Heat Transfer Handbook part 8 pptx

BOOKCOMP, Inc. — John Wiley & Sons / Page 60 / 2nd Proofs / Heat Transfer Handbook / Bejan 60 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 [60], (18) Lines: 566 to 604 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [60], (18) TABLE 2.6 Dilute Gas Viscosity (µPa · s) 100 K 150 K 200 K 250 K 300 K 350 K 400 K 450 K 500 K 550 K 600 K Methane 3.9829 5.9087 7.7900 9.5673 11.233 12.795 14.264 15.652 16.969 18.225 19.426 Ethane 3.3157 4.8014 6.3522 7.8926 9.3864 10.820 12.192 13.504 14.759 15.963 17.118 Propane 2.9792 4.2268 5.5379 6.8715 8.2038 9.5190 10.807 12.060 13.273 14.443 15.568 Butane — 3.7091 4.9832 6.2381 7.4730 8.6883 9.8849 11.064 12.226 13.371 14.502 Isobutane — 3.7994 5.0857 6.3403 7.5639 8.7583 9.9253 11.067 12.184 13.279 14.353 Pentane — 3.4241 4.5472 5.7121 6.8932 8.0678 9.2197 10.339 11.421 12.465 13.472 Isopentane — 3.9857 4.8092 6.0426 7.2928 8.5359 9.7548 10.939 12.084 13.189 14.254 Hexane — — 4.3039 5.4420 6.5526 7.6788 8.8014 9.9075 10.989 12.041 13.063 Heptane — — 3.5540 4.9393 5.9304 6.9437 7.9569 8.9564 9.9342 10.886 11.810 Ammonia — — 6.9639 8.4513 10.188 12.052 13.977 15.922 17.862 19.783 21.678 Argon 8.1386 12.179 15.922 19.402 22.656 25.718 28.612 31.363 33.987 36.499 38.913 Carbon dioxide — — — 12.556 15.014 17.395 19.690 21.896 24.013 26.044 27.995 Carbon monoxide 6.8135 10.031 12.857 15.385 17.696 19.836 21.836 23.720 25.507 27.212 28.847 Ethylene — 5.3064 7.0041 8.6638 10.361 12.008 13.575 15.061 16.478 17.838 19.149 Heavy water ————10.235 11.879 13.740 15.724 17.780 19.876 21.991 Helium 9.7650 12.491 15.135 17.597 19.926 22.151 24.290 26.356 28.361 30.311 32.213 Hydrogen (normal) 4.1824 5.5558 6.7762 7.8996 8.9507 9.9440 10.890 11.797 12.670 13.516 14.337 Hydrogen sulfide — — 8.4917 10.686 12.882 15.035 17.121 19.129 21.056 22.905 24.685 Krypton — 12.825 17.186 21.346 25.238 28.875 32.291 35.532 38.598 41.538 44.361 Neon 14.568 19.609 23.897 27.718 31.235 34.532 37.662 40.654 43.530 46.307 48.996 Nitrogen 6.9167 10.063 12.900 15.490 17.882 20.111 22.205 24.185 26.069 27.868 29.594 Oxygen 7.6302 11.275 14.609 17.682 20.539 23.214 25.735 28.124 30.399 32.575 34.663 Parahydrogen 4.1824 5.5558 6.7762 7.8996 8.9507 9.9440 10.890 11.797 12.670 13.516 14.337 Water ————9.9262 11.531 13.347 15.285 17.294 19.345 21.416 Xenon — — 15.942 19.472 23.021 26.536 29.984 33.346 36.615 39.787 42.864 R-11 — — — 8.5895 10.366 12.144 13.899 15.613 17.277 18.887 20.444 R-113 — — — 8.0710 9.7388 11.413 13.070 14.694 16.275 17.807 19.290 BOOKCOMP, Inc. — John Wiley & Sons / Page 61 / 2nd Proofs / Heat Transfer Handbook / Bejan 61 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 [61], (19) Lines: 604 to 635 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [61], (19) R-114 — — — — 10.967 12.823 14.633 16.384 18.072 19.696 21.259 R-115 — — 8.3439 10.501 12.633 14.700 16.684 18.581 20.394 22.131 23.800 R-116 — — 9.4781 11.889 14.212 16.420 18.510 20.493 22.382 24.188 R-12 — — 7.8613 9.8945 11.925 13.914 15.838 17.688 19.463 21.166 22.803 R-123 — — 6.9649 8.9742 10.863 12.632 14.281 15.810 