Ethylene 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. Ethylene-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 1.383 326.8 31.752 99948 1719 18.1 2896 948.6 1.170 31.130 1128000 5.260 1452 33.3 1529 708.2 1.250 1300 4.019 52.0 0.749 2.709 18078 11.824 0.4 0.0 1.0 295 1.369 326.2 31.535 192010 1974 24.0 3462 1070.2 1.180 28.505 1569000 6.052 1707 44.3 1770 753.9 1.220 1472 4.977 64.0 0.134 0.479 15952 9.013 0.6 0.0 1.0 295 1.356 325.8 31.341 274910 2138 27.8 3704 1155.3 1.210 26.151 1893000 6.563 1876 52.2 1891 774.5 1.200 1622 4.914 62.8 0.066 0.236 15855 8.385 0.8 0.0 1.0 295 1.346 325.5 31.168 349960 2268 31.1 3847 1224.5 1.220 24.230 2172000 6.968 2010 58.9 1975 788.1 1.180 1755 5.248 66.7 0.042 0.152 16102 8.153 1.0 0.0 1.0 295 1.338 325.3 31.013 418230 2376 33.8 3937 1283.3 1.240 22.652 2418000 7.305 2123 64.8 2035 797.9 1.170 1878 5.226 66.1 0.031 0.112 16321 8.020 1.2 0.0 1.0 295 1.330 325.1 30.872 480580 2467 36.2 3989 1333.0 1.240 21.331 2636000 7.590 2218 69.9 2080 805.0 1.160 1989 5.633 70.9 0.024 0.089 16448 7.908 1.4 0.0 1.0 295 1.324 325.0 30.744 537760 2543 38.2 4008 1374.7 1.240 20.202 2827000 7.826 2298 74.3 2112 809.9 1.150 2090 5.985 75.0 0.021 0.076 16496 7.811 1.6 0.0 1.0 295 1.318 324.9 30.627 590390 2604 39.8 3993 1410.0 1.230 19.222 2987000 8.016 2363 77.8 2130 812.6 1.140 2181 6.576 82.1 0.019 0.069 16444 7.720 1.8 0.0 1.0 295 1.312 324.8 30.519 638980 2650 41.0 3945 1438.2 1.220 18.359 3117000 8.161 2412 80.6 2134 813.1 1.140 2263 7.147 88.9 0.018 0.066 16227 7.604 2.0 0.0 1.0 295 1.308 324.8 30.421 683990 2682 41.7 3867 1459.2 1.210 17.592 3215000 8.257 2447 82.4 2126 811.3 1.130 2336 7.698 95.5 0.018 0.066 15948 7.501 2.2 0.0 1.0 295 1.303 324.7 30.330 725800 2699 41.9 3761 1474.0 1.210 16.908 3281000 8.312 2468 83.4 2106 807.3 1.130 2402 7.786 96.3 0.018 0.069 15559 7.388 2.4 0.0 1.0 295 1.300 324.7 30.246 764730 2703 41.7 3634 1482.9 1.210 16.294 3319000 8.327 2476 83.5 2076 801.6 1.130 2459 7.800 96.2 0.019 0.075 15032 7.241 2.6 0.0 1.0 295 1.296 324.7 30.167 801080 2697 41.2 3493 1486.3 1.220 15.743 3334000 8.308 2473 83.0 2038 794.4 1.120 2510 7.362 90.5 0.021 0.083 14444 7.087 2.8 0.0 1.0 295 1.294 324.8 30.094 835090 2682 40.4 3341 1485.3 1.220 15.245 3328000 8.258 2461 82.0 1994 785.9 1.120 2555 7.261 89.1 0.023 0.094 13802 6.922 3.0 0.0 1.0 295 1.291 324.8 30.026 866990 2657 39.3 3183 1478.9 1.230 14.805 3304000 8.181 2439 80.3 1943 776.1 1.120 2594 6.767 82.8 0.027 0.109 13481 6.938 