Propane detonation properties from Eric Schultz STANJAN, ZND, and CVE (Konnov 1998 mechanism) Caltech, 6/8/00 Schultz E, Shepherd JE (1999) Validation of detailed reaction mechanisms for detonation simulation. Graduate Aeronautical Laboratories of the California Institute of Technology, Technical Report FM99-5. Propane-Oxygen, varying equivalence ratio f diluent P1 T1 g1 a1 W1 h1 VCJ PCJ TCJ aCJ gCJ WCJ hCJ MCJ uvN PvN TvN avN gvN Cp,vN Dh0 Q=Dh0/R1T1 D t E/R q=E/RTvN (%) (bar) (K) (m/s) (kg/kmol) (J/kg) (m/s) (bar) (K) (m/s) (kg/kmol) (J/kg) (m/s) (bar) (K) (m/s) (J/kgK) (MJ/kg) (mm) (ms) (K) 0.2 0.0 1.0 295 1.369 321.6 32.464 -126010 1692 17.9 2780 937.3 1.180 30.829 866900 5.263 1437 33.2 1479 685.2 1.240 1327 3.645 48.2 0.542 1.945 20043 13.552 0.4 0.0 1.0 295 1.344 316.5 32.895 -236910 1958 24.6 3368 1060.5 1.170 28.235 1117000 6.184 1710 45.9 1710 719.3 1.200 1535 5.198 69.7 0.091 0.328 17995 10.523 0.6 0.0 1.0 295 1.323 312.2 33.295 -337320 2123 29.2 3611 1145.4 1.190 25.886 1261000 6.802 1887 55.4 1816 728.5 1.170 1718 5.398 73.3 0.050 0.187 17803 9.803 0.8 0.0 1.0 295 1.306 308.4 33.668 -428660 2253 33.2 3749 1213.8 1.210 23.957 1373000 7.306 2028 63.7 1884 731.7 1.150 1882 5.434 74.6 0.037 0.139 18042 9.576 1.0 0.0 1.0 295 1.291 305.1 34.015 -512110 2361 36.7 3829 1271.0 1.220 22.362 1466000 7.736 2144 71.2 1930 732.3 1.140 2030 5.657 78.5 0.030 0.117 18412 9.540 1.2 0.0 1.0 295 1.279 302.2 34.340 -588650 2449 39.8 3864 1318.8 1.220 21.013 1541000 8.103 2240 77.8 1960 730.9 1.130 2165 6.085 85.2 0.027 0.107 18772 9.577 1.4 0.0 1.0 295 1.269 299.7 34.645 -659090 2520 42.3 3856 1358.0 1.210 19.844 1593000 8.408 2317 83.5 1975 727.7 1.120 2288 6.778 95.7 0.026 0.104 19128 9.685 1.6 0.0 1.0 295 1.259 297.3 34.932 -724150 2571 44.3 3801 1388.5 1.200 18.811 1617000 8.648 2375 88.0 1975 722.5 1.110 2399 7.441 106.0 0.026 0.109 19391 9.818 1.8 0.0 1.0 295 1.251 295.2 35.201 -784410 2602 45.5 3697 1410.5 1.190 17.884 1606000 8.814 2412 91.1 1959 714.9 1.100 2496 8.054 115.6 0.029 0.124 19511 9.960 2.0 0.0 1.0 295 1.244 293.3 35.455 -840390 2612 45.9 3547 1423.4 1.190 17.049 1559000 8.906 2428 92.7 1927 704.9 1.100 2581 8.098 117.1 0.036 0.154 19546 10.143 2.2 0.0 1.0 295 1.237 291.5 35.695 -892530 2603 45.5 3362 1427.6 1.200 16.294 1476000 8.928 2424 92.8 1880 692.8 1.100 2653 7.576 110.3 0.047 0.209 19219 10.223 2.4 0.0 1.0 295 1.231 290.0 35.923 -941200 2576 44.5 3151 1423.2 1.220 