1.9719 2.1482 2.3490 2.5745 2.8322 3.1467 3.5984 c p (liq.) 4.2270 4.3423 4.4488 4.5477 4.6562 4.8001 5.0184 5.3846 6.0817 7.8177 22.728 c p (vap.) 2.0755 2.1599 2.2984 2.5028 2.7878 3.1767 3.7181 4.5302 5.9545 9.3949 34.924 w (liq.) 2080.2 1913.7 1766.9 1624.5 1481.0 1333.2 1177.9 1011.8 830.62 628.75 384.58 w (vap.) 357.91 373.38 386.30 396.20 402.59 404.95 402.70 395.05 380.83 357.96 318.22 η (liq.) 507.28 346.68 254.85 197.34 158.12 129.33 106.91 88.555 72.796 58.315 41.802 η (vap.) 6.9515 7.4846 8.0587 8.6558 9.2664 9.8938 10.561 11.330 12.346 14.025 18.529 λ (liq.) 803.14 733.17 665.09 600.07 538.50 480.25 424.83 371.51 319.25 266.57 216.00 λ (vap.) 19.684 20.132 20.978 22.258 24.034 26.408 29.568 33.945 40.752 54.556 113.54 σ 0.0604 0.0523 0.0447 0.0374 0.0306 0.0242 0.0183 0.0129 0.0080 0.0038 0.0005 Argon (R-740) T 90.000 100.00 110.00 115.00 120.00 125.00 130.00 135.00 140.00 145.00 150.00 p 0.1335 0.3238 0.6653 0.9098 1.2130 1.5823 2.0255 2.5509 3.1682 3.8896 4.7346 ρ (liq.) 1378.6 1313.7 1242.8 1204.2 1162.8 1117.9 1068.1 1011.5 943.71 854.28 680.43 ρ (vap.) 7.4362 16.859 33.287 45.126 60.144 79.194 103.56 135.39 178.86 244.44 394.50 h (liq.) −114.49 −103.06 −91.129 −84.874 −78.353 −71.488 −64.161 −56.177 −47.162 −36.192 −17.880 h (vap.) 44.572 47.401 48.840 48.899 48.413 47.268 45.295 42.211 37.472 29.757 11.522 BOOKCOMP, Inc. — John Wiley & Sons / Page 71 / 2nd Proofs / Heat Transfer Handbook / Bejan 71 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 [71], (29) Lines: 949 to 985 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [71], (29) s (liq.) 1.4090 1.5278 1.6390 1.6928 1.7461 1.7995 1.8538 1.9102 1.9712 2.0425 2.1589 s (vap.) 3.1763 3.0324 2.9114 2.8560 2.8025 2.7495 2.6957 2.6390 2.5757 2.4973 2.3550 c v (liq.) 0.5268 0.4976 0.4747 0.4653 0.4576 0.4520 0.4492 0.4509 0.4598 0.4893 0.7060 c v (vap.) 0.3309 0.3445 0.3633 0.3752 0.3893 0.4064 0.4275 0.4544 0.4940 0.5662 0.8218 c p (liq.) 1.1212 1.1537 1.2176 1.2663 1.3324 1.4253 1.5638 1.7903 2.2247 3.3994 23.582 c p (vap.) 0.5757 0.6269 0.7122 0.7760 0.8627 0.9857 1.1717 1.4822 2.1036 3.8959 35.468 w (liq.) 819.45 746.91 669.20 627.79 584.19 537.83 487.88 433.10 371.63 297.06 174.74 w (vap.) 172.83 178.91 183.03 184.33 185.09 185.28 184.85 183.74 181.50 176.57 157.01 η (liq.) 247.64 183.99 140.92 123.88 108.89 95.502 83.326 72.024 61.193 50.126 35.321 η (vap.) 7.3861 8.3516 9.4080 9.9908 10.628 11.341 12.166 13.165 14.466 16.416 21.305 λ (liq.) 122.07 108.87 95.888 89.504 83.208 77.005 70.891 64.854 58.883 53.102 50.932 λ (vap.) 5.7436 6.6691 7.8579 8.6048 9.5027 10.612 12.031 13.935 16.706 21.516 40.853 σ 0.0119 0.0094 0.0071 0.0060 0.0050 0.0040 0.0030 0.0021 0.0013 0.0006 0.0000 Benzene T 300.00 325.00 350.00 375.00 400.00 425.00 450.00 475.00 500.00 525.00 550.00 p 0.0138 0.0388 0.0916 0.1894 0.3528 0.6053 0.9724 1.4820 2.1651 3.0585 4.2145 ρ (liq.) 871.65 844.82 817.14 788.52 758.60 726.83 692.37 653.91 609.15 553.06 466.88 ρ (vap.) 0.4357 1.1393 2.5361 5.0014 9.0028 15.138 24.226 37.522 57.259 88.461 150.30 h (liq.) −95.464 −51.903 −6.0993 42.075 92.593 145.52 