17.219 18.507 19.675 R-124 — — 7.7230 9.7203 11.697 13.617 15.461 17.225 18.912 20.529 22.082 R-125 — — 8.6666 10.903 13.102 15.223 17.252 19.188 21.035 22.805 24.504 R-13 — 6.9581 9.3573 11.747 14.059 16.264 18.355 20.340 22.231 24.040 25.777 R-134a — — 7.7659 9.8718 11.893 13.830 15.686 17.468 19.181 20.831 22.423 R-14 — 8.7213 11.679 14.491 17.118 19.570 21.873 24.051 R-141b — — — 7.7183 9.3140 10.914 12.495 14.042 15.547 17.004 18.414 R-142b — — 6.6993 8.4275 10.166 11.881 13.550 15.163 16.714 18.206 19.643 R-143a — — 7.3820 9.2892 11.169 12.987 14.729 16.392 17.982 19.504 20.965 R-152a — — 6.7055 8.4826 10.367 12.174 13.909 15.577 17.182 18.731 20.288 R-22 — — 8.4013 10.575 12.735 14.840 16.868 18.813 20.674 22.459 24.174 R-227ea — — — 9.6938 11.678 13.615 15.484 17.277 18.996 20.644 22.228 R-23 — 7.1874 9.9500 12.554 15.012 17.329 19.533 21.634 23.645 25.576 27.436 R-236ea — — — 9.1613 11.052 12.918 14.735 16.491 18.181 19.807 21.372 R-236fa — — 7.3159 9.2059 11.101 12.964 14.772 16.515 18.189 19.797 21.345 R-245ca — — — 8.5345 10.301 12.059 13.785 15.464 17.089 18.657 20.170 R-245fa — — — 8.6749 10.468 12.245 13.981 15.663 17.286 18.849 20.355 R-32 — — 8.3720 10.538 12.695 14.801 16.834 18.784 20.653 22.446 24.169 R-41 — — 7.3138 9.1921 11.022 12.775 14.443 16.030 17.543 18.991 20.381 RC318 — — — 9.6361 11.616 13.556 15.435 17.242 18.977 20.641 22.243 BOOKCOMP, Inc. — John Wiley & Sons / Page 62 / 2nd Proofs / Heat Transfer Handbook / Bejan 62 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 [62], (20) Lines: 635 to 672 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [62], (20) TABLE 2.7 Thermophysical Properties of Fluids along the Saturation Line a Methane (R-50) T 100.00 110.00 120.00 130.00 140.00 150.00 160.00 170.00 180.00 185.00 190.00 p 0.0344 0.0881 0.1914 0.3673 0.6412 1.0400 1.5921 2.3283 3.2852 3.8617 4.5186 ρ (liq.) 438.89 424.78 409.90 394.04 376.87 357.90 336.31 310.50 276.23 251.36 200.78 ρ (vap.) 0.6746 1.5982 3.2619 5.9804 10.152 16.328 25.382 38.974 61.375 80.435 125.18 h (liq.) −40.269 −5.8134 29.405 65.628 103.20 142.64 184.80 231.24 285.94 320.51 378.27 h (vap.) 490.21 508.02 524.02 537.66 548.34 555.23 557.07 551.54 532.83 512.49 459.03 s (liq.) −0.3793 −0.0522 0.2521 0.5385 0.8116 1.0761 1.3378 1.6054 1.8991 2.0765 2.3687 s (vap.) 4.9255 4.6191 4.3738 4.1695 3.9912 3.8267 3.6645 3.4895 3.2707 3.1142 2.7937 c v (liq.) 2.1136 2.0642 2.0196 1.9795 1.9452 1.9186 1.9037 1.9095 1.9669 2.0623 2.6022 c v (vap.) 1.5887 1.6108 1.6390 1.6739 1.7172 1.7727 1.8473 1.9556 2.1404 2.3118 2.8546 c p (liq.) 3.4084 3.4692 3.5493 3.6580 3.8129 4.0474 4.4354 5.1872 7.2923 11.109 94.012 c p (vap.) 2.1458 2.2053 2.2930 2.4208 2.6108 2.9083 3.4189 4.4585 7.5740 13.527 140.81 w (liq.) 1452.0 1354.7 1253.5 1148.1 1037.7 920.85 795.43 657.52 497.01 398.59 250.31 w (vap.) 260.09 270.01 277.76 283.13 285.93 285.97 283.01 276.66 266.04 258.03 238.55 η (liq.) 155.78 121.34 97.432 79.868 66.333 55.437 46.266 38.115 30.193 25.773 18.982 η (vap.) 3.9976 4.3964 4.1823 5.2517 5.7254 6.2526 6.8688 7.6515 8.8251 9.8238 12.455 λ (liq.) 199.67 186.18 