15.611 1363000 8.883 2402 91.6 1821 678.8 1.090 2712 6.649 97.4 0.067 0.304 18692 10.265 2.6 0.0 1.0 295 1.226 288.5 36.138 -986760 2532 42.8 2918 1410.9 1.230 14.988 1222000 8.776 2363 89.1 1751 663.0 1.090 2758 6.079 89.6 0.103 0.475 17858 10.199 2.8 0.0 1.0 295 1.221 287.1 36.342 -102950 2471 40.6 2671 1389.4 1.260 14.420 1057000 8.606 2307 85.5 1672 645.6 1.090 2790 5.008 74.2 0.167 0.793 16695 9.985 3.0 0.0 1.0 295 1.217 285.8 36.536 -106960 2394 38.0 2417 1358.2 1.280 13.904 874700 8.378 2235 80.7 1585 626.6 1.090 2807 4.288 63.9 0.285 1.391 15237 9.613 Propane-Air, varying equivalence ratio Konnov (1998) f diluent P1 T1 g1 a1 W1 h1 VCJ PCJ TCJ aCJ gCJ WCJ hCJ MCJ uvN PvN TvN avN gvN Cp,vN Dh0 Q=Dh0/R1T1 D t E/R q=E/RTvN (%) (bar) (K) (m/s) (kg/kmol) (J/kg) (m/s) (bar) (K) (m/s) (kg/kmol) (J/kg) (m/s) (bar) (K) (m/s) (J/kgK) (MJ/kg) (mm) (ms) (K) 0.2 78.3 1.0 295 1.396 343.7 28.978 -33065 1091 6.5 1159 663.6 1.310 28.738 342400 3.175 834 11.7 819 560.2 1.340 1142 0.742 8.8 134900.00515400.00 21708 26.505 0.4 77.7 1.0 295 1.389 342.1 29.103 -62201 1388 10.5 1782 810.9 1.270 28.628 572800 4.058 1119 19.4 1112 642.3 1.300 1244 1.498 17.8 173.000 604.800 17455 15.697 0.6 77.0 1.0 295 1.382 340.5 29.226 -90616 1588 13.9 2280 905.7 1.230 28.488 759300 4.662 1312 25.8 1324 692.7 1.270 1321 2.404 28.6 13.340 45.040 18124 13.689 0.8 76.4 1.0 295 1.375 339.0 29.346 -118340 1722 16.7 2638 961.5 1.190 28.201 901600 5.078 1444 30.7 1465 722.4 1.260 1386 3.545 42.4 3.637 12.080 19131 13.059 1.0 75.8 1.0 295 1.370 337.7 29.465 -145390 1801 18.5 2822 994.3 1.170 27.670 982100 5.334 1524 34.0 1541 735.5 1.240 1438 4.402 52.9 2.072 6.847 19526 12.671 1.2 75.2 1.0 295 1.364 336.3 29.582 -171790 1836 19.1 2845 1018.7 1.190 26.931 994500 5.460 1563 35.6 1561 735.9 1.230 1482 4.027 48.6 1.889 6.283 19536 12.515 1.4 74.6 1.0 295 1.358 334.9 29.698 -197580 1834 18.8 2741 1031.7 1.220 26.067 952000 5.477 1567 35.8 1538 726.7 1.230 1516 3.386 41.0 2.427 8.196 19094 12.415 1.6 74.0 1.0 295 1.353 333.6 29.811 -222760 1813 18.3 2587 1029.5 1.240 25.195 891300 5.435 1553 35.2 1494 713.0 1.220 1545 2.980 36.2 3.629 12.520 18265 12.226 1.8 73.4 1.0 295 1.348 332.4 29.923 -247370 1785 17.7 2425 1019.6 1.260 24.374 825700 5.370 1530 34.3 1443 698.0 1.220 1569 2.619 32.0 5.674 20.010 17165 11.895 2.0 72.9 1.0 295 1.343 331.2 30.033 -271410 1752 17.0 2265 1005.7 1.270 23.613 757500 5.289 1504 33.3 1390 682.7 1.210 