Table B.1
Thermodynamic Properties of Selected Substances
Substance | R | TPT | TPP | ΔHfus | NBP | ΔHboil | Pc | Tc | vc | Zc | ω | a | b |
Hydrogen | 4124 | 13.96 | 73.59 | 454.5 | 20.37 | 448.7 | 12.96 | 33.15 | 0.0336 | 3.135 | − 0.2187 | 26,785 | 0.0165 |
Para-hydrogen | 4124 | 13.8 | 70.41 | 432.5 | 20.27 | 446.6 | 12.86 | 32.94 | 0.0327 | 3.228 | − 0.2186 | 26,670 | 0.0165 |
Oxygen | 259.8 | 54.36 | 1.463 | 243 | 90.19 | 213.2 | 50.43 | 154.6 | 0.00217 | 3.661 | 0.0222 | 149,769 | 0.0198 |
Nitrogen | 296.8 | 63.15 | 125.2 | 215.5 | 77.36 | 199.2 | 33.96 | 126.2 | 0.00280 | 3.936 | 0.0372 | 148,225 | 0.0240 |
Helium | 2077 | 1 | 1 | 1 | 4.222 | 20.7 | 2.275 | 5.195 | 0.01196 | 3.967 | − 0.385 | 3751 | 0.0147 |
Neon | 412 | 24.56 | 432 | 88.16 | 27.11 | 85.77 | 26.8 | 44.49 | 0.00188 | 3.62 | − 0.037 | 23,345 | 0.0107 |
Argon | 208.1 | 83.81 | 688.9 | 172.2 | 87.3 | 169.4 | 48.63 | 150.7 | 0.00161 | 4.002 | − 0.002 | 147,587 | 0.0200 |
Xenon | 63.32 | 161.4 | 827.6 | 96.72 | 164.9 | 95.87 | 58.4 | 289.7 | 0.001 | 3.142 | 0.0036 | 454,364 | 0.0320 |
Fluorine | 218.8 | 53.48 | 2.413 | 196.3 | 85.03 | 175.2 | 52.4 | 144.4 | 0.00163 | 3.691 | 0.0504 | 125,813 | 0.0178 |
Ammonia | 488.2 | 195.5 | 61.02 | 1486 | 239.8 | 1369 | 113.3 | 405.4 | 0.00516 | 3.381 | 0.2558 | 458,377 | 0.0231 |
Hydrogen sulfide | 244 | 187.7 | 231.9 | 574.7 | 212.9 | 546.6 | 89.63 | 373.4 | 0.00298 | 3.401 | 0.0961 | 491,620 | 0.0269 |
Krypton | 99.21 | 115.8 | 732 | 108.8 | 119.8 | 107.5 | 55.1 | 209.4 | 0.00121 | 3.101 | − 0.002 | 251,616 | 0.0245 |
Methane | 518.3 | 90.69 | 117 | 544.2 | 111.7 | 510.8 | 45.99 | 190.6 | 0.00734 | 2.923 | 0.0114 | 249,574 | 0.0268 |
Methanol | 259.5 | 175.6 | 0.0018 | 1314 | 338.2 | 1103 | 81.04 | 513.4 | 0.00581 | 2.828 | 0.5646 | 1.028 × 106 | 0.0409 |
Ethane | 276.5 | 90.37 | 0.0114 | 595.7 | 184.6 | 489.4 | 48.72 | 305.3 | 0.00451 | 3.838 | 0.0995 | 604,771 | 0.0405 |
Ethanol | 180.5 | 159.1 | 0.00002 | 1017 | 351.4 | 848.8 | 61.48 | 513.9 | 0.00611 | 2.466 | 0.6442 | 1.358 × 106 | 0.0540 |
n-Octane | 72.79 | 216.4 | 0.01399 | 411.5 | 398.6 | 302.4 | 24.97 | 569.3 | 0.00390 | 4.249 | 0.3928 | 4.103 × 106 | 0.1475 |
Isobutane | 143 | 113.6 | 0.00021 | 482.9 | 261.5 | 365.5 | 36.4 | 407.8 | 0.0049 | 3.271 | 0.1853 | 1.444 × 106 | 0.0724 |
Propane | 188.6 | 85.48 | N/A | 1 | 231.1 | 425.3 | 42.47 | 369.8 | 0.00505 | 3.245 | 0.1524 | 1.017 × 106 | 0.0563 |
Isopentane | 115.2 | 112.7 | N/A | N/A | 301 | 342.5 | 33.7 | 460.4 | 0.00446 | 3.524 | 0.2266 | 1.988 × 106 | 0.0883 |
n-Butane | 143 | 134.9 | 0.00693 | 494 | 272.6 | 384.7 | 37.96 | 425.1 | 0.00373 | 4.29 | 0.2 | 1.505 × 106 | 0.0724 |
n-Decane | 58.44 | 243.5 | 0.01452 | 392.6 | 447.4 | 276.3 | 21.03 | 617.7 | 0.00379 | 4.519 | 0.4903 | 5.735 × 106 | 0.19 |
n-Dodecane | 48.81 | 263.6 | 0.00631 | 381.5 | 489.5 | 256.3 | 18.17 | 658.1 | 0.00514 | 3.436 | 0.574 | 7.534 × 106 | 0.2343 |
Isobutane | 143 | 113.6 | 0.00021 | 482.9 | 261.5 | 365.5 | 36.4 | 407.8 | 0.0049 | 3.271 | 0.185 | 1.444 × 106 | 0.0724 |
Isopropanol | 138.4 | 0 | N/A | N/A | 355.6 | 663.1 | 47.62 | 508.3 | 0.00363 | 4.062 | 0.668 | 1.715 × 106 | 0.0690 |
Ethylene | 296.4 | 104 | 1.226 | 568.2 | 169.3 | 482.2 | 50.4 | 282.3 | 0.00484 | 3.43 | 0.086 | 499,944 | 0.0362 |
Cyclohexane | 98.79 | 279.5 | 52.49 | 402.4 | 353.9 | 356 | 40.75 | 553.6 | 0.00375 | 3.571 | 0.2091 | 2.378 × 106 | 0.0878 |
n-Heptane | 82.98 | 182.6 | 0.00176 | 441.1 | 371.5 | 316.9 | 27.27 | 540.1 | 0.00556 | 2.956 | 0.3479 | 3.382 × 106 | 0.1281 |
n-Hexane | 96.49 | 177.8 | 0.0035 | 618.8 | 342.4 | 329.9 | 30.58 | 507.9 | 0.00400 | 3.998 | 0.3117 | 2.666 × 106 | 0.1074 |
n-Nonane | 64.83 | 219.7 | 0.0046 | 410.3 | 424.2 | 288.4 | 22.81 | 594.6 | 0.00482 | 3.5 | 0.4468 | 4.898 × 106 | 0.1686 |
n-Pentane | 115.2 | 143.5 | 0.00012 | 466.1 | 309 | 358 | 33.64 | 469.7 | 0.00540 | 2.977 | 0.2499 | 2.073 × 106 | 0.0903 |
Propylene | 197.6 | 87.95 | N/A | N/A | 225.4 | 439.2 | 46.65 | 365.6 | 0.00458 | 3.38 | 0.1407 | 905,579 | 0.0506 |
R22 | 96.15 | 115.7 | 0.004715 | 301.9 | 232.3 | 232.5 | 49.89 | 369.3 | 0.00203 | 3.503 | 0.2208 | 864,055 | 0.0478 |
R134a | 81.49 | 168.9 | 3.545 | 263.7 | 247.1 | 217 | 40.59 | 374.2 | 0.00170 | 4.408 | 0.3269 | 1.09 × 106 | 0.0596 |
R290 | 188.6 | 85.48 | 1 | 1 | 231.1 | 425.3 | 42.47 | 369.8 | 0.00505 | 3.245 | 0.1524 | 1.0 × 106 | 0.0563 |
R404a | 85.19 | − 555 | 1 | 1 | 226.6 | 199.7 | 37.35 | 345.3 | 0.00193 | 4.065 | 0.275 | 1.0 × 106 | 0.0598 |
R218 | 44.22 | 125.5 | 0.02119 | 141.1 | 236.5 | 105.1 | 26.4 | 345 | 0.00169 | 3.417 | 0.3201 | 1.4 × 106 | 0.0845 |
R245fa | 62.03 | 171.1 | 0.1303 | 258.5 | 288.3 | 196 | 36.51 | 427.2 | 0.00203 | 3.561 | 0.379 | 1.5 × 106 | 0.0756 |
R507a | 84.1 | − 555 | 1 | 1 | 226.1 | 196.3 | 37.14 | 343.9 | 0.00199 | 3.903 | 0.2793 | 1 × 106 | 0.0599 |
R508b | 87.16 | − 555 | 1 | 1 | 184.9 | 163 | 39.25 | 287.1 | 0.0017 | 3.735 | 0.2272 | 664,053 | 0.047 |
R=, gas constant (J/kg K); TPT, triple point temperature (K); TPP, triple point pressure (bar); ΔHfus=, fusion heat at triple point (kJ/kg); NBP, normal boiling point (K); ΔHboil=, boiling enthalpy at normal boiling point; P, pressure (bar); T, temperature (K); v, specific volume (m3/kg); Z, compressibility factor; subscript “c”, critical point; ω, accentric factor; a, b, constants in Peng-Robinson equation of state.