172.15 157.91 143.65 129.43 115.19 100.73 85.799 78.733 96.970 λ (vap.) 10.015 11.350 12.811 14.449 16.334 18.581 21.423 25.477 33.392 43.706 119.40 σ 0.0163 0.0137 0.0113 0.0091 0.0071 0.0052 0.0035 0.0021 0.0009 0.0004 0.0000 Ethane (R-170) T 100.00 120.00 140.00 160.00 180.00 200.00 220.00 240.00 260.00 280.00 300.00 p 0.000011 0.00035 0.0038 0.0215 0.0787 0.2174 0.4923 0.9673 1.7125 2.8076 4.3565 ρ (liq.) 641.24 619.31 596.90 573.82 549.66 523.96 496.10 465.08 429.02 383.15 303.22 ρ (vap.) 0.0004 0.0107 0.0991 0.4893 1.6257 4.1746 9.0367 17.492 31.703 56.583 114.50 h (liq.) −199.04 −152.04 −105.35 −58.612 −11.027 38.151 89.685 144.53 204.23 272.18 363.80 h (vap.) 386.60 410.88 435.96 460.84 484.38 505.82 524.45 539.23 548.17 546.52 512.98 BOOKCOMP, Inc. — John Wiley & Sons / Page 63 / 2nd Proofs / Heat Transfer Handbook / Bejan 63 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 [63], (21) Lines: 672 to 707 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [63], (21) s (liq.) −1.4399 −1.0115 −0.6516 −0.3398 −0.0603 0.1974 0.4403 0.6745 0.9066 1.1481 1.4478 s (vap.) 4.4165 3.6795 3.2149 2.9067 2.6920 2.5357 2.4165 2.3190 2.2294 2.1279 1.9451 c v (liq.) 1.6012 1.5345 1.4647 1.4282 1.4184 1.4281 1.4536 1.4941 1.5513 1.6356 1.8781 c v (vap.) 0.9080 0.9168 0.8995 0.9217 1.0065 1.1280 1.2633 1.4047 1.5560 1.7365 2.0507 c p (liq.) 2.3318 2.3453 2.3284 2.3497 2.4082 2.5019 2.6377 2.8398 3.1805 3.9711 9.9832 c p (vap.) 1.1840 1.1875 1.1618 1.1888 1.3017 1.4791 1.7090 2.0151 2.4986 3.6068 12.744 w (liq.) 1938.3 1795.5 1647.8 1498.5 1347.7 1194.8 1039.0 878.23 708.85 520.93 276.76 w (vap.) 189.89 207.39 223.45 236.89 246.81 252.96 254.94 252.03 243.27 227.16 200.47 η (liq.) 877.99 488.15 320.91 231.74 176.39 138.23 109.90 87.650 69.273 52.962 34.918 η (vap.) 3.3157 3.8961 4.4956 5.1100 5.7388 6.3908 7.0891 7.8826 8.8799 10.381 14.023 λ (liq.) 248.15 230.30 210.90 191.08 171.51 152.56 134.47 117.37 101.18 85.534 71.371 λ (vap.) 3.4562 4.6535 5.9584 7.4110 9.0663 10.997 13.305 16.179 20.060 26.418 46.929 σ 0.0300 0.0267 0.0233 0.0200 0.0168 0.0136 0.0105 0.0076 0.0048 0.0023 0.0003 Propane (R-290) T 100.00 125.00 150.00 175.00 200.00 225.00 250.00 275.00 300.00 325.00 350.00 p 2.5 ×10 −8 7.5 × 10 −6 0.00028 0.0034 0.0201 0.0769 0.2179 0.5020 0.9980 1.7832 2.9510 ρ (liq.) 718.54 693.01 667.73 642.23 615.98 588.40 558.78 526.17 489.14 444.89 384.02 ρ (vap.) 0.0000 0.0003 0.0100 0.1026 0.5404 1.8711 4.9424 10.941 21.658 40.480 77.052 h (liq.) −168.39 −119.73 −70.291 −19.808 32.227 86.460 143.65 204.67 270.61 343.27 427.71 h (vap.) 379.56 404.10 430.71 459.04 488.58 518.59 548.27 576.71 602.56 623.16 630.91 s (liq.) −1.0920 −0.6577 −0.2973 0.0138 0.2915 0.5465 0.7863 1.0168 1.2428 1.4699 1.7116 s (vap.) 4.3876 3.5329 3.0427 2.7501 2.5733 2.4670 2.4048 2.3697 2.3493 2.3311 2.2921 c v (liq.) 1.3436 1.3339 1.3391 1.3582 1.3926 1.4423 1.5065 1.5839 1.6738 1.7794 1.9248 c v (vap.) 0.7480 0.8366 0.9184 1.0016 1.0946 1.2040 1.3313 1.4736 1.6281 1.7975 2.0004 c p (liq.) 1.9310 1.9613 1.9956 2.0461 2.1194 2.2196 2.3515 2.5233 2.7572 3.1371 4.2091 c p (vap.) 0.9365 