1590 2.403 29.4 8.958 32.260 15833 11.390 2.2 72.3 1.0 295 1.338 330.0 30.141 -294910 1716 16.3 2109 989.1 1.280 22.910 687400 5.198 1473 32.1 1337 667.1 1.210 1608 2.195 27.0 14.080 51.650 14322 10.712 2.4 71.8 1.0 295 1.333 328.8 30.247 -317890 1676 15.6 1958 970.2 1.290 22.259 615400 5.096 1439 30.7 1282 651.4 1.200 1623 1.997 24.6 21.800 81.400 12726 9.927 2.6 71.2 1.0 295 1.329 327.7 30.352 -340360 1633 14.8 1812 949.2 1.300 21.656 541700 4.981 1401 29.3 1227 635.4 1.200 1634 1.808 22.4 32.920 125.300 11369 9.266 2.8 70.7 1.0 295 1.326 326.7 30.456 -362350 1586 14.0 1670 926.2 1.300 21.097 466300 4.854 1359 27.8 1171 619.2 1.200 1643 1.694 21.0 49.450 191.100 10655 9.099 3.0 70.1 1.0 295 1.321 325.7 30.557 -383860 1536 13.1 1531 901.4 1.310 20.576 389000 4.715 1314 26.1 1114 602.7 1.200 1646 1.510 18.8 76.020 298.800 11059 9.928 Propane-Oxygen, varying initial pressure Konnov (1998) f diluent P1 T1 g1 a1 W1 h1 VCJ PCJ TCJ aCJ gCJ WCJ hCJ MCJ uvN PvN TvN avN gvN Cp,vN Dh0 Q=Dh0/R1T1 D t E/R q=E/RTvN (%) (bar) (K) (m/s) (kg/kmol) (J/kg) (m/s) (bar) (K) (m/s) (kg/kmol) (J/kg) (m/s) (bar) (K) (m/s) (J/kgK) (MJ/kg) (mm) (ms) (K) 1.0 0.0 0.2 295 1.291 305.1 34.015 -512110 2288 6.9 3526 1228.1 1.220 21.876 1351000 7.498 2074 13.3 1846 716.7 1.140 2012 5.312 73.7 0.166 0.647 19420 10.520 1.0 0.0 0.4 295 1.291 305.1 34.015 -512110 2319 14.2 3653 1246.6 1.220 22.076 1400000 7.600 2104 27.5 1882 723.4 1.140 2020 5.460 75.7 0.080 0.311 19060 10.128 1.0 0.0 0.6 295 1.291 305.1 34.015 -512110 2337 21.6 3730 1257.3 1.220 22.199 1429000 7.660 2121 41.8 1903 727.3 1.140 2024 5.548 76.9 0.052 0.203 18780 9.869 1.0 0.0 0.8 295 1.291 305.1 34.015 -512110 2351 29.1 3785 1265.0 1.220 22.290 1450000 7.703 2134 56.5 1918 730.1 1.140 2027 5.608 77.8 0.038 0.149 18560 9.677 1.0 0.0 1.0 295 1.291 305.1 34.015 -512110 2361 36.7 3829 1271.0 1.220 22.362 1466000 7.736 2144 71.2 1930 732.3 1.140 2030 5.657 78.5 0.030 0.117 18410 9.539 1.0 0.0 1.2 295 1.291 305.1 34.015 -512110 2369 44.3 3865 1275.9 1.220 22.422 1480000 7.763 2152 86.0 1939 734.0 1.140 2032 5.696 79.0 0.025 0.096 18260 9.417 1.0 0.0 1.4 295 1.291 305.1 34.015 -512110 2376 52.0 3896 1280.1 1.220 22.473 1491000 7.786 2158 101.0 1947 735.5 1.140 2033 5.730 79.5 0.021 0.082 18150 9.322 1.0 0.0 1.6 295 1.291 305.1 34.015 -512110 2382 59.6 3923 1283.9 1.220 22.519 1500000 7.806 2164 116.0 1954 736.8 1.140 2035 5.759 79.9 0.018 0.071 18050 9.237 1.0 