Ethylene-Air, 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 77.9 1.0 295 1.399 345.0 28.839 21841 1119 6.8 1216 677.6 1.310 28.839 418700 3.244 858 12.3 846 571.1 1.340 1144 0.787 9.3 121700.00460000.00 20203 23.881 0.4 76.8 1.0 295 1.395 344.5 28.828 46200 1423 11.0 1880 828.4 1.270 28.825 716500 4.131 1147 20.2 1155 658.9 1.300 1241 1.582 18.6 149.000 528.100 20888 18.085 0.6 75.8 1.0 295 1.391 344.1 28.817 69922 1623 14.4 2402 921.4 1.220 28.753 962900 4.716 1337 26.5 1375 713.4 1.280 1308 2.656 31.2 7.271 24.480 21243 15.449 0.8 74.8 1.0 295 1.387 343.7 28.807 93030 1749 17.0 2748 972.6 1.180 28.463 1151000 5.090 1460 31.0 1514 744.5 1.270 1362 3.901 45.8 1.799 5.871 18814 12.427 1.0 73.8 1.0 295 1.384 343.3 28.798 115550 1824 18.5 2924 1005.3 1.170 27.930 1275000 5.314 1534 33.9 1589 759.9 1.260 1405 4.528 53.2 0.963 3.096 17196 10.822 1.2 72.9 1.0 295 1.381 343.0 28.788 137500 1868 19.3 2982 1031.1 1.180 27.253 1351000 5.445 1579 35.6 1624 765.8 1.250 1443 4.447 52.2 0.724 2.314 16373 10.082 1.4 71.9 1.0 295 1.377 342.6 28.779 158910 1886 19.5 2949 1050.8 1.200 26.494 1387000 5.506 1601 36.4 1628 764.8 1.240 1475 4.017 47.1 0.665 2.131 16336 10.035 1.6 71.0 1.0 295 1.374 342.3 28.769 179790 1887 19.3 2857 1061.3 1.220 25.710 1397000 5.512 1605 36.5 1609 758.8 1.240 1503 3.594 42.2 0.703 2.274 16977 10.552 1.8 70.1 1.0 295 1.372 342.0 28.761 200160 1877 18.9 2741 1063.6 1.240 24.950 1397000 5.488 1599 36.2 1579 750.4 1.230 1529 3.209 37.6 0.809 2.652 18020 11.412 2.0 69.3 1.0 295 1.369 341.7 28.752 220050 1862 18.5 2619 1061.0 1.250 24.234 1392000 5.450 1589 35.7 1545 741.0 1.230 1552 3.004 35.2 0.983 3.280 19214 12.436 2.2 68.4 1.0 295 1.366 341.4 28.743 239460 1844 18.0 2497 1055.4 1.270 23.566 1384000 5.401 1575 35.0 1508 731.1 1.230 1574 2.684 31.5 1.256 4.279 20440 13.554 2.4 67.6 1.0 295 1.363 341.1 28.735 258420 1823 17.6 2377 1047.8 1.280 22.943 1373000 5.345 1558 34.3 1470 721.0 1.220 1593 2.507 29.4 1.686 5.884 21681 14.749 2.6 66.8 1.0 295 1.361 340.8 28.727 276940 1800 17.1 2259 1038.5 1.280 22.363 1359000 5.281 1539 33.4 1431 710.6 1.220 1611 2.435 28.5 2.390 8.553 22678 15.848 2.8 66.0 1.0 295 1.359 340.6 28.719 295040 1775 16.5 2144 1027.6 1.290 21.821 1343000 5.210 1517 32.5 1391 700.0 1.220 1626 2.262 26.5 3.563 13.090 23197 16.676 3.0 65.3 1.0 295 1.356 340.3 28.712 312730 1747 16.0 2033 1015.4 1.300 21.325 1324000 5.134 1494 31.6 1351 689.3 1.210 1640 2.098 24.6 5.533 20.880 23104 17.101 Ethylene-Oxygen, varying