Table B.2
Properties of Air at Atmospheric Pressure
T (°C) | ρ, (g/dm3) | μ, (μPa s) | cp, (J/kg K) | k, (mW/m K) | Pr | β, (K− 1) | c, (m/s) | γ |
− 200 | 47.61 | 5.201 | 1002 | 6.667 | 0.7821 | 0.01367 | 171.6 | 1.401 |
− 170 | 33.77 | 7.311 | 1002 | 9.668 | 0.7581 | 0.009695 | 203.7 | 1.401 |
− 140 | 26.16 | 9.296 | 1002 | 12.53 | 0.7435 | 0.00751 | 231.4 | 1.401 |
− 110 | 21.35 | 11.16 | 1003 | 15.26 | 0.7332 | 0.006129 | 256.2 | 1.401 |
− 80 | 18.03 | 12.93 | 1003 | 17.87 | 0.7251 | 0.005177 | 278.8 | 1.401 |
− 50 | 15.61 | 14.6 | 1003 | 20.37 | 0.7186 | 0.004481 | 299.6 | 1.401 |
− 20 | 13.76 | 16.19 | 1003 | 22.77 | 0.7131 | 0.00395 | 319.1 | 1.401 |
10 | 12.3 | 17.7 | 1004 | 25.09 | 0.7086 | 0.003532 | 337.4 | 1.4 |
40 | 11.12 | 19.15 | 1006 | 27.32 | 0.7049 | 0.003193 | 354.7 | 1.4 |
70 | 10.15 | 20.54 | 1008 | 29.49 | 0.702 | 0.002914 | 371.2 | 1.398 |
100 | 9.334 | 21.88 | 1011 | 31.6 | 0.6999 | 0.00268 | 386.8 | 1.397 |
130 | 8.639 | 23.18 | 1014 | 33.64 | 0.6985 | 0.00248 | 401.8 | 1.395 |
160 | 8.041 | 24.43 | 1018 | 35.64 | 0.6978 | 0.002309 | 416.2 | 1.393 |
190 | 7.52 | 25.64 | 1023 | 37.59 | 0.6977 | 0.002159 | 429.9 | 1.39 |
220 | 7.063 | 26.82 | 1028 | 39.5 | 0.6982 | 0.002028 | 443.2 | 1.387 |
250 | 6.658 | 27.96 | 1034 | 41.37 | 0.6991 | 0.001912 | 456 | 1.384 |
280 | 6.296 | 29.07 | 1041 | 43.2 | 0.7004 | 0.001808 | 468.3 | 1.381 |
310 | 5.973 | 30.16 | 1047 | 45.0 | 0.7019 | 0.001715 | 480.3 | 1.378 |
340 | 5.68 | 31.22 | 1054 | 46.77 | 0.7038 | 0.001631 | 491.9 | 1.374 |
370 | 5.415 | 32.26 | 1061 | 48.51 | 0.7058 | 0.001555 | 503.1 | 1.371 |
400 | 5.174 | 33.28 | 1069 | 50.23 | 0.7079 | 0.001486 | 514.1 | 1.367 |
430 | 4.953 | 34.27 | 1076 | 51.92 | 0.7101 | 0.001422 | 524.7 | 1.364 |
760 | 3.371 | 44.21 | 1147 | 69.34 | 0.7314 | 0.0009679 | 629 | 1.334 |
790 | 3.276 | 45.04 | 1153 | 70.84 | 0.7328 | 0.0009406 | 637.5 | 1.332 |
820 | 3.186 | 45.86 | 1158 | 72.33 | 0.7341 | 0.0009148 | 646 | 1.33 |
850 | 3.101 | 46.67 | 1163 | 73.82 | 0.7353 | 0.0008904 | 654.3 | 1.328 |
880 | 3.02 | 47.48 | 1168 | 75.29 | 0.7364 | 0.0008672 | 662.6 | 1.326 |
910 | 2.944 | 48.28 | 1172 | 76.75 | 0.7374 | 0.0008452 | 670.7 | 1.324 |
940 | 2.871 | 49.07 | 1177 | 78.21 | 0.7383 | 0.0008243 | 678.8 | 1.323 |
970 | 2.802 | 49.85 | 1181 | 79.65 | 0.7391 | 0.0008044 | 686.7 | 1.321 |
1000 | 2.736 | 50.63 | 1185 | 81.09 | 0.7398 | 0.0007855 | 694.5 | 1.32 |
T, temperature; ρ, density; μ, dynamic viscosity; cp, specific heat; k,thermal conductivity; Pr, Prandtl number; β, volume expansion coefficient; c, sound speed; γ,adiabatic expansion coefficient; ω = − 0.009278,accentric factor. Critical parameters: Tc = 132.531 K, Pc = 37.86 bar, vc = 2.917 dm3/kg.