0.0 1.8 295 1.291 305.1 34.015 -512110 2387 67.3 3948 1287.1 1.220 22.559 1509000 7.824 2169 131.0 1960 737.9 1.140 2036 5.787 80.3 0.016 0.062 17970 9.168 1.0 0.0 2.0 295 1.291 305.1 34.015 -512110 2392 75.1 3969 1289.9 1.220 22.596 1517000 7.839 2174 146.0 1966 739.0 1.140 2037 5.809 80.6 0.014 0.056 17930 9.120 Propane-Air, varying initial pressure Konnov (1998) f diluent P1 T1 g1 a1 W1 h1 VCJ PCJ TCJ aCJ gCJ WCJ hCJ MCJ uvN PvN TvN avN gvN Cp,vN Dh0 Q=Dh0/R1T1 D t E/R q=E/RTvN (%) (bar) (K) (m/s) (kg/kmol) (J/kg) (m/s) (bar) (K) (m/s) (kg/kmol) (J/kg) (m/s) (bar) (K) (m/s) (J/kgK) (MJ/kg) (mm) (ms) (K) 1.0 75.8 0.2 295 1.370 337.7 29.465 -145390 1772 3.6 2721 974.3 1.160 27.499 949200 5.247 1497 6.6 1505 727.1 1.250 1432 4.564 54.8 9.009 30.300 21310 14.159 1.0 75.8 0.4 295 1.370 337.7 29.465 -145390 1785 7.3 2766 983.2 1.170 27.574 963800 5.286 1509 13.3 1521 730.8 1.240 1435 4.327 52.0 4.823 16.130 20710 13.616 1.0 75.8 0.6 295 1.370 337.7 29.465 -145390 1792 11.0 2791 988.2 1.170 27.617 972000 5.307 1516 20.2 1530 732.9 1.240 1437 4.360 52.4 3.332 11.090 20220 13.216 1.0 75.8 0.8 295 1.370 337.7 29.465 -145390 1797 14.7 2809 991.6 1.170 27.647 977800 5.322 1521 27.1 1536 734.3 1.240 1438 4.385 52.7 2.551 8.460 19840 12.917 1.0 75.8 1.0 295 1.370 337.7 29.465 -145390 1801 18.5 2822 994.3 1.170 27.670 982100 5.334 1524 34.0 1541 735.5 1.240 1438 4.402 52.9 2.071 6.845 19530 12.674 1.0 75.8 1.2 295 1.370 337.7 29.465 -145390 1804 22.2 2833 996.4 1.180 27.688 985600 5.343 1527 40.9 1545 736.3 1.240 1439 4.143 49.8 1.745 5.751 19260 12.466 1.0 75.8 1.4 295 1.370 337.7 29.465 -145390 1807 26.0 2842 998.3 1.180 27.703 988400 5.351 1530 47.9 1548 737.1 1.240 1440 4.154 49.9 1.507 4.956 19040 12.300 1.0 75.8 1.6 295 1.370 337.7 29.465 -145390 1809 29.7 2850 999.8 1.180 27.716 990900 5.357 1532 54.8 1551 737.7 1.240 1440 4.164 50.0 1.328 4.357 18850 12.153 1.0 75.8 1.8 295 1.370 337.7 29.465 -145390 1811 33.5 2857 1001.2 1.180 27.728 993000 5.363 1533 61.8 1553 738.3 1.240 1440 4.173 50.1 1.186 3.883 18680 12.028 1.0 75.8 2.0 295 1.370 337.7 29.465 -145390 1813 37.3 2863 1002.4 1.180 27.738 994900 5.368 1535 68.9 1555 738.7 1.240 1441 4.181 50.2 1.072 3.505 18540 11.923 Propane-Oxygen-Argon, varying argon dilution Konnov (1998) f diluent P1 T1 g1 a1 W1 h1 VCJ PCJ TCJ aCJ gCJ WCJ hCJ MCJ uvN PvN TvN avN gvN Cp,vN Dh0 Q=Dh0/R1T1 D t E/R q=E/RTvN (%) (bar) (K) (m/s) (kg/kmol) (J/kg) (m/s) (bar) (K) (m/s) (kg/kmol) (J/kg) (m/s) (bar) (K) (m/s) (J/kgK) (MJ/kg) (mm) (ms) (K) 1.0 0.0 1.0 295 1.291 305.1 34.015 -512110 2361 36.7 3829 1271.0 1.220 22.362 1466000 7.736 2144 71.2 1930 732.3 1.140 2030 5.657 78.5 0.030 0.117 18412 9.540 1.0 10.0 1.0 295 1.310 304.6 34.611 -452930 2286 35.0 3795 1232.6 1.220 23.612 1399000 7.503 2061 67.5 1954 734.2 1.150 1859 5.313 75.0 0.031 0.119 18587 9.512 1.0 20.0 1.0 295 1.329 304.3 35.201 -396260 2211 33.2 3756 1194.3 1.210 24.951 1334000 7.264 1978 63.7 1981 737.4 1.160 1696 5.244 75.3 0.033 0.120 18771 9.476 1.0 30.0 1.0 295 1.353 304.4 35.793 -341280 2134 31.5 3710 1155.6 1.210 26.408 1269000 7.011 1891 59.9 2011 741.9 1.180 1536 4.896 71.5 0.034 0.121 18929 9.412 1.0 40.0 1.0 295 1.379 304.8 36.387 -287960 2056 29.7 3655 1116.3 1.200 27.996 1203000 6.745 1801 55.9 2045 748.2 1.200 1381 4.805 71.3 0.036 0.123 19089 9.334 1.0 50.0 1.0 295 1.409 305.7 36.980 -236420 1975 27.8 3588 1076.0 1.200 29.729 1135000 6.460 1706 51.8 2080 756.6 1.220 1229 4.444 67.0 0.038 0.126 19160 9.212 1.0 60.0 1.0 295 1.445 307.1 37.572 -186500 1889 25.7 3500 1034.2 1.200 31.628 1063000 6.152 1603 47.4 2116 767.3 1.260 1082 4.076 62.4 0.042 0.134 19134 9.043 1.0 70.0 1.0 295 1.489 309.3 38.165 -138130 1795 23.5 3375 989.8 1.200 33.712 982700 5.803 1488 42.6 2146 780.5 1.300 937 3.687 57.4 0.050 0.151 19151 8.924 1.0 80.0 1.0 295 1.540 312.2 38.758 -91241 1681 20.7 3168 940.0 1.220 35.993 879700 5.385 1349 36.8 2147 794.2 1.370 795 2.911 46.0 0.074 0.209 19063 8.879 1.0 90.0 1.0 295 1.605 316.3 39.351 -45766 1494 15.8 2668 874.3 1.330 38.382 687300 4.721 1138 28.3 1985 787.7 1.480 652 1.433 23.0 0.299 0.795 20535 10.345 Propane-Oxygen-Carbon Dioxide, varying carbon dioxide dilution Konnov (1998) f diluent P1 T1 g1 a1 W1 h1 VCJ PCJ TCJ aCJ gCJ WCJ hCJ MCJ uvN PvN TvN avN gvN Cp,vN Dh0 Q=Dh0/R1T1 D t E/R q=E/RTvN (%) (bar) (K) (m/s) (kg/kmol) (J/kg) (m/s) (bar) (K) (m/s) (kg/kmol) (J/kg) (m/s) (bar) (K) (m/s) (J/kgK) (MJ/kg) (mm) (ms) (K) 1.0 0.0 1.0 295 1.291 305.1 34.015 -512110 2361 36.7 3829 1271.0 1.220 22.362 1466000 7.736 2144 71.2 1930 732.3 1.140 2030 5.657 78.5 0.030 0.117 18412 9.540 1.0 10.0 1.0 295 1.291 300.7 35.019 -157660 2224 33.6 3684 1196.8 1.200 24.164 181400 7.398 2013 64.9 1820 702.0 1.140 1924 5.581 79.7 0.056 0.227 18285 10.047 1.0 20.0 1.0 295 1.291 296.5 36.014 -257290 2092 30.7 3530 1124.9 1.190 26.101 -1017000 7.056 1886 59.0 1710 