201.07 259.71 322.22 390.29 469.81 h (vap.) 336.21 362.75 390.92 420.32 450.58 481.27 511.90 541.72 569.48 592.42 600.44 s (liq.) −0.2922 −0.1529 −0.0173 0.1153 0.2451 0.3726 0.4984 0.6235 0.7495 0.8793 1.0230 s (vap.) 1.1467 1.1230 1.1170 1.1239 1.1401 1.1626 1.1891 1.2172 1.2441 1.2643 1.2605 c v (liq.) 1.1906 1.2529 1.3416 1.4289 1.5092 1.5840 1.6568 1.7314 1.8130 1.9106 2.0533 c v (vap.) 0.9505 1.0545 1.1573 1.2597 1.3626 1.4666 1.5728 1.6828 1.7999 1.9316 2.1038 c p (liq.) 1.7055 1.7839 1.8779 1.9710 2.0643 2.1640 2.2794 2.4258 2.6373 3.0331 4.7654 c p (vap.) 1.0608 1.1696 1.2807 1.3967 1.5206 1.6573 1.8161 2.0169 2.3136 2.9126 5.8688 w (liq.) 1295.7 1180.0 1060.9 947.23 839.45 735.77 633.92 531.41 425.31 311.24 179.15 w (vap.) 187.37 192.67 196.74 199.21 199.73 197.89 193.24 185.11 172.54 153.85 125.56 σ 0.0280 0.0247 0.0215 0.0185 0.0155 0.0126 0.0099 0.0072 0.0048 0.0025 0.0006 continued BOOKCOMP, Inc. — John Wiley & Sons / Page 72 / 2nd Proofs / Heat Transfer Handbook / Bejan 72 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 [72], (30) Lines: 985 to 1020 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [72], (30) TABLE 2.7 Thermophysical Properties of Fluids along the Saturation Line a (Continued) Carbon Dioxide (R-744) T 220.00 230.00 240.00 250.00 260.00 270.00 280.00 285.00 290.00 295.00 300.00 p 0.5991 0.8929 1.2825 1.7850 2.4188 3.2033 4.1607 4.7123 5.3177 5.9822 6.7131 ρ (liq.) 1166.1 1128.7 1088.9 1046.0 998.89 945.83 883.58 847.05 804.67 752.56 679.24 ρ (vap.) 15.817 23.271 33.295 46.644 64.417 88.374 121.74 143.92 171.96 209.72 268.58 h (liq.) 86.728 106.57 126.84 147.71 169.44 192.41 217.30 230.86 245.63 262.38 283.38 h (vap.) 431.64 434.60 436.49 437.04 435.92 432.56 425.94 420.80 413.75 403.64 387.08 s (liq.) 0.5517 0.6387 0.7235 0.8068 0.8895 0.9732 1.0598 1.1056 1.1544 1.2087 1.2759 s (vap.) 2.1194 2.0649 2.0137 1.9641 1.9144 1.8626 1.8050 1.7720 1.7341 1.6876 1.6215 c v (liq.) 0.9698 0.9567 0.9454 0.9364 0.9323 0.9396 0.9605 0.9748 0.9937 1.0265 1.1199 c v (vap.) 0.6389 0.6700 0.7053 0.7459 0.7943 0.8517 0.9232 0.9686 1.0260 1.1060 1.2476 c p (liq.) 1.9618 1.9970 2.0510 2.1320 2.2554 2.4534 2.8141 3.1333 3.6756 4.7939 8.6979 c p (vap.) 0.9303 1.0053 1.1033 1.2366 1.4295 1.7307 2.2769 2.7668 3.6142 5.4316 11.921 w (liq.) 951.21 879.09 806.38 731.78 652.58 565.46 471.54 422.75 371.95 315.91 245.67 w (vap.) 223.15 223.57 222.96 221.22 218.19 213.75 207.72 203.94 199.45 193.84 185.33 η (liq.) 242.01 204.23 172.96 146.74 124.40 105.02 87.731 79.548 71.409 62.936 53.107 η (vap.) 11.135 11.689 12.272 12.902 13.614 14.469 15.601 16.361 17.357 18.792 21.306 λ (liq.) 176.15 163.28 150.75 138.47 126.35 114.25 102.03 95.810 89.546 83.558 80.593 λ (vap.) 11.301 12.221 13.297 14.610 16.306 18.687 22.468 25.424 29.821 37.215 53.689 σ 0.0163 0.0139 0.0115 0.0093 0.0071 0.0051 0.0033 0.0024 0.0017 0.0010 0.0003 Carbon Monoxide T 70.000 80.000 90.000 95.000 100.00 105.00 110.00 115.00 120.00 125.00 130.00 p 0.0210 0.0836 0.2384 0.3685 0.5443 0.7741 1.0663 1.4299 1.8745 2.4112 3.0556 ρ (liq.) 840.21 798.97 754.42 730.36 