initial pressure 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 1.338 325.3 31.013 418230 2299 6.4 3611 1237.3 1.230 22.143 2295000 7.067 2049 12.1 1939 779.3 1.170 1861 5.129 64.9 0.192 0.707 13230 6.823 1.0 0.0 0.4 295 1.338 325.3 31.013 418230 2332 13.1 3747 1256.8 1.230 22.351 2347000 7.169 2081 25.0 1980 787.3 1.170 1868 5.279 66.7 0.087 0.319 14600 7.374 1.0 0.0 0.6 295 1.338 325.3 31.013 418230 2351 19.9 3829 1268.4 1.240 22.479 2378000 7.229 2100 38.0 2005 791.9 1.170 1873 5.117 64.7 0.055 0.200 15370 7.666 1.0 0.0 0.8 295 1.338 325.3 31.013 418230 2365 26.9 3890 1276.8 1.240 22.574 2401000 7.272 2113 51.4 2022 795.3 1.170 1876 5.180 65.5 0.040 0.144 15930 7.878 1.0 0.0 1.0 295 1.338 325.3 31.013 418230 2376 33.8 3937 1283.5 1.240 22.649 2418000 7.306 2123 64.8 2036 797.9 1.170 1878 5.226 66.1 0.031 0.111 16310 8.011 1.0 0.0 1.2 295 1.338 325.3 31.013 418230 2385 40.9 3977 1288.7 1.240 22.712 2432000 7.333 2132 78.3 2047 800.0 1.170 1880 5.267 66.6 0.025 0.090 16660 8.139 1.0 0.0 1.4 295 1.338 325.3 31.013 418230 2393 48.0 4011 1292.7 1.240 22.767 2445000 7.357 2139 92.0 2057 801.9 1.170 1882 5.300 67.0 0.021 0.076 16940 8.235 1.0 0.0 1.6 295 1.338 325.3 31.013 418230 2399 55.1 4040 1296.5 1.240 22.814 2456000 7.376 2145 105.7 2065 803.4 1.170 1883 5.328 67.4 0.018 0.065 17170 8.315 1.0 0.0 1.8 295 1.338 325.3 31.013 418230 2405 62.3 4066 1299.9 1.240 22.856 2465000 7.394 2151 119.5 2072 804.8 1.170 1884 5.353 67.7 0.016 0.057 17360 8.378 1.0 0.0 2.0 295 1.338 325.3 31.013 418230 2410 69.5 4090 1302.9 1.240 22.895 2474000 7.410 2155 133.4 2079 806.0 1.170 1885 5.377 68.0 0.014 0.050 17550 8.442 Ethylene-Air, varying initial pressure 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 73.8 0.2 295 1.384 343.3 28.799 115550 1792 3.6 2808 983.8 1.160 27.729 1237000 5.220 1504 6.5 1548 750.3 1.260 1400 4.680 55.0 3.394 10.830 13530 8.740 1.0 73.8 0.4 295 1.384 343.3 28.799 115550 1807 7.3 2859 993.3 1.170 27.816 1254000 5.262 1518 13.3 1566 754.6 1.260 1402 4.442 52.2 1.907 6.102 14980 9.566 1.0 73.8 0.6 295 1.384 343.3 28.799 115550 1815 11.0 2889 998.7 1.170 27.866 1263000 5.286 1525 20.1 1577 757.0 1.260 1404 4.483 52.6 1.397 4.479 15960 10.120 1.0 73.8 0.8 295 1.384 343.3 28.799 115550 1821 14.8 2909 1002.6 1.170 27.901 1270000 5.303 1531 27.0 1584 758.7 1.260 1405 4.509 52.9 1.127 3.620 16650 10.511 1.0 73.8 1.0 295 1.384 343.3 28.799 115550 1825 18.6 2925 1005.5 1.170 27.928 1275000 5.316 1535 33.9 1590 