672.3 1.140 1824 5.221 76.7 0.113 0.477 18015 10.535 1.0 30.0 1.0 295 1.291 292.4 37.012 -351880 1961 27.8 3366 1054.3 1.170 28.213 -2151000 6.707 1761 53.1 1600 642.6 1.150 1729 5.189 78.3 0.253 1.112 17601 11.001 1.0 40.0 1.0 295 1.290 288.5 38.013 -441700 1831 25.0 3187 984.8 1.160 30.513 -3225000 6.349 1637 47.5 1488 612.8 1.150 1639 4.835 74.9 0.643 2.942 17034 11.448 1.0 50.0 1.0 295 1.290 284.8 39.013 -526820 1701 22.2 2987 915.7 1.140 32.995 -4241000 5.972 1512 41.9 1374 582.5 1.160 1553 4.832 76.9 1.922 9.166 16396 11.933 1.0 60.0 1.0 295 1.289 281.1 40.012 -607680 1565 19.4 2748 845.4 1.130 35.629 -5210000 5.566 1382 36.3 1253 550.7 1.160 1470 4.439 72.4 7.353 36.550 15818 12.624 1.0 70.0 1.0 295 1.289 277.7 41.012 -684610 1413 16.2 2430 770.0 1.130 38.280 -6144000 5.090 1236 30.2 1117 515.1 1.170 1386 3.620 60.5 44.340 231.300 15853 14.193 1.0 80.0 1.0 295 1.289 274.3 42.011 -757870 1215 12.2 1937 676.1 1.150 40.566 -7069000 4.431 1045 22.8 940 468.9 1.180 1290 2.273 38.9 1106.000 6230.000 19871 21.139 Propane-Oxygen-Helium, varying helium dilution Konnov (1998) f diluent P1 T1 g1 a1 W1 h1 VCJ PCJ TCJ aCJ gCJ WCJ hCJ MCJ uvN PvN TvN avN gvN Cp,vN Dh0 Q=Dh0/R1T1 D t E/R q=E/RTvN (%) (bar) (K) (m/s) (kg/kmol) (J/kg) (m/s) (bar) (K) (m/s) (kg/kmol) (J/kg) (m/s) (bar) (K) (m/s) (J/kgK) (MJ/kg) (mm) (ms) (K) 1.0 0.0 1.0 295 1.291 305.1 34.015 -512110 2361 36.7 3829 1271.0 1.220 22.362 1466000 7.736 2144 71.2 1930 732.3 1.140 2030 5.657 78.5 0.030 0.117 18412 9.540 1.0 10.0 1.0 295 1.309 321.8 31.000 -505680 2415 35.0 3795 1302.4 1.220 21.149 1562000 7.505 2178 67.5 1954 775.8 1.150 2076 5.932 75.0 0.033 0.119 18558 9.498 1.0 20.0 1.0 295 1.329 341.1 28.013 -497940 2478 33.2 3756 1338.8 1.210 19.856 1676000 7.265 2217 63.8 1981 826.6 1.160 2131 6.589 75.3 0.036 0.120 18695 9.437 1.0 30.0 1.0 295 1.352 364.1 25.015 -488320 2553 31.5 3710 1382.4 1.210 18.456 1815000 7.011 2262 59.9 2011 887.5 1.180 2198 7.006 71.5 0.040 0.121 18879 9.388 1.0 40.0 1.0 295 1.378 391.9 22.010 -476050 2644 29.7 3655 1435.3 1.200 16.935 1988000 6.745 2316 55.9 2045 962.0 1.200 2282 7.943 71.3 0.046 0.123 18984 9.283 1.0 50.0 1.0 295 1.409 426.4 19.009 -459920 2755 27.8 3588 1500.7 1.200 15.282 2208000 6.460 2380 51.8 2080 1055.3 1.220 2391 8.645 67.0 0.053 0.126 19138 9.201 1.0 60.0 1.0 295 1.445 470.5 16.008 -437740 2894 25.7 3500 1584.4 1.200 13.475 2496000 6.151 2456 47.4 2116 1175.5 1.260 2540 9.567 