704.70 677.01 646.65 612.68 573.40 525.22 455.45 ρ (vap.) 1.0232 3.6494 9.6370 14.530 21.137 29.920 41.533 56.990 78.080 108.67 161.99 h (liq.) −25.074 −3.5476 18.162 29.279 40.692 52.515 64.903 78.078 92.410 108.66 129.41 h (vap.) 205.08 213.81 220.88 223.56 225.53 226.64 226.69 225.37 222.13 215.82 202.48 BOOKCOMP, Inc. — John Wiley & Sons / Page 73 / 2nd Proofs / Heat Transfer Handbook / Bejan 73 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 [73], (31) Lines: 1020 to 1056 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [73], (31) s (liq.) −0.3301 −0.0436 0.2097 0.3280 0.4426 0.5547 0.6658 0.7778 0.8933 1.0180 1.1730 s (vap.) 2.9578 1.6734 2.4621 2.3731 2.2909 2.2130 2.1366 2.0586 1.9744 1.8752 1.7323 c v (liq.) 1.2779 1.1803 1.1075 1.0780 1.0525 1.0312 1.0147 1.0049 1.0063 1.0305 1.1232 c v (vap.) 0.7540 0.7727 0.8056 0.8280 0.8546 0.8857 0.9225 0.9673 1.0249 1.1072 1.2555 c p (liq.) 2.1606 2.1448 2.1877 2.2355 2.3068 2.4110 2.5651 2.8045 3.2168 4.1075 7.9566 c p (vap.) 1.0669 1.1157 1.2115 1.2858 1.3860 1.5243 1.7245 2.0383 2.5995 3.8853 9.7719 w (liq.) 967.52 872.05 773.63 722.64 670.00 615.20 557.54 495.94 428.49 351.29 253.47 w (vap.) 169.27 178.52 184.85 186.78 187.83 187.97 187.16 185.34 182.45 178.27 171.80 η (liq.) 255.08 178.90 139.80 125.97 114.09 103.40 93.380 83.643 73.841 63.508 51.253 η (vap.) 4.7766 5.6070 6.6165 7.2220 7.9187 8.7333 9.7056 10.903 12.453 14.661 18.685 λ (liq.) 162.95 145.12 126.19 116.48 106.76 97.193 87.895 78.967 70.419 61.995 52.280 λ (vap.) 6.8841 7.9811 9.1267 9.7277 10.359 11.039 11.803 12.730 13.986 15.999 20.331 σ 0.0119 0.0098 0.0078 0.0067 0.0057 0.0047 0.0037 0.0027 0.0018 0.0010 0.0003 Cyclohexane T 300.00 325.00 350.00 375.00 400.00 425.00 450.00 475.00 500.00 525.00 550.00 p 0.0141 0.0388 0.0900 0.1833 0.3373 0.5729 0.9133 1.3839 2.0124 2.8316 3.8928 ρ (liq.) 772.06 748.08 723.43 697.80 670.77 641.79 609.94 573.73 530.62 475.08 349.73 ρ (vap.) 0.4810 1.2313 2.6979 5.2621 9.4161 15.830 25.495 40.045 62.573 100.85 198.59 h (liq.) −107.66 −59.864 −8.3171 46.568 104.68 166.10 231.07 300.04 373.80 454.16 559.79 h (vap.) 283.43 315.78 350.42 386.93 424.83 463.47 502.44 540.44 576.11 606.53 617.68 s (liq.) −0.3290 −0.1761 −0.0236 0.1275 0.2769 0.4249 0.5722 0.7196 0.8685 1.0221 1.2136 s (vap.) 0.9747 0.9797 1.0014 1.0351 1.0772 1.1248 1.1752 1.2257 1.2731 1.3123 1.3188 c v (liq.) 1.3176 1.4866 1.6165 1.7279 1.8312 1.9316 2.0139 2.1344 2.2419 2.3598 2.5605 c v (vap.) 1.1713 1.3075 1.4443 1.5846 1.7297 1.8806 2.0381 2.2032 2.3752 2.5444 2.6403 c p (liq.) 1.8265 1.9899 2.1282 2.2570 2.3858 2.5224 2.6760 2.8629 3.1201 3.6393 11.570 c p (vap.) 1.2732 1.4148 1.5618 1.7199 1.8951 2.0972 2.3452 2.6798 3.1989 4.2107 11.408 w (liq.) 1245.3 1108.1 996.64 895.44 797.11 697.60 594.66 487.67 378.12 263.49 108.39 w (vap.) 177.99 182.88 186.30 187.76 186.80 182.91 175.58 164.25 148.10 124.78 87.229 σ 0.0244 0.0214 0.0185 0.0157 0.0130 0.0104 0.0079 0.0056 0.0034 0.0016 0.0001 continued BOOKCOMP, Inc. — John Wiley & Sons / Page 74 / 2nd Proofs / Heat Transfer Handbook / Bejan 74 