Table B.3
Thermophysical Properties of Pure Water at Atmospheric Pressure
T (°C) | ρ, (kg/m3) | μ, (Pa s) | cp, (J/kg K) | k, (W/mK) | Pr | β, (K− 1) | c, (m/s) | σ, (N/m) |
5 | 1000 | 0.001519 | 4200 | 0.5576 | 11.44 | 0.00001135 | 1426 | 0.07494 |
10 | 999.7 | 0.001307 | 4188 | 0.5674 | 9.642 | 0.00008743 | 1448 | 0.07422 |
15 | 999.1 | 0.001138 | 4184 | 0.5769 | 8.253 | 0.0001523 | 1467 | 0.07348 |
20 | 998.2 | 0.001002 | 4183 | 0.5861 | 7.152 | 0.000209 | 1483 | 0.07273 |
25 | 997.1 | 0.0008905 | 4183 | 0.5948 | 6.263 | 0.0002594 | 1497 | 0.07197 |
30 | 995.7 | 0.0007977 | 4183 | 0.603 | 5.534 | 0.0003051 | 1509 | 0.07119 |
35 | 994 | 0.0007196 | 4183 | 0.6107 | 4.929 | 0.000347 | 1520 | 0.0704 |
40 | 992.2 | 0.0006533 | 4182 | 0.6178 | 4.422 | 0.0003859 | 1528 | 0.06959 |
45 | 990.2 | 0.0005963 | 4182 | 0.6244 | 3.994 | 0.0004225 | 1534 | 0.06877 |
50 | 988 | 0.0005471 | 4181 | 0.6305 | 3.628 | 0.0004572 | 1537 | 0.06794 |
55 | 985.7 | 0.0005042 | 4182 | 0.636 | 3.315 | 0.0004903 | 1538 | 0.0671 |
60 | 983.2 | 0.0004666 | 4183 | 0.641 | 3.045 | 0.0005221 | 1537 | 0.06624 |
65 | 980.6 | 0.0004334 | 4184 | 0.6455 | 2.81 | 0.0005528 | 1534 | 0.06536 |
70 | 977.8 | 0.000404 | 4187 | 0.6495 | 2.605 | 0.0005827 | 1529 | 0.06448 |
75 | 974.9 | 0.0003779 | 4190 | 0.653 | 2.425 | 0.0006118 | 1523 | 0.06358 |
80 | 971.8 | 0.0003545 | 4194 | 0.6562 | 2.266 | 0.0006402 | 1514 | 0.06267 |
85 | 968.6 | 0.0003335 | 4199 | 0.6589 | 2.125 | 0.0006682 | 1504 | 0.06175 |
90 | 965.3 | 0.0003145 | 4204 | 0.6613 | 2 | 0.0006958 | 1491 | 0.06081 |
95 | 961.9 | 0.0002974 | 4210 | 0.6634 | 1.888 | 0.000723 | 1475 | 0.05987 |
100 | 0.5896 | 0.00001227 | 2042 | 0.02506 | 0.9996 | 0.002881 | 472.8 | 0.05891 |
T, temperature; ρ, density; μ,dynamic viscosity; cp, specific heat; k, thermal conductivity; Pr, Prandtl number; β, volume expansion coefficient; c, sound speed; σ, superficial tension; ω = 0.3443, accentric factor. Critical parameters: Tc = 373.984 °C, Pc = 220.64 bar, vc = 3.106 dm3/kg. Triple point parameters: Tt = 0.01 °C, Pt = 611.732 Pa.
Table B.4
Thermophysical Properties of Water at Saturation
T | P | σ | ρL | cpL | kL | μL | PrL | βL | vV | cpV | kV | μV | PrV | βV | γ |
0.01 | 0.00612 | 75.64 | 1000 | 4.23 | 547.5 | 1792 | 13.84 | N/A | 206.0 | 1.87 | 17.07 | 9.216 | 1.008 | 3.672 | 1.33 |
10 | 0.0123 | 74.22 | 999.7 | 4.19 | 567.4 | 1307 | 9.645 | 0.0872 | 106.3 | 1.87 | 17.62 | 9.461 | 1.006 | 3.548 | 1.33 |
20 | 0.0234 | 72.73 | 998.2 | 4.18 | 586 | 1002 | 7.154 | 0.209 | 57.78 | 1.88 | 18.22 | 9.727 | 1.004 | 3.435 | 1.33 |
30 | 0.0425 | 71.19 | 995.6 | 4.18 | 602.9 | 797.7 | 5.535 | 0.305 | 32.9 | 1.89 | 18.88 | 10.01 | 1.003 | 3.332 | 1.33 |
40 | 0.0738 | 69.59 | 992.2 | 4.18 | 617.8 | 653.3 | 4.423 | 0.386 | 19.53 | 1.90 | 19.59 | 10.31 | 1.002 | 3.239 | 1.33 |
50 | 0.1234 | 67.94 | 988 | 4.18 | 630.4 | 547.1 | 3.629 | 0.457 | 12.04 | 1.92 | 20.36 | 10.62 | 1.001 | 3.156 | 1.33 |
60 | 0.1993 | 66.24 | 983.2 | 4.18 | 640.9 | 466.6 | 3.045 | 0.522 | 7.674 | 1.94 | 21.18 | 10.93 | 1 | 3.082 | 1.33 |
70 | 0.3118 | 64.48 | 977.7 | 4.19 | 649.5 | 404 | 2.605 | 0.583 | 5.045 | 1.96 | 22.06 | 11.26 | 0.9995 | 3.017 | 1.33 |
80 | 0.4737 | 62.67 | 971.8 | 4.19 | 656.2 | 354.5 | 2.266 | 0.64 | 3.409 | 1.98 | 23 | 11.59 | 0.9993 | 2.962 | 1.33 |
90 | 0.7012 | 60.81 | 965.3 | 4.20 | 661.3 | 314.5 | 2 | 0.696 | 2.362 | 2.01 | 24 | 11.93 | 0.9994 | 2.917 | 1.34 |
100 | 1.013 | 58.91 | 958.4 | 4.22 | 665.1 | 281.9 | 1.787 | 0.75 | 1.674 | 2.04 | 25.08 | 12.27 | 1 | 2.882 | 1.34 |
110 | 1.432 | 56.96 | 951 | 4.23 | 667.6 | 254.8 | 1.615 | 0.804 | 1.211 | 2.08 | 26.22 | 12.61 | 1.001 | 2.857 | 1.34 |