62.4 0.065 0.133 19100 9.026 1.0 70.0 1.0 295 1.488 529.7 13.006 -405320 3075 23.5 3375 1695.5 1.200 11.489 2884000 5.804 2549 42.6 2146 1337.0 1.300 2751 10.818 57.4 0.086 0.151 18910 8.812 1.0 80.0 1.0 295 1.540 614.5 10.005 -353450 3308 20.7 3168 1850.0 1.220 9.291 3408000 5.384 2655 36.8 2147 1563.0 1.370 3080 11.279 46.0 0.145 0.208 19056 8.876 1.0 90.0 1.0 295 1.605 749.8 7.004 -257130 3540 15.8 2668 2072.3 1.330 6.831 3862000 4.722 2697 28.3 1985 1867.0 1.480 3664 8.052 23.0 0.709 0.794 20612 10.384 Propane-Oxygen-Nitrogen, varying nitrogen dilution Konnov (1998) f diluent P1 T1 g1 a1 W1 h1 VCJ PCJ TCJ aCJ gCJ WCJ hCJ MCJ uvN PvN TvN avN gvN Cp,vN Dh0 Q=Dh0/R1T1 D t E/R q=E/RTvN (%) (bar) (K) (m/s) (kg/kmol) (J/kg) (m/s) (bar) (K) (m/s) (kg/kmol) (J/kg) (m/s) (bar) (K) (m/s) (J/kgK) (MJ/kg) (mm) (ms) (K) 1.0 0.0 1.0 295 1.291 305.1 34.015 -512110 2361 36.7 3829 1271.0 1.220 22.362 1466000 7.736 2144 71.2 1930 732.3 1.140 2030 5.657 78.5 0.030 0.117 18412 9.540 1.0 10.0 1.0 295 1.300 308.9 33.412 -469260 2306 34.4 3760 1241.9 1.210 22.974 1418000 7.465 2082 66.4 1900 735.9 1.150 1961 5.687 77.5 0.040 0.153 18519 9.747 1.0 20.0 1.0 295 1.309 312.8 32.815 -425230 2252 32.3 3691 1214.0 1.200 23.592 1374000 7.201 2021 61.9 1872 740.1 1.150 1892 5.732 76.7 0.054 0.202 18675 9.976 1.0 30.0 1.0 295 1.318 316.7 32.215 -379420 2195 30.1 3611 1184.5 1.190 24.251 1328000 6.930 1956 57.4 1841 744.1 1.170 1819 5.766 75.7 0.076 0.278 18848 10.238 1.0 40.0 1.0 295 1.328 321.0 31.614 -331760 2132 27.9 3515 1152.6 1.180 24.956 1277000 6.643 1885 52.8 1804 747.4 1.180 1744 5.780 74.5 0.114 0.405 19057 10.564 1.0 50.0 1.0 295 1.339 325.4 31.014 -282310 2062 25.6 3396 1117.4 1.170 25.703 1220000 6.338 1807 48.1 1758 749.6 1.190 1664 5.764 72.9 0.187 0.649 19293 10.974 1.0 60.0 1.0 295 1.350 329.9 30.414 -230910 1981 23.2 3239 1077.3 1.170 26.482 1150000 6.004 1716 43.2 1699 749.4 1.210 1581 5.321 66.0 0.358 1.214 19511 11.484 1.0 70.0 1.0 295 1.362 334.8 29.814 -177440 1879 20.4 3014 1029.1 1.170 27.257 1058000 5.612 1606 37.7 1614 743.9 1.230 1493 4.791 58.2 0.916 3.046 19650 12.175 1.0 75.8 1.0 295 1.370 337.7 29.465 -145390 1801 18.5 2822 994.3 1.170 27.670 982100 5.334 1524 34.0 1541 735.5 1.240 1438 4.402 52.9 2.072 6.847 19526 12.671 1.0 80.0 1.0 295 1.375 339.7 29.214 -121770 1728 16.8 2632 963.4 1.190 27.919 907800 5.088 1450 30.8 1468 724.4 1.260 1395 3.574 42.6 4.809 15.900 19150 13.045