1.0252 1.1075 1.1933 1.2950 1.4244 1.5908 1.8048 2.0984 2.5937 4.0530 w (liq.) 2026.4 1857.6 1684.4 1515.0 1349.7 1187.5 1027.5 868.89 710.10 544.17 350.19 w (vap.) 153.65 169.94 184.59 197.65 208.68 216.87 221.28 220.90 214.52 200.36 175.23 continued BOOKCOMP, Inc. — John Wiley & Sons / Page 64 / 2nd Proofs / Heat Transfer Handbook / Bejan 64 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 [64], (22) Lines: 707 to 742 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [64], (22) TABLE 2.7 Thermophysical Properties of Fluids along the Saturation Line a (Continued) Propane (R-290) (Continued) η (liq.) 3821.5 1269.7 655.97 415.28 289.68 212.58 160.60 123.31 95.085 72.351 51.632 η (vap.) 2.9792 3.5913 4.2258 4.8708 5.5148 6.1540 6.8026 7.5026 8.3405 9.5083 11.634 λ (liq.) 203.49 192.17 178.46 163.55 148.25 133.13 118.62 105.08 92.755 81.720 71.502 λ (vap.) 2.4171 3.7887 5.3418 7.0722 8.9711 11.040 13.323 15.957 19.248 23.915 32.636 σ 0.0354 0.0315 0.0277 0.0239 0.0203 0.0167 0.0132 0.0099 0.0068 0.0039 0.0014 Butane (R-600) T 150.00 200.00 225.00 250.00 275.00 300.00 325.00 350.00 375.00 400.00 425.00 p 8.8 × 10 −6 0.0020 0.0106 0.0393 0.1109 0.2580 0.5206 0.9447 1.5821 2.4950 3.7828 ρ (liq.) 720.91 673.73 649.75 624.93 598.78 570.67 539.76 504.77 463.27 408.14 256.91 ρ (vap.) 0.0004 0.0687 0.3336 1.1234 2.9507 6.5301 12.847 23.402 40.982 72.839 201.07 h (liq.) −58.828 41.883 93.960 147.89 204.27 263.73 326.94 394.69 468.29 551.10 680.26 h (vap.) 422.68 484.26 517.46 551.89 587.15 622.77 685.13 692.20 722.98 745.40 709.19 s (liq.) −0.2501 0.3289 0.5741 0.8011 1.1055 1.2215 1.4223 1.6206 1.8200 2.0282 2.3307 s (vap.) 2.9600 2.5407 2.4563 2.4171 2.4078 2.4183 2.4414 2.4707 2.4992 2.5140 2.3988 c v (liq.) 1.4290 1.4718 1.5135 1.5709 1.6422 1.7248 1.8161 1.9147 2.0215 2.1482 2.4543 c v (vap.) 1.0149 1.1748 1.2650 1.3681 1.4849 1.6133 1.7508 1.8955 2.0485 2.2178 2.4822 c p (liq.) 1.9824 2.0537 2.1155 2.2004 2.3092 2.4435 2.6082 2.8194 3.1351 3.8592 211.56 c p (vap.) 1.1580 1.3198 1.4147 1.5282 1.6644 1.8266 2.0227 2.2764 2.6684 3.6114 242.27 w (liq.) 1719.0 1430.6 1290.7 1153.3 1018.2 884.92 752.87 620.83 483.83 328.58 119.17 w (vap.) 156.47 178.85 188.13 195.52 200.40 202.11 199.83 192.54 178.61 154.97 113.84 η (liq.) 1370.6 494.94 349.26 259.20 198.78 155.62 123.09 97.300 75.697 55.863 27.110 η (vap.) 3.7090 4.9792 5.5998 6.2086 6.8131 7.4364 8.1245 8.9613 10.110 12.016 21.260 λ (liq.) 171.21 149.19 137.42 125.77 114.53 103.94 94.180 85.386 77.581 70.526 118.63 λ (vap.) 5.5793 8.4973 10.250 12.197 14.357 16.785 19.604 23.061 27.664 34.993 123.39 σ 0.0313 0.0243 0.0210 0.0177 0.0146 0.0116 0.0088 0.0061 0.0037 0.0015 0.0000 BOOKCOMP, Inc. — John Wiley & Sons / Page 65 / 2nd Proofs / Heat Transfer Handbook / Bejan 65 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 [65], (23) Lines: 742 to 776 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [65], (23) Isobutane (2-Methylpropane, R-600a) T 150.00 175.00 200.00 225.00 250.00 275.00 300.00 325.00 350.00 375.00 400.00 p 0.000023 0.00045 0.0038 0.0185 0.0631 0.1672 0.3698 0.7162 1.2577 2.0551 3.1920 