120 | 1.985 | 54.96 | 943.2 | 4.25 | 669.1 | 232.1 | 1.474 | 0.858 | 0.892 | 2.12 | 27.44 | 12.96 | 1.004 | 2.843 | 1.35 |
130 | 2.7 | 52.93 | 934.9 | 4.27 | 669.7 | 213 | 1.357 | 0.912 | 0.669 | 2.17 | 28.73 | 13.3 | 1.007 | 2.84 | 1.36 |
140 | 3.612 | 50.85 | 926.2 | 4.29 | 669.4 | 196.6 | 1.259 | 0.968 | 0.509 | 2.23 | 30.09 | 13.65 | 1.012 | 2.849 | 1.36 |
150 | 4.757 | 48.74 | 917.1 | 4.31 | 668.3 | 182.5 | 1.178 | 1.026 | 0.393 | 2.30 | 31.54 | 13.99 | 1.02 | 2.872 | 1.37 |
160 | 6.177 | 46.59 | 907.5 | 4.34 | 666.4 | 170.3 | 1.109 | 1.087 | 0.3071 | 2.37 | 33.06 | 14.34 | 1.029 | 2.908 | 1.39 |
170 | 7.915 | 44.4 | 897.5 | 4.37 | 663.7 | 159.6 | 1.051 | 1.152 | 0.243 | 2.46 | 34.66 | 14.68 | 1.042 | 2.959 | 1.40 |
180 | 10.02 | 42.19 | 887.1 | 4.40 | 660.2 | 150.2 | 1.002 | 1.221 | 0.194 | 2.56 | 36.34 | 15.03 | 1.057 | 3.027 | 1.42 |
190 | 12.54 | 39.94 | 876.1 | 4.44 | 655.9 | 141.8 | 0.9607 | 1.296 | 0.156 | 2.67 | 38.09 | 15.37 | 1.077 | 3.114 | 1.44 |
200 | 15.54 | 37.67 | 864.7 | 4.49 | 650.7 | 134.4 | 0.9269 | 1.377 | 0.127 | 2.80 | 39.93 | 15.71 | 1.1 | 3.221 | 1.46 |
210 | 19.06 | 35.38 | 852.8 | 4.54 | 644.7 | 127.7 | 0.8994 | 1.467 | 0.104 | 2.94 | 41.85 | 16.06 | 1.129 | 3.351 | 1.48 |
220 | 23.18 | 33.06 | 840.3 | 4.60 | 637.6 | 121.6 | 0.8777 | 1.567 | 0.086 | 3.11 | 43.86 | 16.41 | 1.162 | 3.508 | 1.52 |
230 | 27.95 | 30.73 | 827.3 | 4.67 | 629.5 | 116 | 0.8615 | 1.679 | 0.071 | 3.30 | 45.96 | 16.76 | 1.203 | 3.697 | 1.55 |
240 | 33.45 | 28.39 | 813.5 | 4.76 | 620.3 | 110.9 | 0.8508 | 1.807 | 0.06 | 3.51 | 48.15 | 17.12 | 1.25 | 3.923 | 1.59 |
250 | 39.74 | 26.04 | 799.1 | 4.86 | 609.8 | 106.2 | 0.8455 | 1.954 | 0.050 | 3.77 | 50.46 | 17.49 | 1.306 | 4.195 | 1.64 |
260 | 46.89 | 23.68 | 783.8 | 4.97 | 598 | 101.7 | 0.846 | 2.126 | 0.042 | 4.06 | 52.9 | 17.88 | 1.373 | 4.523 | 1.70 |
270 | 55 | 21.33 | 767.7 | 5.11 | 584.5 | 97.55 | 0.853 | 2.33 | 0.036 | 4.41 | 55.49 | 18.28 | 1.453 | 4.923 | 1.77 |
280 | 64.13 | 18.99 | 750.5 | 5.28 | 569.4 | 93.56 | 0.8673 | 2.576 | 0.031 | 4.83 | 58.28 | 18.7 | 1.549 | 5.415 | 1.86 |
290 | 74.38 | 16.66 | 732.2 | 5.48 | 552.3 | 89.71 | 0.8908 | 2.88 | 0.026 | 5.33 | 61.31 | 19.15 | 1.666 | 6.032 | 1.97 |
300 | 85.84 | 14.35 | 712.4 | 5.74 | 533.1 | 85.95 | 0.9262 | 3.266 | 0.022 | 5.97 | 64.67 | 19.65 | 1.813 | 6.822 | 2.11 |
310 | 98.61 | 12.08 | 691 | 6.08 | 511.3 | 82.22 | 0.9782 | 3.773 | 0.018 | 6.78 | 68.45 | 20.21 | 2.001 | 7.861 | 2.29 |
320 | 112.8 | 9.858 | 667.4 | 6.54 | 486.8 | 78.46 | 1.054 | 4.47 | 0.015 | 7.87 | 72.84 | 20.84 | 2.251 | 9.278 | 2.54 |
330 | 128.5 | 7.697 | 641 | 7.2 | 458.8 | 74.57 | 1.17 | 5.489 | 0.013 | 9.41 | 78.1 | 21.6 | 2.603 | 11.31 | 2.91 |
340 | 145.9 | 5.62 | 610.8 | 8.24 | 426.9 | 70.45 | 1.359 | 7.116 | 0.011 | 11.8 | 84.68 | 22.55 | 3.137 | 14.43 | 3.47 |
350 | 165.2 | 3.66 | 574.7 | 10.1 | 389.7 | 65.88 | 1.711 | 10.1 | 0.0088 | 15.9 | 93.48 | 23.81 | 4.058 | 19.77 | 4.47 |
360 | 186.6 | 1.872 | 528.1 | 14.7 | 344.4 | 60.39 | 2.574 | 17.11 | 0.007 | 25.2 | 106.6 | 25.71 | 6.085 | 30.79 | 6.74 |
370 | 210.3 | 0.3846 | 453.1 | 41.7 | 280.7 | 52.25 | 7.765 | 45.88 | 0.0050 | 70.4 | 132.6 | 29.57 | 15.7 | 64.53 | 18.0 |
373.9 | 220.4 | 0.0004 | 349.4 | N/A | 210.8 | 41.95 | 277.1 | 87.51 | 0.0034 | 340.1 | 180 | 37 | 69.91 | 104.5 | 84.5 |
T, temperature (°C); P, pressure (bar); σ=, surface tension (mN/m); ρ, density (kg/m3); cp, specific heat (kJ/kg K); k, thermal conductivity (mW/m K); μ, dynamic viscosity (μPa s); Pr, Prandtl number; β, volumetric expansion coefficient (mK− 1); v, specific volume (m3/kg); γ, isentropic expansion coefficient of saturated vapor; indices: L, liquid; V, vapor.