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 [74], (32) Lines: 1056 to 1090 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [74], (32) TABLE 2.7 Thermophysical Properties of Fluids along the Saturation Line a (Continued) Cyclopropane T 290.00 300.00 310.00 320.00 330.00 340.00 350.00 360.00 370.00 380.00 390.00 p 0.5777 0.7615 0.9849 1.2529 1.5709 1.9441 2.3784 2.8796 3.4546 4.1114 4.8609 ρ (liq.) 631.52 616.18 600.11 583.17 565.14 545.75 524.57 500.93 473.63 440.16 393.04 ρ (vap.) 11.361 14.851 19.140 24.390 30.814 38.698 48.459 60.747 76.696 98.678 133.76 h (liq.) 240.80 263.98 287.23 311.06 335.82 361.86 389.49 419.11 451.33 487.35 530.72 h (vap.) 655.85 663.68 671.20 678.30 684.84 690.64 695.42 698.72 699.73 696.75 684.85 s (liq.) 1.1437 1.2213 1.2964 1.3705 1.4450 1.5208 1.5985 1.6791 1.7642 1.8564 1.9643 s (vap.) 2.5749 2.5537 2.5350 2.5182 2.5027 2.4878 2.4726 2.4558 2.4355 2.4074 2.3595 c v (liq.) 1.4862 1.4188 1.4010 1.4173 1.4571 1.5130 1.5800 1.6556 1.7388 1.8322 1.9471 c v (vap.) 1.1838 1.2513 1.3221 1.3961 1.4735 1.5546 1.6400 1.7305 1.8276 1.9341 2.0566 c p (liq.) 2.3257 2.3054 2.3424 2.4242 2.5449 2.7051 2.9144 3.1994 3.6306 4.4382 6.9802 c p (vap.) 1.5298 1.6387 1.7615 1.9024 2.0682 2.2705 2.5304 2.8917 3.4598 4.5706 8.1541 w (liq.) 875.75 836.04 789.18 736.55 679.48 618.85 554.99 487.71 416.20 338.70 251.34 w (vap.) 239.65 238.29 236.10 232.99 228.84 223.51 216.83 208.55 198.34 185.70 169.73 Deuterium T 20.000 22.000 24.000 26.000 28.000 30.000 32.000 34.000 36.000 37.000 38.000 p 0.0333 0.0678 0.1232 0.2055 0.3209 0.4767 0.6814 0.9432 1.2621 1.4389 1.6903 ρ (liq.) 171.96 167.25 161.96 156.41 150.64 144.33 136.77 126.83 113.42 103.75 83.193 ρ (vap.) 0.7929 1.4776 2.5031 3.9668 6.0163 8.9050 13.070 19.017 26.539 30.756 83.193 h (liq.) −22.077 −9.5250 5.3945 22.156 40.366 60.234 82.614 109.06 140.62 160.36 195.52 h (vap.) 303.50 315.14 325.69 334.40 340.44 342.68 339.65 330.70 319.19 313.41 195.52 s (liq.) −0.9991 −0.4114 0.2224 0.8721 1.5187 2.1673 2.8420 3.5829 4.4081 4.9041 5.7696 s (vap.) 15.280 14.346 13.568 12.882 12.236 11.582 10.874 10.102 9.3686 9.0408 5.7696 c v (liq.) 3.5194 4.1411 4.6767 4.9486 4.9985 4.9028 4.7342 4.5971 4.7493 5.1300 6.4594 c v (vap.) 2.4782 2.2988 2.1682 2.1164 2.1737 2.3814 2.8067 3.5034 4.3132 4.6790 6.4594 BOOKCOMP, Inc. — John Wiley & Sons / Page 75 / 2nd Proofs / Heat Transfer Handbook / Bejan 75 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 [75], (33) Lines: 1090 to 1125 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [75], (33) c p (liq.) 5.6785 6.7969 7.8537 8.5907 9.2946 10.320 12.182 15.584 21.483 40.467 75.419 c p (vap.) 4.1521 3.9417 3.8780 4.0466 4.5882 5.7989 8.3068 12.743 18.581 23.229 75.419 w (liq.) 1023.8 919.13 858.60 830.29 801.77 755.58 683.32 578.05 437.40 337.51 243.33 w (vap.) 266.64 280.24 292.49 302.87 310.72 315.32 316.51 315.63 313.14 309.68 243.33 σ 0.0038 0.0034 0.0030 0.0026 0.0021 0.0017 0.0013 0.0009 0.0005 0.0003 0.0000 Ethylene (Ethene, R-1150) T 120.00 140.00 160.00 180.00 200.00 220.00 240.00 250.00 260.00 270.00 280.00 p 0.0014 0.0118 0.0562 0.1818 0.4555 