ρ (liq.) 706.14 682.48 658.25 633.09 606.61 578.29 547.48 513.31 474.24 425.57 340.74 ρ (vap.) 0.0011 0.0179 0.1318 0.5807 1.8175 4.5187 9.6081 18.417 33.238 59.391 119.80 h (liq.) −49.648 −3.4665 44.680 95.083 148.13 204.27 264.00 327.86 396.67 472.64 566.69 h (vap.) 404.10 431.22 460.56 491.72 524.22 557.51 591.00 623.83 654.41 679.12 683.39 s (liq.) −0.1998 0.0848 0.3419 0.5791 0.8023 1.0155 1.2220 1.4243 1.6250 1.8296 2.0643 s (vap.) 2.8252 2.5688 2.4212 2.3419 2.3066 2.3000 2.3121 2.3350 2.3614 2.3802 2.3561 c v (liq.) 1.3103 1.3524 1.4019 1.4620 1.5336 1.6160 1.7077 1.8073 1.9144 2.0356 2.2388 c v (vap.) 0.8943 0.9947 1.0959 1.2040 1.3230 1.4541 1.5954 1.7446 1.9021 2.0749 2.3041 c p (liq.) 1.8104 1.8850 1.9684 2.0652 2.1781 2.3095 2.4623 2.6446 2.8911 3.3822 6.5400 c p (vap.) 1.0374 1.1383 1.2419 1.3564 1.4894 1.6466 1.8340 2.0676 2.4005 3.0674 7.3172 w (liq.) 1612.0 1470.8 1332.1 1195.1 1059.3 924.64 791.59 660.70 528.31 378.18 183.42 w (vap.) 157.76 169.14 179.38 188.05 194.51 198.00 197.70 192.61 181.32 161.42 128.34 η (liq.) 1751.4 903.05 551.15 369.87 262.91 194.15 147.22 113.53 87.888 66.264 42.436 η (vap.) 3.7993 4.4453 5.0797 5.6991 6.3047 6.9095 7.5457 8.2773 9.2413 10.815 14.857 λ (liq.) 148.49 139.48 129.36 118.75 108.11 97.862 88.323 79.776 72.402 66.126 62.048 λ (vap.) 4.4606 6.1666 8.0276 10.032 12.174 14.477 17.026 20.030 23.954 30.110 46.264 σ 0.0285 0.0253 0.0221 0.0189 0.0158 0.0128 0.0099 0.0071 0.0045 0.0022 0.0003 Pentane T 150.00 200.00 250.00 275.00 300.00 325.00 350.00 375.00 400.00 425.00 450.00 p 2.7 × 10 −7 0.0002 0.0076 0.0266 0.0732 0.1685 0.3396 0.6177 1.0384 1.6429 2.4836 ρ (liq.) 756.28 711.19 666.32 643.13 618.95 593.35 565.69 535.02 499.73 456.47 395.85 ρ (vap.) 0.0000 0.0086 0.2651 0.8533 2.1937 4.8038 9.3842 16.939 29.117 49.281 87.430 h (liq.) −334.92 −235.81 −132.70 −78.400 −21.633 38.051 101.10 168.03 239.58 317.05 404.03 h (vap.) 139.41 199.97 268.35 305.08 343.22 382.47 422.37 462.26 500.99 536.24 561.62 continued BOOKCOMP, Inc. — John Wiley & Sons / Page 66 / 2nd Proofs / Heat Transfer Handbook / Bejan 66 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 [66], (24) Lines: 776 to 812 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [66], (24) TABLE 2.7 Thermophysical Properties of Fluids along the Saturation Line a (Continued) Pentane (Continued) s (liq.) −1.5046 −0.9346 −0.4749 −0.2681 −0.0709 0.1197 0.3056 0.4889 0.6714 0.8561 1.0503 s (vap.) 1.6576 1.2443 1.1292 1.1264 1.1453 1.1794 1.2235 1.2735 1.3249 1.3719 1.4005 c v (liq.) 1.4426 1.4869 1.5862 1.6572 1.7397 1.8310 1.9284 2.0303 2.1363 2.2488 2.3821 c v (vap.) 1.0061 1.1817 1.3597 1.4629 1.5763 1.6983 1.8272 1.9619 2.1029 2.2543 2.4328 c p (liq.) 1.9682 2.0091 2.1283 2.2171 2.3239 2.4480 2.5916 2.7620 2.9808 3.3177 4.1782 c p (vap.) 1.1214 1.2972 1.4793 1.5889 1.7141 1.8562 2.0189 2.2132 2.4707 2.9032 4.2191 w (liq.) 1788.3 1500.5 1244.1 1122.1 1002.5 884.21 765.87 645.89 522.16 391.45 246.17 w (vap.) 138.80 159.00 175.83 182.32 186.93 189.09 188.17 183.35 173.48 156.77 130.14 η (liq.) 2750.8 689.40 344.14 267.51 214.42 174.84 143.56 117.61 