Table B.5
Thermophysical Properties of Hydrogen at Saturation
T | P | σ | ρL | cpL | kL | μL | PrL | βL | vV | cpV | kV | μV | PrV | βV | γ |
14 | 0.08 | 2.977 | 77.0 | 6.992 | 74.36 | 24.30 | 2.29 | 10.58 | 7.6332 | 10.56 | 14.51 | 1.24 | 0.90 | 74.32 | 1.69 |
15 | 0.13 | 2.819 | 76.1 | 7.335 | 81.62 | 21.68 | 1.95 | 11.26 | 4.7044 | 10.69 | 15.21 | 1.27 | 0.89 | 70.67 | 1.70 |
16 | 0.21 | 2.656 | 75.3 | 7.717 | 87.55 | 19.39 | 1.71 | 12.01 | 3.0742 | 10.85 | 15.94 | 1.31 | 0.89 | 67.82 | 1.72 |
17 | 0.32 | 2.490 | 74.3 | 8.132 | 92.26 | 17.40 | 1.53 | 12.87 | 2.1066 | 11.03 | 16.69 | 1.34 | 0.89 | 65.69 | 1.74 |
18 | 0.47 | 2.321 | 73.4 | 8.574 | 95.85 | 15.69 | 1.40 | 13.85 | 1.4996 | 11.25 | 17.49 | 1.37 | 0.88 | 64.23 | 1.77 |
19 | 0.13 | 2.819 | 76.1 | 7.335 | 81.62 | 21.68 | 1.95 | 11.26 | 4.7044 | 10.69 | 15.21 | 1.27 | 0.89 | 70.67 | 1.70 |
20 | 0.91 | 1.977 | 71.3 | 9.563 | 100.1 | 12.97 | 1.24 | 16.18 | 0.8288 | 11.85 | 19.21 | 1.44 | 0.89 | 63.20 | 1.84 |
21 | 1.22 | 1.804 | 70.1 | 10.13 | 101 | 11.92 | 1.20 | 17.60 | 0.6370 | 12.25 | 20.15 | 1.48 | 0.90 | 63.63 | 1.89 |
22 | 1.59 | 1.630 | 68.9 | 10.76 | 101.1 | 11.02 | 1.17 | 19.26 | 0.4981 | 12.75 | 21.16 | 1.51 | 0.91 | 64.74 | 1.95 |
23 | 2.04 | 1.458 | 67.6 | 11.48 | 100.7 | 10.26 | 1.17 | 21.23 | 0.3951 | 13.36 | 22.25 | 1.54 | 0.93 | 66.61 | 2.03 |
24 | 2.58 | 1.286 | 66.2 | 12.31 | 99.8 | 9.61 | 1.18 | 23.60 | 0.3171 | 14.12 | 23.43 | 1.68 | 1.01 | 69.39 | 2.12 |
25 | 3.21 | 1.117 | 64.7 | 13.28 | 98.51 | 9.03 | 1.22 | 26.55 | 0.2569 | 15.07 | 24.72 | 1.73 | 1.05 | 73.32 | 2.23 |
26 | 3.94 | 0.952 | 63.1 | 14.46 | 96.94 | 8.51 | 1.27 | 30.30 | 0.2098 | 16.29 | 26.14 | 1.78 | 1.11 | 78.77 | 2.37 |
27 | 4.78 | 0.790 | 61.3 | 15.95 | 95.2 | 8.00 | 1.34 | 35.28 | 0.1722 | 17.90 | 27.73 | 1.85 | 1.19 | 86.38 | 2.56 |
28 | 5.74 | 0.634 | 59.3 | 17.91 | 93.4 | 7.49 | 1.44 | 42.19 | 0.1418 | 20.09 | 29.53 | 1.92 | 1.31 | 97.27 | 2.82 |
29 | 6.82 | 0.484 | 57.1 | 20.69 | 91.64 | 6.95 | 1.57 | 52.50 | 0.1168 | 23.24 | 31.62 | 2.01 | 1.47 | 113.61 | 3.19 |
30 | 8.04 | 0.343 | 54.5 | 25.02 | 90.02 | 6.35 | 1.76 | 69.50 | 0.0957 | 28.15 | 34.11 | 2.11 | 1.74 | 140.12 | 3.76 |
31 | 9.42 | 0.213 | 51.4 | 32.99 | 88.65 | 5.65 | 2.10 | 102.69 | 0.0775 | 36.81 | 37.28 | 2.26 | 2.23 | 189.42 | 4.75 |
32 | 10.96 | 0.097 | 47.1 | 53.14 | 87.64 | 4.84 | 2.93 | 193.05 | 0.0606 | 55.68 | 42.11 | 2.50 | 3.31 | 308.86 | 6.89 |
33.1 | 12.88 | 0.0017 | 35.3 | 200 | 1000 | N/A | N/A | 981.45 | 0.0367 | 131.74 | 59.93 | 3.41 | 7.50 | 1036.71 | 15.44 |
T, temperature (K); P, pressure (bar); σ, surface tension (mN/m); ρ, density (kg/m3); cp, specific heat (kJ/kg K); k, thermal conductivity (mW/m K); μ, dynamic viscosity (μPa s); Pr, Prandtl number; β, volumetric expansion coefficient (mK− 1); v, specific volume (m3/kg); γ, isentropic expansion coefficient of saturated vapor; indices: L, liquid; V, vapor.
Table B.6
Thermophysical Properties of Oxygen at Saturation
T | P | σ | ρL | cpL | kL | μL | PrL | βL | vV | cpV | kV | μV | PrV | βV | γ |
55 | N/A | 22.30 | 1303.5 | 1.455 | 201 | 747.53 | 5.41 | N/A | 80.029 | 0.93 | 4.48 | 4.15 | 0.86 | 18.28 | 1.39 |
60 | 0.01 | 20.98 | 1283.1 | 126.4 | 194.3 | 582.46 | 379.02 | 3.49 | 21.463 | 0.95 | 4.98 | 4.55 | 0.86 | 16.87 | 1.39 |
65 | 0.02 | 19.66 | 1260.7 | 1.65 | 187.2 | 460.77 | 4.06 | 3.58 | 7.2177 | 0.96 | 5.49 | 4.96 | 0.87 | 15.70 | 1.38 |
70 | 0.06 | 18.348 | 1237.9 | 1.657 | 180.1 | 373.97 | 3.44 | 3.70 | 2.8933 | 0.97 | 5.99 | 5.36 | 0.87 | 14.70 | 1.38 |
75 | 0.15 | 17.039 | 1214.9 | 9.855 | 172.9 | 310.37 | 17.69 | 3.83 | 1.3306 | 0.98 | 6.50 | 5.75 | 0.86 | 13.84 | 1.39 |
80 | 0.30 | 15.739 | 1191.4 | 1.66 | 165.8 | 262.53 | 2.63 | N/A | 0.6819 | 0.97 | 7.03 | 6.15 | 0.85 | 13.13 | 1.40 |
85 | 0.57 | 14.450 | 1167.5 | 1.669 | 158.6 | 225.61 | 2.37 | 4.15 | 0.3809 | 0.97 | 7.56 | 6.54 | 0.84 | 12.58 | 1.41 |
90 | 0.99 | 13.176 | 1142.9 | 1.683 | 151.3 | 196.38 | 2.18 | 4.36 | 0.2281 | 0.97 | 8.12 | 6.94 | 0.83 | 12.22 | 1.43 |
95 | 1.63 | 11.919 | 1117.7 | 1.704 | 144 | 172.66 | 2.04 | 4.59 | 0.1445 | 0.98 | 8.70 | 7.33 | 0.83 | 12.03 | 1.46 |
100 | 2.54 | 10.6829 | 1091.5 | 1.731 | 136.7 | 152.96 | 1.94 | 4.88 | 0.0959 | 1.00 | 9.31 | 7.73 | 0.83 | 12.04 | 1.49 |
105 | 3.79 | 9.4707 | 1064.4 | 1.765 | 129.3 | 136.23 | 1.86 | 5.21 | 0.0661 | 1.04 | 9.96 | 8.13 | 0.85 | 12.26 | 1.52 |
110 | 5.43 | 8.2861 | 1035.9 | 1.808 | 121.9 | 121.74 | 1.81 | 5.62 | 0.0470 | 1.09 | 10.66 | 8.55 | 0.88 | 12.71 | 1.57 |
115 | 7.56 | 7.1328 | 1006.0 | 1.861 | 114.4 | 108.97 | 1.77 | 6.13 | 0.0342 | 1.16 | 11.42 | 8.98 | 0.92 | 13.42 | 1.62 |
120 | 10.22 | 6.0154 | 974.2 | 1.927 | 106.9 | 97.53 | 1.76 | 6.76 | 0.0254 | 1.26 | 12.26 | 9.43 | 0.97 | 14.49 | 1.70 |
125 | 13.51 | 4.9387 | 939.7 | 2.013 | 99.43 | 87.09 | 1.76 | N/A | 0.0192 | 1.38 | 13.19 | 9.91 | 1.04 | 16.05 | 1.80 |
130 | 17.49 | 3.9088 | 902.6 | 2.152 | 92.02 | 77.59 | 1.81 | 9.52 | 0.0146 | 1.56 | 14.26 | 10.44 | 1.14 | 18.36 | 1.95 |
135 | 22.25 | 2.9333 | 861.0 | 2.35 | 84.54 | 68.69 | 1.91 | 11.69 | 0.0112 | 1.81 | 15.50 | 11.06 | 1.29 | 21.96 | 2.17 |
140 | 27.88 | 2.0224 | 813.1 | 2.682 | 76.97 | 60.20 | 2.10 | 15.40 | 0.0086 | 2.22 | 17.04 | 11.82 | 1.54 | 28.07 | 2.52 |
145 | 34.48 | 1.192 | 755.0 | 3.337 | 69.11 | 51.85 | 2.50 | 23.04 | 0.0065 | 3.00 | 19.09 | 12.88 | 2.02 | 40.28 | 3.17 |
150 | 42.19 | 0.472 | 675.5 | 5.225 | 60.16 | 42.90 | 3.73 | 46.63 | 0.0047 | 4.95 | 22.39 | 14.71 | 3.26 | 74.61 | 4.73 |
154 | 49.31 | 0.036 | 547.4 | 15.42 | 48.04 | 32.13 | 10.31 | N/A | 0.0031 | 10.63 | 29.63 | 19.14 | 6.86 | 218.2 | 8.44 |
T, temperature (K); P, pressure (bar); σ, surface tension (mN/m); ρ, density (kg/m3); cp, specific heat (kJ/kg K); k, thermal conductivity (mW/m K); μ, dynamic viscosity (μPa s); Pr, Prandtl number; β, volumetric expansion coefficient (mK− 1); v, specific volume (m3/kg); γ, isentropic expansion coefficient of saturated vapor; indices: L, liquid; V, vapor.