0.9566 1.7730 2.3295 3.0035 3.8125 4.7835 ρ (liq.) 634.17 608.02 580.87 552.20 521.22 486.67 446.11 422.02 393.47 356.39 290.70 ρ (vap.) 0.0385 0.2876 1.2123 3.5889 8.4936 17.452 33.066 44.970 61.542 86.795 140.70 h (liq.) −119.17 −70.809 −22.661 25.871 75.686 128.03 184.88 216.09 250.40 290.30 347.75 h (vap.) 428.29 451.32 473.00 492.31 508.13 519.07 522.74 520.39 513.45 498.32 457.49 s (liq.) −0.8307 −0.4581 −0.1372 0.1473 0.4070 0.6516 0.8911 1.0132 1.1413 1.2836 1.4814 s (vap.) 3.7314 3.2714 2.9607 2.7386 2.5692 2.4290 2.2989 2.2304 2.1530 2.0541 1.8733 c v (liq.) 1.5530 1.4655 1.3948 1.3464 1.3214 1.3196 1.3435 1.3679 1.4068 1.4839 1.7784 c v (vap.) 0.8937 0.9064 0.9335 0.9783 1.0431 1.1320 1.2540 1.3344 1.4387 1.5918 1.9809 c p (liq.) 2.4271 2.4081 2.4067 2.4413 2.5286 2.7002 3.0430 3.3629 3.9457 5.4086 19.562 c p (vap.) 1.1920 1.2125 1.2598 1.3467 1.4920 1.7382 2.2112 2.6608 3.5116 5.7658 29.260 w (liq.) 1660.4 1520.9 1376.7 1227.0 1069.9 903.49 724.39 628.10 524.13 404.99 246.68 w (vap.) 217.51 233.95 247.39 256.98 261.94 261.54 254.88 248.80 240.47 229.17 208.88 η (liq.) 427.51 277.58 200.13 153.02 120.52 95.681 74.961 65.398 55.950 46.028 33.085 η (vap.) 3.3390 4.8414 5.6998 6.4011 7.1332 8.0066 9.1616 9.9344 10.957 12.506 16.176 λ (liq.) 248.79 222.34 197.46 174.60 153.73 134.45 116.07 106.84 97.241 86.860 83.422 λ (vap.) 6.7795 7.8923 9.1146 10.360 11.862 13.943 17.142 19.563 23.219 30.451 71.723 σ 0.0250 0.0212 0.0175 0.0140 0.0106 0.0075 0.0046 0.0033 0.0021 0.0010 0.0001 Fluorine T 60.000 70.000 80.000 90.000 100.00 110.00 120.00 125.00 130.00 135.00 140.00 p 0.0015 0.0120 0.0547 0.1730 0.4275 0.8891 1.6342 2.1389 2.7475 3.4739 4.3357 continued BOOKCOMP, Inc. — John Wiley & Sons / Page 76 / 2nd Proofs / Heat Transfer Handbook / Bejan 76 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 [76], (34) Lines: 1125 to 1159 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [76], (34) TABLE 2.7 Thermophysical Properties of Fluids along the Saturation Line a (Continued) Fluorine (Continued) ρ (liq.) 1665.4 1602.3 1536.5 1466.3 1390.0 1305.2 1207.4 1150.6 1084.8 1003.7 890.17 ρ (vap.) 0.1134 0.7882 3.1953 9.2442 21.494 43.338 80.165 107.32 143.72 195.17 278.28 h (liq.) −37.242 −22.484 −7.5901 7.5700 23.208 39.593 57.183 66.712 77.048 88.724 103.17 h (vap.) 157.21 164.56 171.31 177.09 181.58 184.41 184.90 183.83 181.40 176.84 168.02 s (liq.) −0.5175 −0.2901 −0.0916 0.0860 0.2488 0.4016 0.5494 0.6237 0.7005 0.7834 0.8817 s (vap.) 2.7233 2.3819 2.1446 1.9696 1.8325 1.7182 1.6138 1.5607 1.5032 1.4361 1.3449 c v (liq.) 0.9015 0.8618 0.8352 0.8062 0.7772 0.7517 0.7329 0.7285 0.7314 0.7504 0.8149 c v (vap.) 0.5482 0.5522 0.5622 0.5793 0.6027 0.6303 0.6641 0.6868 0.7186 0.7697 0.8707 c p (liq.) 1.4654 1.4810 1.4964 1.5295 1.5855 1.6788 1.8572 2.0212 2.3048 2.8936 4.7992 c p (vap.) 0.7686 0.7787 0.8043 0.8519 0.9269 1.0440 1.2591 1.4604 1.8232 2.6291 5.5472 w (liq.) 1043.5 973.15 871.16 779.02 692.27 603.67 506.54 452.05 391.41 321.84 238.35 w (vap.) 135.46 145.85 154.65 161.52 166.12 168.12 167.26 165.81 163.76 161.03 156.46 σ 0.0208 