95.070 74.436 53.842 η (vap.) 3.4236 4.5515 5.7318 6.3409 6.9672 7.6198 8.3158 9.0883 10.004 11.222 13.312 λ (liq.) 172.92 152.50 130.68 120.37 110.64 101.54 93.033 85.073 77.560 70.311 62.809 λ (vap.) 4.3338 6.9615 10.207 12.164 14.393 16.928 19.811 23.099 26.897 31.431 37.367 σ 0.0323 0.0265 0.0208 0.0180 0.0153 0.0126 0.0100 0.0075 0.0051 0.0030 0.0011 Isopentane (2-Methylbutane) T 260.00 280.00 300.00 320.00 340.00 360.00 380.00 400.00 420.00 440.00 460.00 p 0.0189 0.0461 0.0980 0.1872 0.3284 0.5382 0.8347 1.2377 1.7700 2.4600 3.3570 ρ (liq.) 652.36 633.24 613.33 592.35 569.95 545.63 518.63 487.67 450.35 400.63 287.45 ρ (vap.) 0.6394 1.4647 2.9606 5.4417 9.3072 15.089 23.563 36.004 54.920 86.923 190.32 h (liq.) −89.675 −46.927 −2.2196 44.614 93.760 145.45 199.99 257.89 320.05 388.70 482.73 h (vap.) 283.21 312.03 341.94 372.68 403.97 435.42 466.50 496.36 523.38 543.59 525.56 s (liq.) −0.3195 −0.1613 −0.0074 0.1432 0.2914 0.4380 0.5840 0.7304 0.8792 1.0350 1.2378 s (vap.) 1.1147 1.1207 1.1398 1.1685 1.2038 1.2435 1.2853 1.3265 1.3633 1.3870 1.3309 c v (liq.) 1.5651 1.6409 1.7196 1.8006 1.8832 1.9673 2.0530 2.1412 2.2348 2.3440 2.5665 c v (vap.) 1.3572 1.4595 1.5639 1.6702 1.7785 1.8887 2.0017 2.1188 2.2439 2.3883 2.6252 c p (liq.) 2.0902 2.1834 2.2843 2.3939 2.5142 2.6495 2.8094 3.0149 3.3265 4.0252 42.070 c p (vap.) 1.4807 1.5904 1.7064 1.8305 1.9659 2.1186 2.3018 2.5477 2.9552 4.0178 69.567 BOOKCOMP, Inc. — John Wiley & Sons / Page 67 / 2nd Proofs / Heat Transfer Handbook / Bejan 67 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 [67], (25) Lines: 812 to 844 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [67], (25) w (liq.) 1138.6 1041.7 946.48 852.31 758.32 663.63 567.22 467.82 363.47 249.42 102.20 w (vap.) 178.39 182.73 185.71 187.00 186.27 183.10 176.93 167.00 152.15 130.49 96.500 η (liq.) 410.30 310.40 241.39 192.27 156.15 128.61 106.74 88.534 72.481 57.021 28.956 η (vap.) 6.2933 6.7963 7.3046 7.8224 8.3586 8.9291 9.5620 10.310 11.286 12.827 18.849 λ (liq.) 106.77 100.93 95.472 90.390 85.637 81.154 76.898 72.801 68.750 64.508 54.273 λ (vap.) 11.321 13.160 15.181 17.403 19.849 22.552 25.565 28.972 32.944 37.914 47.550 σ 0.0187 0.0164 0.0143 0.0121 0.0101 0.0081 0.0062 0.0044 0.0027 0.0012 0.0000 Neopentane (2,2-Dimethylpropane) T 280.00 300.00 320.00 340.00 360.00 370.00 380.00 390.00 400.00 410.00 420.00 p 0.0921 0.1819 0.3267 0.5443 0.8539 1.0497 1.2766 1.5378 1.8370 2.1782 2.5670 ρ (liq.) 606.22 583.28 559.16 533.36 505.00 489.41 472.49 453.76 432.43 407.01 374.05 ρ (vap.) 2.9706 5.6289 9.8434 16.232 25.712 32.056 39.849 49.555 61.938 78.430 102.36 h (liq.) −5.8227 39.477 87.305 137.73 190.96 218.75 247.47 277.28 308.47 341.55 377.75 h (vap.) 312.19 341.69 371.77 401.99 431.75 446.19 460.11 473.26 485.20 495.16 501.37 s (liq.) −0.0206 0.1351 0.2885 0.4401 0.5905 0.6656 0.7409 0.8169 0.8941 0.9738 1.0586 s (vap.) 1.1151 1.1424 1.1775 1.2174 1.2594 1.2803 1.3005 1.3194 1.3359 1.3484 1.3529 c v (liq.) 1.5236 1.6487 1.7722 1.8881 1.9973 2.0507 2.1043 2.1592 2.2171 2.2810 2.3577 c v (vap.) 1.4748 1.5909 1.7088 1.8300 1.9560 2.0217 