Table B.7
Thermophysical Properties of Nitrogen at Saturation
T | P | σ | ρL | cpL | kL | μL | PrL | βL | vV | cpV | kV | μV | PrV | βV | γ |
64 | 0.15 | 11.9581 | 863.7 | 2.002 | 171.5 | 297.50 | 3.47 | 4.78 | 1.2869 | 1.06 | 5.71 | 4.44 | 0.82 | 16.13 | 1.41 |
65 | 0.17 | 11.7169 | 859.6 | 1.994 | 169.5 | 282.08 | 3.32 | 4.82 | 1.0950 | 1.06 | 5.82 | 4.51 | 0.82 | 15.95 | 1.41 |
70 | 0.39 | 10.5262 | 838.5 | 2.005 | 159.5 | 220.26 | 2.77 | 5.11 | 0.5274 | 1.08 | 6.35 | 4.88 | 0.83 | 15.24 | 1.43 |
75 | 0.76 | 9.3624 | 816.7 | 27.05 | 149.5 | 176.75 | 31.99 | N/A | 0.2825 | 1.11 | 6.91 | 5.26 | 0.84 | 14.82 | 1.44 |
80 | 1.37 | 8.2276 | 793.9 | 2.054 | 139.5 | 145.11 | 2.14 | N/A | 0.1642 | 1.14 | 7.49 | 5.65 | 0.86 | 14.69 | 1.47 |
85 | 2.29 | 7.1240 | 770.1 | 2.094 | 129.6 | 121.31 | 1.96 | N/A | 0.1018 | 1.19 | 8.11 | 6.06 | 0.89 | 14.89 | 1.51 |
90 | 3.60 | 6.0544 | 745.0 | 2.147 | 119.6 | 102.83 | 1.85 | 6.94 | 0.0663 | 1.26 | 8.79 | 6.48 | 0.93 | 15.46 | 1.56 |
95 | 5.41 | 5.0222 | 718.3 | 7.073 | 109.7 | 88.02 | 5.68 | N/A | 0.0449 | 1.35 | 9.55 | 6.94 | 0.98 | 16.54 | 1.64 |
100 | 7.78 | 4.0318 | 689.4 | 2.301 | 99.71 | 75.77 | 1.75 | 9.15 | 0.0313 | 1.55 | 10.44 | 7.43 | 1.10 | 18.14 | 1.67 |
105 | 10.83 | 3.0892 | 659.0 | 2.432 | 90.15 | 65.72 | 1.77 | 10.21 | 0.0222 | 1.44 | 11.49 | 7.98 | 1.00 | 18.19 | 1.80 |
110 | 14.66 | 2.2025 | 625.6 | 2.736 | 80.72 | 56.96 | 1.93 | 12.90 | 0.0160 | 1.16 | 12.80 | 8.63 | 0.78 | 20.83 | 3.96 |
115 | 19.37 | 1.3844 | 583.8 | 3.211 | 70.45 | 48.23 | 2.20 | 18.78 | 0.0115 | 2.02 | 14.51 | 9.44 | 1.32 | 31.69 | 3.57 |
120 | 25.11 | 0.6578 | 527.5 | 4.351 | 59.19 | 39.02 | 2.87 | 33.00 | 0.0080 | 3.74 | 16.98 | 10.62 | 2.34 | 56.88 | 4.00 |
125 | 32.07 | 0.0829 | 430.2 | 11.79 | 44.96 | 27.35 | 7.17 | 136.45 | 0.0049 | 9.65 | 22.52 | 13.33 | 5.71 | 187.71 | N/A |
126 | 33.65 | 0.0083 | 378.6 | 20.16 | 38.93 | 22.77 | 11.79 | 266.83 | 0.0039 | 13.27 | 26.63 | 15.37 | 7.66 | 308.90 | 8.52 |
T, temperature (K); P, pressure (bar); σ, surface tension (mN/m); ρ, density (kg/m3); cp, specific heat (kJ/kg K); k, thermal conductivity (mW/m K); μ, dynamic viscosity (μPa s); Pr, Prandtl number; β, volumetric expansion coefficient (mK− 1); v, specific volume (m3/kg); γ, isentropic expansion coefficient of saturated vapor; indices: L, liquid; V, vapor.