0.0177 0.0148 0.0120 0.0093 0.0067 0.0044 0.0033 0.0022 0.0013 0.0005 Heavy Water (Deuterium oxide) T 300.00 350.00 400.00 425.00 450.00 475.00 500.00 525.00 550.00 575.00 600.00 p 0.0031 0.0388 0.2374 0.4893 0.9205 1.6075 2.6406 4.1228 6.1713 8.9205 12.530 ρ (liq.) 1104.0 1080.3 1040.2 1015.3 987.24 955.76 920.48 880.63 834.82 780.47 712.24 ρ (vap.) 0.0246 0.2690 1.4704 2.9030 5.2871 9.0422 14.735 23.177 35.632 54.331 83.999 h (liq.) −313.36 −102.51 105.78 209.99 315.22 422.31 532.19 646.06 765.72 894.20 1037.4 h (vap.) 1951.3 2032.9 2106.1 2136.7 2161.4 2178.8 2187.4 2185.2 2169.4 2134.8 2071.1 s (liq.) −0.9330 −0.2829 0.2729 0.5250 0.7646 0.9946 1.2178 1.4368 1.6550 1.8773 2.1127 s (vap.) 6.6158 5.8181 5.2737 5.0585 4.8673 4.6926 4.5282 4.3685 4.2071 4.0349 3.8356 c v (liq.) 4.2158 3.9214 3.5946 3.4528 3.3293 3.2237 3.1347 3.0614 3.0045 2.9694 2.9721 c v (vap.) 1.3169 1.3891 1.4982 1.5800 1.6917 1.8413 2.0334 2.2679 2.5414 2.8503 3.1963 c p (liq.) 4.2420 4.1850 4.1541 4.1763 4.2306 4.3211 4.4572 4.6615 4.9842 5.5435 6.7062 c p (vap.) 1.7387 1.8326 2.0042 2.1482 2.3575 2.6583 3.0848 3.6902 4.5816 6.0279 8.8990 BOOKCOMP, Inc. — John Wiley & Sons / Page 77 / 2nd Proofs / Heat Transfer Handbook / Bejan 77 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 [77], (35) Lines: 1159 to 1193 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [77], (35) w (liq.) 1394.9 1457.7 1413.3 1366.2 1306.7 1235.6 1152.3 1056.2 946.14 820.49 674.99 w (vap.) 404.89 434.21 457.95 466.94 473.39 476.73 476.36 471.63 461.90 446.35 423.35 η (liq.) 1046.6 433.25 253.36 207.17 174.50 150.33 131.71 116.77 104.18 92.820 81.477 η (vap.) 10.228 11.828 13.544 14.395 15.229 16.050 16.871 17.722 18.655 19.769 21.290 λ (liq.) 596.96 631.93 633.11 624.05 609.65 590.46 566.82 538.88 506.76 470.46 430.22 λ (vap.) 18.277 22.532 27.812 31.041 34.820 39.366 45.081 52.701 63.267 76.284 98.667 σ 0.0716 0.0632 0.0536 0.0484 0.0429 0.0372 0.0313 0.0254 0.0194 0.0136 0.0079 Helium (R-704) T 2.5000 2.7500 3.0000 3.2500 3.5000 3.7500 4.0000 4.2500 4.5000 4.7500 5.0000 p 0.0100 0.0159 0.0237 0.0339 0.0466 0.0622 0.0810 0.1032 0.1292 0.1594 0.1945 ρ (liq.) 144.96 143.37 141.35 138.91 136.06 132.75 128.90 124.35 118.81 111.65 100.83 ρ (vap.) 2.1163 3.1344 4.4284 6.0404 8.0221 10.443 13.406 17.077 21.756 28.103 38.213 h (liq.) −6.1796 −5.5295 −4.8686 −4.1185 −3.2577 −2.2773 −1.1643 0.1065 1.5856 3.3849 5.8545 h (vap.) 16.972 17.858 18.659 19.361 19.947 20.396 20.679 20.749 20.525 19.838 18.183 s (liq.) −1.6199 −1.3874 −1.1767 −0.9599 −0.7324 −0.4941 −0.2439 0.0216 0.3106 0.6427 1.0809 s (vap.) 7.6406 7.1170 6.6658 6.2645 5.8975 5.5522 5.2169 4.8785 4.5193 4.1065 3.5467 c v (liq.) 2.5212 2.0330 2.0609 2.1996 2.3317 2.4323 2.5045 2.5575 2.6013 2.6462 2.7093 c v (vap.) 3.4863 3.4759 3.4520 3.4184 3.3779 3.3325 3.2839 3.2328 3.1794 3.1221 3.0526 c p (liq.) 2.7003 2.3729 2.5978 2.9782 3.4138 3.9093 4.5230 5.3796 6.7756 9.6775 20.240 c p (vap.) 6.2582 6.4127 6.5921 6.8185 7.1215 7.5475 8.1786 9.1817 10.964 14.856 29.094 w (liq.) 216.03 216.77 214.33 209.15 202.40 194.56 185.70 175.63 164.00 