2.0897 2.1610 2.2369 2.3197 2.4140 c p (liq.) 2.2006 2.3239 2.4512 2.5860 2.7422 2.8372 2.9526 3.1027 3.3181 3.6796 4.5015 c p (vap.) 1.6124 1.7470 1.8952 2.0660 2.2777 2.4110 2.5762 2.7952 3.1163 3.6677 4.9415 w (liq.) 1004.3 877.57 757.88 644.46 535.00 480.86 426.56 371.55 315.16 256.39 193.67 w (vap.) 180.13 181.48 180.61 177.10 170.36 165.54 159.57 152.24 143.28 132.30 118.65 Hexane T 200.00 250.00 300.00 325.00 350.00 375.00 400.00 425.00 450.00 475.00 500.00 p 0.000021 0.0015 0.0219 0.0578 0.1299 0.2582 0.4661 0.7803 1.2313 1.8567 2.7139 continued BOOKCOMP, Inc. — John Wiley & Sons / Page 68 / 2nd Proofs / Heat Transfer Handbook / Bejan 68 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 [68], (26) Lines: 844 to 880 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [68], (26) TABLE 2.7 Thermophysical Properties of Fluids along the Saturation Line a (Continued) Hexane (Continued) ρ (liq.) 741.90 697.89 652.98 629.48 604.84 578.59 550.08 518.24 481.07 433.62 350.12 ρ (vap.) 0.0011 0.0639 0.7683 1.9057 4.0858 7.8720 14.046 23.808 39.364 66.089 129.04 h (liq.) −306.56 −206.69 −98.600 −40.702 20.138 84.182 151.72 223.16 299.18 381.51 478.78 h (vap.) 121.00 189.30 265.66 306.52 348.84 392.27 436.28 480.06 522.13 559.07 577.03 s (liq.) −1.1456 −0.7005 −0.3070 −0.1219 0.0581 0.2342 0.4075 0.5793 0.7510 0.9260 1.1209 s (vap.) 0.9922 0.8835 0.9072 0.9465 0.9972 1.0557 1.1189 1.1838 1.2464 1.2998 1.3174 c v (liq.) 1.4405 1.5804 1.7503 1.8457 1.9453 2.0475 2.1508 2.2547 2.3600 2.4716 2.6218 c v (vap.) 1.1868 1.3657 1.5758 1.6930 1.8161 1.9433 2.0731 2.2053 2.3409 2.4847 2.6579 c p (liq.) 1.9301 2.0713 2.2598 2.3714 2.4933 2.6263 2.7743 2.9479 3.1796 3.6056 6.5887 c p (vap.) 1.2833 1.4636 1.6817 1.8086 1.9478 2.1011 2.2746 2.4853 2.7854 3.4001 7.5559 w (liq.) 1515.7 1269.4 1047.6 942.17 838.85 736.47 633.63 528.43 417.67 294.59 138.19 w (vap.) 144.44 160.40 172.79 176.83 178.87 178.39 174.77 167.09 153.94 132.74 98.609 η (liq.) 1306.4 529.19 290.31 227.83 183.11 149.58 123.38 101.98 83.551 66.222 45.006 η (vap.) 4.2946 5.4709 6.6161 7.2117 7.8304 8.4853 9.2018 10.031 11.090 12.712 16.804 λ (liq.) 154.97 142.43 125.48 117.26 109.61 102.62 96.301 90.550 85.124 79.386 70.105 λ (vap.) 6.4043 9.4265 13.258 15.531 18.065 20.879 24.003 27.502 31.520 36.488 44.807 σ 0.0293 0.0234 0.0177 0.0151 0.0125 0.0100 0.0077 0.0055 0.0035 0.0017 0.0003 Heptane T 200.00 250.00 300.00 325.00 350.00 375.00 400.00 425.00 450.00 475.00 500.00 p 2.1 ×10. −6 0.00031 0.0067 0.0204 0.0514 0.1121 0.2182 0.3887 0.6451 1.0120 1.5191 ρ (liq.) 761.24 719.62 677.94 656.47 634.23 610.90 586.03 558.97 528.70 493.27 448.22 ρ (vap.) 0.0001 0.0150 0.2702 0.7680 1.8293 3.8189 7.2279 12.736 21.379 34.995 57.736 h (liq.) −380.96 −279.59 −171.54 −114.10 −54.026 8.9028 74.888 144.16 217.04 294.13 376.79 h (vap.) 47.527 115.51 192.43 234.17 277.88 323.27 369.98 417.53 465.21 511.77 554.66 s (liq.) −1.3567 −0.9047 −0.5112 −0.3274 −0.1495 0.0238 0.1936 0.3609 0.5264 0.6915 0.8588 s (vap.) 0.7857 0.6757 0.7020 0.7442 0.7987 0.8621 0.9314 1.0041 1.0779 1.1497 1.2146 BOOKCOMP, Inc. — John Wiley & Sons / Page 69 / 2nd Proofs / Heat Transfer Handbook / Bejan 69 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 [69], (27) Lines: 880 to 914 ——— * 528.0pt PgVar ——— Normal Page * PgEnds: PageBreak [69], (27) c v (liq.) 1.5143 1.6246 1.7815 1.8727 1.9689 2.0678 2.1676 2.2674 2.3669 2.4667 2.5700 c v (vap.) 1.1910 1.3692 1.5776 1.6923 1.8118 1.9344 2.0586 2.1837 2.3095 2.4372 2.5703 c p (liq.) 1.9825 2.0836 2.2477 2.3479 2.4574 2.5748 2.7007 2.8386 2.9977 3.2033 2.5488 c p (vap.) 1.2739 1.4526 1.6644 1.7838 1.9115 2.0475 2.1934 2.3540 2.5425 2.7963 3.2569 w (liq.) 1576.5 1336.1 1120.1 1018.0 918.29 819.96 721.82 622.51 520.31 412.79 295.82 w (vap.) 133.23 148.24 160.82 165.69 169.16 170.85 170.28 166.88 159.83 147.86 128.88 η (liq.) 2171.4 741.16 380.04 293.16 233.07 189.27 155.88 129.39 107.48 88.425 70.558 η (vap.) 3.5470 4.9751 6.0076 6.5434 7.0975 7.6775 8.2967 8.9798 9.7730 10.775 12.243 λ (liq.) 153.82 143.43 130.74 124.39 118.19 112.17 106.32 100.56 94.763 88.670 81.714 λ (vap.) 5.6156 8.3161 11.741 13.757 15.983 18.427 21.103 24.041 27.294 30.978 35.390 σ 0.0310 0.0253 0.0198 0.0172 0.0148 0.0123 0.0100 0.0078 0.0058 0.0038 0.0021 Octane T 250.00 300.00 350.00 375.00 400.00 425.00 450.00 475.00 500.00 525.00 550.00 p 0.000063 0.0021 0.0207 0.0497 0.1048 0.1993 0.3489 0.5717 0.8882 1.3229 1.9082 ρ (liq.) 736.69 696.69 655.47 633.81 611.07 586.81 560.43 530.96 496.64 453.63 389.70 ρ (vap.) 0.0035 0.0946 0.8269 1.8851 3.8175 7.0696 12.255 20.289 32.752 53.043 92.190 h (liq.) −347.92 −240.35 −123.85 −61.705 3.2520 71.155 142.17 216.57 294.82 378.01 469.56 h (vap.) 46.050 123.10 209.74 256.28 304.60 354.35 405.08 456.14 506.48 554.02 592.73 s (liq.) −1.0811 −0.6893 −0.3306 −0.1593 0.0081 0.1724 0.3341 0.4941 0.6533 0.8139 0.9816 s (vap.) 0.4947 0.5222 0.6225 0.6887 0.7615 0.8387 0.9183 0.9984 1.0767 1.1491 1.2055 c v (liq.) 1.6551 1.8107 1.9962 2.0936 2.1916 2.2891 2.3854 2.4806 2.5754 2.6724 2.7811 c v (vap.) 1.3726 1.5808 1.8108 1.9299 2.0498 2.1699 2.2896 2.4092 2.5299 2.6547 2.7926 c p (liq.) 2.0786 2.2333 2.4311 2.5400 2.6544 2.7750 2.9049 3.0521 3.2372 3.5293 4.3831 c p (vap.) 1.4455 1.6551 1.8916 2.0180 2.1498 2.2887 2.4391 2.6120 2.8367 3.2176 4.4619 w (liq.) 1344.5 1138.6 948.81 857.47 767.20 676.95 585.56 491.62 393.17 287.24 168.34 w (vap.) 138.40 150.71 160.16 163.15 164.51 163.85 160.64 154.15 143.24 125.94 98.584 σ 0.0259 0.0210 0.0163 0.0141 0.0119 0.0098 0.0078 0.0058 0.0040 0.0023 0.0008 continued . 23 .80 0 R-116 — — 9.4 781 11 .88 9 14.212 16.420 18. 510 20.493 22. 382 24. 188 R-12 — — 7 .86 13 9 .89 45 11.925 13.914 15 .83 8 17. 688 19.463 21.166 22 .80 3 R-123 — — 6.9649 8. 9742 10 .86 3 12.632 14. 281 15 .81 0. 1.16 18 1. 188 8 1.3017 1.4791 1.7090 2.0151 2.4 986 3.60 68 12.744 w (liq.) 19 38. 3 1795.5 1647 .8 14 98. 5 1347.7 1194 .8 1039.0 87 8.23 7 08. 85 520.93 276.76 w (vap.) 189 .89 207.39 223.45 236 .89 246 .81 . 1 28. 61 106.74 88 .534 72. 481 57.021 28. 956 η (vap.) 6.2933 6.7963 7.3046 7 .82 24 8. 3 586 8. 9291 9.5620 10.310 11. 286 12 .82 7 18. 849 λ (liq.) 106.77 100.93 95.472 90.390 85 .637 81 .154 76 .89 8 72 .80 1