Table B.8
Thermophysical Properties of Carbon Dioxide at Saturation
T | P | σ | ρL | cpL | kL | μL | PrL | βL | vV | cpV | kV | μV | PrV | βV | γ |
− 56.6 | 5.18 | 15.7767 | 1178.5 | 1.953 | 180.4 | 256.7 | 2.78 | N/A | 0.0727 | 0.90 | 10.97 | 10.95 | 0.90 | 6.11 | 1.44 |
− 50 | 6.82 | 14.3248 | 1154.6 | 14.29 | 171.8 | 229.3 | 19.07 | 3.27 | 0.0558 | 0.95 | 11.51 | 11.31 | 0.93 | 6.30 | 1.46 |
− 45 | 8.32 | 13.2367 | 1135.9 | 1.989 | 165.3 | 210.7 | 2.54 | 3.36 | 0.0460 | 0.98 | 11.94 | 11.58 | 0.95 | 6.50 | 1.48 |
− 40 | 10.05 | 12.1654 | 1116.5 | 2.011 | 158.9 | 193.8 | 2.45 | N/A | 0.0383 | 1.03 | 12.41 | 11.87 | 0.98 | 6.74 | 1.51 |
− 35 | 12.02 | 11.1118 | 1096.4 | 4.99 | 152.5 | 178.3 | 5.83 | N/A | 0.0320 | 1.07 | 12.90 | 12.16 | 1.01 | 7.04 | 1.54 |
− 30 | 14.28 | 10.0769 | 1075.7 | 2.377 | 146.3 | 164.2 | 2.67 | 3.93 | 0.0270 | 1.13 | 13.42 | 12.46 | 1.05 | 7.41 | 1.57 |
− 25 | 16.83 | 9.0619 | 1054.2 | 2.114 | 140 | 151.3 | 2.28 | 4.38 | 0.0228 | 1.19 | 13.99 | 12.78 | 1.09 | 7.87 | 1.62 |
− 20 | 19.70 | 8.0682 | 1031.7 | 2.165 | 133.8 | 139.3 | 2.25 | 4.74 | 0.0193 | 1.27 | 14.60 | 13.12 | 1.14 | 8.44 | 1.67 |
− 15 | 22.91 | 7.0974 | 1008.0 | 2.227 | 127.6 | 128.3 | 2.24 | 5.18 | 0.0165 | 1.36 | 15.27 | 13.47 | 1.20 | 9.15 | 1.73 |
− 10 | 26.49 | 6.1514 | 982.9 | 2.306 | 121.4 | 118 | 2.24 | 5.73 | 0.0140 | 1.47 | 16.01 | 13.86 | 1.27 | 10.06 | 1.81 |
− 5 | 30.46 | 5.2326 | 956.2 | 2.406 | 115.1 | 108.4 | 2.27 | 6.44 | 0.0120 | 1.61 | 16.84 | 14.30 | 1.37 | 11.23 | 1.92 |
0 | 34.85 | 4.3440 | 927.4 | 2.539 | 108.7 | 99.39 | 2.32 | 7.37 | 0.0102 | 1.79 | 17.77 | 14.79 | 1.49 | 12.79 | 2.05 |
5 | 39.69 | 3.4893 | 896.0 | 2.72 | 102.2 | 90.81 | 2.42 | 8.67 | 0.0087 | 2.03 | 18.86 | 15.36 | 1.65 | 14.95 | 2.23 |
10 | 45.02 | 2.6737 | 861.1 | 2.985 | 95.46 | 82.55 | 2.58 | 10.59 | 0.0074 | 2.37 | 20.14 | 16.06 | 1.89 | 18.12 | 2.49 |
15 | 50.87 | 1.9043 | 821.2 | 3.405 | 88.32 | 74.43 | 2.87 | 13.71 | 0.0062 | 2.89 | 21.74 | 16.95 | 2.25 | 23.17 | 2.88 |
20 | 57.29 | 1.1924 | 773.4 | 4.159 | 80.48 | 66.15 | 3.42 | 19.52 | 0.0051 | 3.77 | 23.83 | 18.19 | 2.87 | 32.32 | 3.51 |
25 | 64.34 | 0.5584 | 711.8 | 5.903 | 71.43 | 57.23 | 4.73 | 33.72 | 0.0041 | 5.54 | 26.94 | 20.16 | 4.14 | 53.05 | 4.69 |
30 | 72.14 | 0.0582 | 602.4 | 13.83 | 57.69 | 44.68 | 10.71 | 102.99 | 0.0029 | 10.16 | 33.86 | 25.03 | 7.51 | 128.22 | 6.80 |
30.9 | 73.64 | 0.0025 | 521.3 | 18.05 | 49.07 | 37.25 | 13.71 | 141.42 | 0.0024 | 11.77 | 39.21 | 29.16 | 8.75 | 163.45 | 5.80 |
T, temperature (°C); P, pressure (bar); σ, surface tension (mN/m); ρ, density (kg/m3); cp, specific heat (kJ/kg K); k, thermal conductivity (mW/m K); μ, dynamic viscosity (μPa s); Pr, Prandtl number; β, volumetric expansion coefficient (mK− 1); v, specific volume (m3/kg); γ, isentropic expansion coefficient of saturated vapor; indices: L, liquid; V, vapor.
Table B.9
Thermophysical Properties of Ammonia at Saturation
T | P | σ | ρL | cpL | kL | μL | PrL | βL | vV | cpV | kV | μV | PrV | βV | γ |
− 77.6 | 0.061 | 44.78 | 733.6 | 3.95 | 821.2 | 564.1 | 2.713 | 1.514 | 15.68 | 2.062 | 19.64 | 6.84 | 0.7182 | 5.23 | 1.325 |
− 65 | 0.1563 | 41.51 | 719.3 | 4.162 | 774.8 | 430.6 | 2.312 | 1.586 | 6.478 | 2.102 | 19.82 | 7.162 | 0.7597 | 4.99 | 1.328 |
− 55 | 0.3013 | 38.95 | 707.8 | 4.332 | 739.3 | 357.5 | 2.095 | 1.63 | 3.498 | 2.147 | 20.07 | 7.433 | 0.7951 | 4.86 | 1.331 |
− 45 | 0.5447 | 36.42 | 696 | 4.387 | 704.6 | 303 | 1.887 | 1.717 | 2.008 | 2.205 | 20.43 | 7.715 | 0.8328 | 4.77 | 1.336 |
− 35 | 0.9307 | 33.93 | 683.9 | 4.439 | 670.8 | 261.2 | 1.728 | 1.804 | 1.215 | 2.277 | 20.88 | 8.004 | 0.8729 | 4.72 | 1.343 |
− 25 | 1.515 | 31.46 | 671.4 | 4.489 | 638 | 228.3 | 1.606 | 1.896 | 0.7695 | 2.365 | 21.44 | 8.3 | 0.9154 | 4.716 | 1.352 |
− 15 | 2.362 | 29.04 | 658.6 | 4.538 | 605.9 | 201.7 | 1.511 | 1.995 | 0.5068 | 2.47 | 22.12 | 8.599 | 0.9603 | 4.757 | 1.364 |
− 5 | 3.549 | 26.65 | 645.4 | 4.589 | 574.7 | 179.8 | 1.436 | 2.079 | 0.3452 | 2.595 | 22.92 | 8.902 | 1.008 | 4.846 | 1.379 |
5 | 5.16 | 24.29 | 631.8 | 4.643 | 544.3 | 161.4 | 1.377 | 2.199 | 0.2421 | 2.74 | 23.85 | 9.209 | 1.058 | 4.989 | 1.399 |
15 | 7.288 | 21.98 | 617.6 | 4.705 | 514.7 | 145.6 | 1.331 | 2.338 | 0.1741 | 2.908 | 24.92 | 9.519 | 1.111 | 5.193 | 1.424 |
25 | 10.03 | 19.71 | 602.9 | 4.781 | 485.7 | 131.8 | 1.297 | 2.499 | 0.1279 | 3.104 | 26.16 | 9.834 | 1.167 | 5.466 | 1.456 |
35 | 13.51 | 17.49 | 587.5 | 4.873 | 457.4 | 119.6 | 1.275 | 2.688 | 0.0956 | 3.333 | 27.58 | 10.16 | 1.228 | 5.826 | 1.497 |