150.22 132.96 w (vap.) 87.618 90.530 93.038 95.167 96.937 98.367 99.469 100.26 100.75 101.05 101.63 η (liq.) 3.7456 3.7462 3.6940 3.6113 3.5106 3.3987 3.2785 3.1500 3.0100 2.8488 2.6342 η (vap.) 0.6382 0.7164 0.7961 0.8783 0.9640 1.0544 1.1509 1.2554 1.3718 1.5075 1.6874 λ (liq.) 14.894 15.783 16.553 17.209 17.751 18.173 18.476 18.668 18.785 18.915 19.301 λ (vap.) 4.7651 5.3301 5.8927 6.4659 7.0604 7.6838 8.3555 9.1128 10.036 11.314 13.587 σ 0.0003 0.0002 0.0002 0.0002 0.0002 0.0001 0.0001 0.0001 0.0001 0.0000 0.0000 continued BOOKCOMP, Inc. — John Wiley & Sons / Page 78 / 2nd Proofs / Heat Transfer Handbook / Bejan 78 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 [78], (36) Lines: 1193 to 1227 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [78], (36) TABLE 2.7 Thermophysical Properties of Fluids along the Saturation Line a (Continued) Hydrogen (R-702) T 14.000 16.000 18.000 20.000 22.000 24.000 26.000 28.000 30.000 31.000 32.000 p 0.0079 0.0215 0.0481 0.0932 0.1631 0.2641 0.4025 0.5852 0.8199 0.9596 1.1168 ρ (liq.) 76.867 75.116 73.220 71.110 68.727 65.997 62.801 58.916 53.838 50.432 45.636 ρ (vap.) 0.1391 0.3380 0.6880 1.2429 2.0666 3.2435 4.9001 7.2581 10.814 13.459 17.503 h (liq.) −51.323 −36.642 −20.891 −2.7322 18.221 42.350 70.318 103.40 144.51 170.44 204.55 h (vap.) 397.84 415.41 430.92 443.88 453.66 459.49 460.25 454.04 436.68 420.39 392.55 s (liq.) −2.9267 −1.9580 −1.0526 −0.1300 0.8199 1.8035 2.8358 3.9492 5.2217 5.9839 6.9620 s (vap.) 29.156 26.296 24.048 22.201 20.613 19.184 17.833 16.472 14.961 14.047 12.837 c v (liq.) 5.4352 4.7859 5.1897 5.6168 5.9417 6.1793 6.3692 6.5599 6.8276 7.0430 7.4038 c v (vap.) 6.5127 6.4022 6.4898 6.5876 6.7038 6.8464 7.0274 7.2696 7.6185 7.8644 8.2019 c p (liq.) 7.7121 7.2964 8.2552 9.4843 10.881 12.575 14.893 18.656 26.883 37.140 70.365 c p (vap.) 10.885 11.012 11.469 12.128 13.096 14.572 16.982 21.456 32.270 46.373 92.295 w (liq.) 1359.6 1271.6 1185.5 1110.7 1038.2 960.99 874.29 773.58 652.73 581.16 497.24 w (vap.) 305.17 325.05 340.22 352.59 362.25 369.34 373.96 376.19 375.97 374.91 373.31 η (liq.) 25.310 19.784 16.182 13.607 11.641 10.057 8.7151 7.5160 6.3620 5.7518 5.0391 η (vap.) 0.6670 0.8106 0.9355 1.0569 1.1819 1.3151 1.4619 1.6331 1.8628 2.0375 2.3378 λ (liq.) 76.650 90.079 98.405 103.01 104.87 104.60 102.53 98.654 92.547 88.221 82.176 λ (vap.) 10.431 12.681 14.669 16.716 18.956 21.493 24.477 28.202 33.407 37.226 43.200 σ 0.0030 0.0027 0.0023 0.0020 0.0017 0.0014 0.0011 0.0007 0.0004 0.0003 0.0002 Hydrogen Sulfide T 200.00 220.00 240.00 260.00 280.00 300.00 320.00 330.00 340.00 350.00 360.00 p 0.0504 0.1436 0.3374 0.6870 1.2555 2.1116 3.3296 4.1000 4.9939 6.0257 7.2129 ρ (liq.) 971.76 936.62 899.77 860.53 817.99 770.74 716.26 684.82 648.98 606.07 549.45 ρ (vap.) 1.0479 2.7604 6.1003 11.898 21.243 35.712 57.989 73.601 93.816 121.19 161.67 h (liq.) −25.538 14.221 54.188 94.816 136.65 180.44 227.37 252.68 279.89 310.11 346.08 h (vap.) 534.46 551.02 565.59 577.58 586.27 590.63 588.92 584.82 577.57 565.71 545.98 BOOKCOMP, Inc. — John Wiley & Sons / Page 79 / 2nd Proofs / Heat Transfer