760.0 1.260 1405 4.530 53.2 0.959 3.081 17170 10.799 1.0 73.8 1.2 295 1.384 343.3 28.799 115550 1828 22.3 2938 1007.9 1.170 27.949 1279000 5.326 1538 40.8 1594 761.0 1.260 1406 4.548 53.4 0.841 2.705 17570 11.023 1.0 73.8 1.4 295 1.384 343.3 28.799 115550 1831 26.1 2949 1009.9 1.170 27.968 1283000 5.335 1541 47.8 1598 761.9 1.260 1406 4.562 53.6 0.752 2.421 17870 11.183 1.0 73.8 1.6 295 1.384 343.3 28.799 115550 1834 29.9 2958 1011.6 1.170 27.983 1285000 5.342 1543 54.8 1601 762.7 1.260 1407 4.574 53.7 0.684 2.201 18090 11.299 1.0 73.8 1.8 295 1.384 343.3 28.799 115550 1836 33.7 2966 1013.1 1.180 27.997 1288000 5.348 1545 61.7 1604 763.3 1.260 1407 4.301 50.5 0.627 2.020 18280 11.397 1.0 73.8 2.0 295 1.384 343.3 28.799 115550 1838 37.6 2973 1014.5 1.180 28.009 1290000 5.354 1547 68.8 1607 763.9 1.260 1408 4.310 50.6 0.581 1.870 18420 11.462 Ethylene-Oxygen-Argon, varying argon dilution 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 1.338 325.3 31.013 418230 2376 33.8 3937 1283.3 1.240 22.652 2418000 7.305 2123 64.8 2035 797.9 1.170 1878 5.226 66.1 0.031 0.112 16321 8.020 1.0 10.0 1.0 295 1.355 322.8 31.898 366120 2296 32.5 3900 1242.2 1.230 23.996 2231000 7.115 2037 61.8 2062 796.3 1.180 1713 5.127 66.7 0.033 0.115 16408 7.957 1.0 20.0 1.0 295 1.375 320.7 32.799 315960 2216 31.1 3856 1200.7 1.220 25.457 2050000 6.910 1948 58.7 2092 796.0 1.190 1554 5.023 67.2 0.035 0.120 16535 7.904 1.0 30.0 1.0 295 1.398 319.0 33.687 269130 2137 29.7 3806 1160.2 1.220 26.993 1879000 6.698 1860 55.6 2123 797.3 1.210 1406 4.677 64.2 0.038 0.126 16681 7.857 1.0 40.0 1.0 295 1.424 317.7 34.588 224130 2056 28.2 3746 1119.3 1.210 28.659 1711000 6.470 1768 52.3 2157 800.3 1.240 1262 4.568 64.4 0.042 0.135 16862 7.817 1.0 50.0 1.0 295 1.453 316.9 35.478 181870 1974 26.6 3672 1078.5 1.210 30.425 1549000 6.229 1674 48.8 2191 805.3 1.260 1125 4.219 61.0 0.048 0.148 16855 7.693 1.0 60.0 1.0 295 1.486 316.5 36.371 141560 1888 24.9 3576 1036.4 1.210 32.326 1387000 5.965 1572 45.0 2222 812.4 1.300 991 3.867 57.3 0.057 0.170 17044 7.671 1.0 70.0 1.0 295 1.524 316.7 37.264 103210 1794 22.9 3440 992.1 1.210 34.363 1221000 5.665 1460 40.8 2241 820.9 1.350 865 3.498 53.1 0.076 0.215 17169 7.661 1.0 80.0 1.0 295 1.570 317.6 38.158 66609 1681 20.3 3218 942.4 1.230 36.535 1036000 5.293 1327 35.7 2221 827.4 1.410 744 2.776 43.2 0.125 0.336 16745 7.540 1.0 90.0 1.0 295 1.622 319.2 39.051 31704 1493 15.7 2687 876.0 1.330 38.719 762100 4.676 1124 27.7 2020 807.0 1.510 627 