45 | 17.82 | 15.32 | 571.3 | 4.993 | 429.6 | 108.8 | 1.264 | 3.006 | 0.0726 | 3.604 | 29.21 | 10.5 | 1.295 | 6.295 | 1.549 |
55 | 23.1 | 13.2 | 554.1 | 5.143 | 402.3 | 98.99 | 1.265 | 3.335 | 0.0557 | 3.93 | 31.11 | 10.86 | 1.372 | 6.912 | 1.615 |
65 | 29.48 | 11.14 | 535.8 | 5.34 | 375.4 | 90.06 | 1.281 | 3.768 | 0.0432 | 4.334 | 33.33 | 11.25 | 1.463 | 7.738 | 1.702 |
75 | 37.09 | 9.154 | 516.1 | 5.608 | 348.6 | 81.83 | 1.316 | 4.359 | 0.0336 | 4.851 | 35.97 | 11.7 | 1.578 | 8.876 | 1.819 |
85 | 46.09 | 7.24 | 494.5 | 5.987 | 322 | 74.18 | 1.379 | 5.21 | 0.0262 | 5.55 | 39.21 | 12.23 | 1.732 | 10.52 | 1.983 |
95 | 56.65 | 5.414 | 470.2 | 6.56 | 294.6 | 66.84 | 1.489 | 6.525 | 0.0203 | 6.56 | 43.31 | 12.9 | 1.954 | 13.05 | 2.227 |
105 | 68.95 | 3.695 | 442.1 | 7.52 | 266.1 | 59.7 | 1.687 | 8.801 | 0.0156 | 8.168 | 48.83 | 13.82 | 2.312 | 17.35 | 2.622 |
115 | 83.22 | 2.113 | 407.4 | 9.492 | 235 | 52.35 | 2.114 | 13.67 | 0.0116 | 11.14 | 56.96 | 15.22 | 2.977 | 26.03 | 3.358 |
125 | 99.7 | 0.7327 | 357.8 | 16.29 | 196.6 | 43.8 | 3.629 | 31.43 | 0.0082 | 18.25 | 71.25 | 17.84 | 4.57 | 50.81 | 5.121 |
127.5 | 104.2 | 0.437 | 338.7 | 21.71 | 183.4 | 40.94 | 4.848 | 46.11 | 0.0074 | 21.75 | 76.35 | 18.82 | 5.363 | 65.59 | 6.022 |
130 | 108.9 | 0.1754 | 310.5 | 34.41 | 165.1 | 37.05 | 7.72 | 81.46 | 0.0065 | 26.74 | 84.63 | 20.44 | 6.457 | 90.37 | 7.258 |
132.2 | 113.1 | 0.0017 | 248.5 | 64.71 | 129.5 | 29.55 | 14.77 | 168.7 | 0.0055 | 32.93 | 97.33 | 22.96 | 7.77 | 127.8 | 8.808 |
T, temperature (°C); P, pressure (bar); σ, surface tension (mN/m); ρ, density (kg/m3); cp, specific heat (kJ/kg K); k, thermal conductivity (mW/m K); μ, dynamic viscosity (μPa s); Pr, Prandtl number; β, volumetric expansion coefficient (mK− 1); v, specific volume (m3/kg); γ, isentropic expansion coefficient of saturated vapor; indices: L, liquid; V, vapor.
Table B.10
Standard Chemical Exergy of Some Elements
Element | B | C | Ca | Cl2 | Cu | F2 | Fe | H2 | I2 | K | Mg |
exch (kJ/mol) | 628.1 | 410.27 | 729.1 | 123.7 | 132.6 | 505.8 | 374.3 | 236.12 | 175.7 | 336.7 | 626.9 |
Element | Mo | N2 | Na | Ni | O2 | P | Pb | Pt | Pu | Si | Ti |
exch (kJ/mol | 731.3 | 0.67 | 336.7 | 242.6 | 3.92 | 861.3 | 249.2 | 141.2 | 1100 | 855.0 | 907.2 |
Source: Rivero R., Garfias M., Standard chemical exergy of elements updated. Energy 31:3310-3326.
Table B.11
Formation Enthalpy, Entropy, Gibbs Energy, and Chemical Exergy of Some Substances
Substance name | Chemical formula | M | ΔfH0 | ΔfS0 | ΔfG0 | exch |
Acetone | C3H6O | 59 | − 217.14 | 295.6 | − 152.69 | 1788 |
Acetylene | C2H2 | 26 | 228.19 | 200.9 | 210.67 | 1267 |
Ammonia | NH3 | 17 | − 46.14 | 99.5 | − 16.5 | 337.9 |
n-Butane | C4H10 | 58 | − 125.78 | 309.90 | − 16.529 | 2805 |
Calcium carbonate | CaCO3 | 100.1 | − 1207 | 91.7 | − 1128 | 17.52 |
Carbon monoxide | CO | 28 | − 110.53 | 197.6 | − 137.17 | 275.06 |
Carbon dioxide | CO2 | 44 | − 393.49 | 213.8 | − 394.35 | 198.38 |
Copper oxychloride | Cu2OCl2 | 214 | − 384.65 | 154.35 | − 369.7 | 21.08 |
Cupric oxide | CuO | 79 | − 156.06 | 42.59 | − 128.29 | 6.27 |
Copper(II) chloride | CuCl2 | 134 | − 218.0 | 108.07 | − 173.83 | 82.47 |
Cuprous chloride | CuCl | 100 | − 136.82 | 87.45 | − 119.44 | 75.00 |
Ethanol | C2H5OH | 47 | − 234.94 | 280.60 | − 167.71 | 1363 |
Iron(III) oxide | Fe2O3 | 159.7 | − 824.20 | 205.1 | − 742.22 | 12.26 |
Lithium bromide | LiBr | 86.85 | − 351.14 | 74.01 | − 341.83 | 101.37 |
Magnetite | Fe3O4 | 231.5 | − 1118 | 146.1 | − 1015 | 115.61 |
Methane | CH4 | 16 | − 74.60 | 186.40 | − 50.53 | 831.98 |
Nitrogen dioxide | NO2 | 46 | 34.19 | 240.20 | 52.31 | 56.56 |
Nitrous oxide | N2O | 44 | 81.59 | 220.00 | 103.71 | 106.34 |
n-Octane | C8H18 | 131 | − 208.74 | 5.734 | 16.25 | 7549 |
Propane | C3H2 | 44 | − 104.67 | 130.7 | − 24.29 | 2151 |
Sodium chloride | NaCl | 58.44 | − 411.24 | 223.1 | − 384.20 | 14.353 |
Sulphur dioxide | SO2 | 64 | − 296.79 | 248.2 | − 300.0 | 313.10 |
Uranium hexafluoride | UF6 | 352 | − 2198 | 227.8 | − 2069 | 644.96 |
Water | H2O | 18 | − 285.81 | 69.94 | − 237.12 | 0.750 |
M, molecular mass (kg/kmol); ΔfH0, formation enthalpy (kJ/mol); formation entropy, ΔfS0 = s0 − ∑ elements, J/mol K, where ν is the number of moles of the element in chemical equation of formation of the substance; Gibbs free energy of formation, ΔfG0 = ΔfH0 − T0ΔfS0, (kJ/mol); chemical exergy, exch = ΔfG0 + ∑ elementsν × , (kJ/mol); reference temperature, T0 = 298.15 K; reference pressure, P0 = 1 bar; superscript 0 in above notations refers to standard pressure.