Handbook / Bejan 79 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 [79], (37) Lines: 1227 to 1261 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [79], (37) s (liq.) −0.1235 0.0655 0.2385 0.3994 0.5519 0.6992 0.8453 0.9198 0.9970 1.0798 1.1753 s (vap.) 2.6765 2.5055 2.3693 2.2562 2.1577 2.0665 1.9752 1.9263 1.8725 1.8101 1.7306 c v (liq.) 1.2344 1.1873 1.1483 1.1162 1.0900 1.0697 1.0561 1.0529 1.0534 1.0604 1.0806 c v (vap.) 0.7538 0.7721 0.7962 0.8254 0.8595 0.8990 0.9453 0.9720 1.0021 1.0369 1.0794 c p (liq.) 1.9878 1.9854 2.0037 2.0468 2.1242 2.2577 2.5040 2.7174 3.0656 3.7338 5.5180 c p (vap.) 1.0162 1.0547 1.1118 1.1936 1.3123 1.4961 1.8187 2.0937 2.5378 3.3708 5.4584 w (liq.) 1386.6 1280.4 1173.3 1064.3 951.91 834.38 708.55 640.77 568.10 488.44 398.78 w (vap.) 252.66 262.30 269.67 274.46 276.40 275.21 270.62 267.00 262.49 257.21 251.56 η (liq.) 386.41 311.85 252.16 204.45 165.98 134.42 107.82 95.796 84.274 72.846 60.710 η (vap.) 8.5566 9.4845 10.455 11.485 12.606 13.873 15.397 16.328 17.454 18.919 21.089 λ (liq.) 241.07 219.71 199.10 179.34 160.41 142.13 124.18 115.11 105.74 95.684 84.012 λ (vap.) 11.438 12.822 14.334 16.022 17.954 20.231 23.039 24.759 26.822 29.451 33.217 Krypton T 120.00 130.00 140.00 150.00 160.00 170.00 180.00 185.00 190.00 195.00 200.00 p 0.1031 0.2108 0.3873 0.6547 1.0363 1.5562 2.2396 2.6512 3.1145 3.6339 4.2148 ρ (liq.) 2411.5 2334.5 2253.2 2166.2 2071.6 1966.5 1846.2 1777.8 1701.2 1613.0 1505.6 ρ (vap.) 8.9533 17.276 30.370 49.827 77.728 117.09 172.91 209.69 255.02 312.65 390.21 h (liq.) 0.1163 5.4315 10.873 16.509 22.422 28.727 35.606 39.354 43.396 47.852 52.975 h (vap.) 107.33 108.90 110.09 110.79 110.91 110.28 108.66 107.33 105.53 103.08 99.598 s (liq.) 0.0010 0.0431 0.0829 0.1209 0.1579 0.1946 0.2318 0.2511 0.2712 0.2928 0.3168 s (vap.) 0.8944 0.8391 0.7915 0.7495 0.7110 0.6743 0.6377 0.6185 0.5983 0.5760 0.5499 c v (liq.) 0.2555 0.2454 0.2369 0.2299 0.2242 0.2202 0.2187 0.2194 0.2218 0.2271 0.2375 c v (vap.) 0.1607 0.1673 0.1755 0.1853 0.1965 0.2095 0.2252 0.2347 0.2459 0.2598 0.2783 c p (1iq.) 0.5251 0.5335 0.5481 0.5706 0.6044 0.6566 0.7439 0.8130 0.9158 1.0866 1.4338 c p (vap.) 0.2753 0.2928 0.3172 0.3510 0.3988 0.4707 0.5913 0.6890 0.8377 1.0909 1.6167 w (liq.) 685.71 643.02 598.86 552.79 504.18 452.07 394.88 363.54 329.61 292.16 249.52 w (vap.) 138.00 141.81 144.75 146.78 147.90 148.07 147.23 146.39 145.21 143.62 141.42 continued . 1.6215 c v (liq.) 0 .96 98 0 .95 67 0 .94 54 0 .93 64 0 .93 23 0 .93 96 0 .96 05 0 .97 48 0 .99 37 1.0265 1.1 199 c v (vap.) 0.63 89 0.6700 0.7053 0.74 59 0. 794 3 0.8517 0 .92 32 0 .96 86 1.0260 1.1060 1.2476 c p (liq.) 1 .96 18 1 .99 70. (liq.) 162 .95 145.12 126. 19 116.48 106.76 97 . 193 87. 895 78 .96 7 70.4 19 61 .99 5 52.280 λ (vap.) 6.8841 7 .98 11 9. 1267 9. 7277 10.3 59 11.0 39 11.803 12.730 13 .98 6 15 .99 9 20.331 σ 0.01 19 0.0 098 0.0078. 3.3 296 4.1000 4 .99 39 6.0257 7.21 29 ρ (liq.) 97 1.76 93 6.62 899 .77 860.53 817 .99 770.74 716.26 684.82 648 .98 606.07 5 49. 45 ρ (vap.) 1.04 79 2.7604 6.1003 11. 898 21.243 35.712 57 .98 9 73.601 93 .816