1.431 22.8 0.460 1.205 14672 7.264 Ethylene-Oxygen-Carbon Dioxide, varying carbon dioxide dilution 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 1.338 325.3 31.013 418230 2376 33.8 3937 1283.3 1.240 22.652 2418000 7.305 2123 64.8 2035 797.9 1.170 1878 5.226 66.1 0.031 0.112 16321 8.020 1.0 10.0 1.0 295 1.332 318.0 32.301 -845920 2228 31.1 3773 1201.3 1.220 24.626 913700 7.004 1986 59.3 1897 755.2 1.170 1787 5.055 66.6 0.052 0.200 15632 8.241 1.0 20.0 1.0 295 1.326 311.1 33.612 -2033500 2083 28.4 3598 1122.0 1.200 26.776 -494100 6.695 1852 53.9 1760 713.6 1.170 1704 4.908 67.3 0.099 0.400 16467 9.356 1.0 30.0 1.0 295 1.321 304.6 34.905 -3116900 1945 25.9 3417 1047.5 1.180 29.041 -1773000 6.386 1725 48.8 1630 674.4 1.170 1627 4.808 68.4 0.223 0.953 18542 11.376 1.0 40.0 1.0 295 1.315 298.5 36.215 -4136100 1811 23.3 3223 974.8 1.160 31.489 -2972000 6.066 1600 43.8 1502 636.0 1.170 1555 4.742 70.0 0.644 2.918 20038 13.341 1.0 50.0 1.0 295 1.311 292.7 37.511 -5074000 1679 20.9 3012 905.0 1.150 34.049 -4074000 5.735 1478 38.9 1377 599.0 1.180 1486 4.376 66.9 2.355 11.280 20287 14.732 1.0 60.0 1.0 295 1.306 287.3 38.811 -5951700 1544 18.3 2764 834.9 1.130 36.700 -5108000 5.375 1352 34.0 1250 561.6 1.180 1420 4.335 68.6 11.680 59.060 19993 15.994 1.0 70.0 1.0 295 1.302 282.1 40.110 -6771900 1395 15.5 2437 760.8 1.130 39.266 -6088000 4.945 1212 28.7 1111 521.5 1.180 1352 3.540 57.9 101.700 543.100 20035 18.033 1.0 80.0 1.0 295 1.297 277.2 41.410 -7541800 1200 11.8 1929 668.4 1.150 41.321 -7045000 4.329 1026 21.8 932 471.4 1.190 1268 2.220 37.5 4280.000 24240.000 20508 22.004 Ethylene-Oxygen-Helium, varying helium dilution 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 1.338 325.3 31.013 418230 2376 33.8 3937 1283.3 1.240 22.652 2418000 7.305 2123 64.8 2035 797.9 1.170 1878 5.226 66.1 0.031 0.112 16321 8.020 1.0 10.0 1.0 295 1.355 342.5 28.336 412140 2437 32.5 3900 1317.9 1.230 21.317 2512000 7.114 2161 61.8 2062 844.8 1.180 1929 5.771 66.7 0.034 0.115 16451 7.978 1.0 20.0 1.0 295 1.375 362.9 25.611 404640 2508 31.1 3856 1358.8 1.220 19.878 2626000 6.909 2205 58.7 2092 900.8 1.190 1990 6.432 67.2 0.039 0.119 16585 7.928 1.0 30.0 1.0 295 1.398 386.7 22.924 395500 2590 29.7 3806 1406.5 1.220 18.369 2761000 6.698 2255 55.6 2123 966.5 1.210 2066 6.873 64.2 0.045 0.125 16736 7.883 1.0 40.0 1.0 295 1.424 415.8 20.200 383760 2690 28.2 3746 1464.6 1.210 16.738 2929000 6.470 2314 52.3 2157 1047.2 1.240 2160 7.821 64.4 0.054 0.133 16895 7.833 1.0 50.0 1.0 295 1.453 451.1 17.508 368550 2810 26.6 3672 1535.2 1.210 15.014 3138000 6.229 2382 48.8 2191 1146.3 1.260 2280 8.549 61.0 0.067 0.145 17017 7.767 1.0 60.0 1.0 295 1.486 496.1 14.807 347740 2959 24.9 3576 1624.3 1.210 13.160 3407000 5.965 2464 45.0 2222 1273.4 1.300 2435 9.499 57.3 0.088 0.165 17091 7.692 1.0 70.0 1.0 295 1.524 555.6 12.108 317670 3148 22.9 3440 1740.5 1.210 11.165 3758000 5.666 2562 40.8 2241 1440.2 1.350 2662 10.765 53.1 0.128 0.206 17131 7.644 1.0 80.0 1.0 295 1.569 639.7 9.405 270250 3386 20.3 3218 1898.3 1.230 9.005 4202000 5.294 2672 35.7 2221 1666.5 1.410 3018 11.264 43.2 0.237 0.316 16797 7.563 1.0 90.0 1.0 295 1.623 770.5 6.704 184680 3603 15.7 2687 2114.2 1.330 6.647 4439000 4.676 2712 27.7 2020 1947.8 1.510 3653 8.338 22.8 1.020 1.107 14905 7.379 Ethylene-Oxygen-Nitrogen, varying nitrogen dilution 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 1.338 325.3 31.013 418230 2376 33.8 3937 1283.3 1.240 22.652 2418000 7.305 2123 64.8 2035 797.9 1.170 1878 5.226 66.1 0.031 0.112 16321 8.020 1.0 10.0 1.0 295 1.343 327.4 30.715 380130 2317 31.9 3862 1251.2 1.220 23.325 2282000 7.076 2059 60.7 1995 796.6 1.180 1818 5.476 68.6 0.041 0.145 15861 7.950 1.0 20.0 1.0 295 1.349 329.8 30.413 340580 2259 30.1 3784 1220.5 1.210 24.005 2147000 6.848 1995 56.9 1957 795.9 1.180 1757 5.482 68.0 0.054 0.191 15395 7.867 1.0 30.0 1.0 295 1.355 332.2 30.114 300800 2198 28.2 3696 1189.1 1.200 24.704 2010000 6.617 1929 53.1 1915 794.7 1.190 1696 5.483 67.3 0.075 0.257 14907 7.784 1.0 40.0 1.0 295 1.361 334.7 29.812 259680 2132 26.3 3590 1155.1 1.190 25.442 1866000 6.371 1858 49.2 1867 792.3 1.210 1635 5.462 66.4 0.107 0.363 14448 7.739 1.0 50.0 1.0 295 1.368 337.2 29.513 218180 2060 24.3 3461 1118.6 1.180 26.195 1715000 6.111 1780 45.1 1810 788.2 1.220 1571 5.418 65.2 0.164 0.545 14153 7.819 1.0 60.0 1.0 295 1.375 339.7 29.213 175710 1977 22.2 3291 1077.2 1.170 26.957 1550000 5.820 1692 40.8 1738 781.2 1.230 1503 5.317 63.3 0.282 0.919 14411 8.292 1.0 70.0 1.0 295 1.381 342.3 28.913 132390 1874 19.7 3051 1028.1 1.170 27.681 1360000 5.475 1585 36.0 1640 768.1 1.250 1433 4.779 56.3 0.617 1.988 16036 9.778 1.0 73.8 1.0 295 1.385 343.4 28.798 115400 1824 18.5 2924 1005.3 1.170 27.930 1274000 5.313 1534 33.9 1589 759.9 1.260 1405 4.529 53.2 0.963 3.096 17196 10.822 1.0 80.0 1.0 295 1.388 345.0 28.613 88095 1723 16.3 2649 961.4 1.190 28.246 1110000 4.993 1433 29.8 1480 739.8 1.270 1355 3.557 41.5 2.853 9.216 19690 13.304