Datasets
-
Mole fraction (20)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
ρl - Mass density, kg/m3 (2)
Mole fraction of Phenol, 3-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Phenol, 3-methyl- (1) - Liquid mixture 1 |
| 289.15 |
0.0647 |
| 323.15 |
0.1669 |
Mole fraction of Phenol, 3-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mole fraction of Phenol, 3-methyl- (1) - Liquid mixture 2 |
| 289.15 |
0.4931 |
| 323.15 |
0.4552 |
Mole fraction of Octane (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Octane (2) - Liquid mixture 1 |
| 289.15 |
0.9193 |
| 323.15 |
0.7484 |
Mole fraction of Octane (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mole fraction of Octane (2) - Liquid mixture 2 |
| 289.15 |
0.0736 |
| 323.15 |
0.1109 |
Mole fraction of Phenol, 3-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Mole fraction of Octane (2) - Liquid mixture 1 |
Mole fraction of Phenol, 3-methyl- (1) - Liquid mixture 1 |
| 298.15 |
0.0000 |
0.5184 |
| 298.15 |
0.0340 |
0.5211 |
| 298.15 |
0.0462 |
0.5227 |
| 298.15 |
0.1016 |
0.5534 |
| 298.15 |
0.1057 |
0.5598 |
| 298.15 |
0.1392 |
0.5835 |
| 298.15 |
0.1680 |
0.6044 |
| 298.15 |
0.1749 |
0.6074 |
| 298.15 |
0.1885 |
0.6114 |
| 298.15 |
0.1989 |
0.6079 |
| 298.15 |
0.2115 |
0.6078 |
| 298.15 |
0.2225 |
0.6084 |
| 298.15 |
0.2265 |
0.6032 |
| 298.15 |
0.2609 |
0.5914 |
| 298.15 |
0.2882 |
0.5816 |
| 298.15 |
0.3180 |
0.5612 |
| 298.15 |
0.3549 |
0.5308 |
| 298.15 |
0.4018 |
0.5012 |
| 298.15 |
0.4053 |
0.5030 |
| 298.15 |
0.4163 |
0.4886 |
| 298.15 |
0.5275 |
0.4036 |
| 298.15 |
0.6151 |
0.3227 |
| 298.15 |
0.6543 |
0.2887 |
| 298.15 |
0.7793 |
0.1872 |
| 323.15 |
0.0000 |
0.4742 |
| 323.15 |
0.0299 |
0.4842 |
| 323.15 |
0.1119 |
0.4911 |
| 323.15 |
0.1324 |
0.5080 |
| 323.15 |
0.1677 |
0.5213 |
| 323.15 |
0.1938 |
0.5202 |
| 323.15 |
0.2401 |
0.5138 |
| 323.15 |
0.2440 |
0.5139 |
| 323.15 |
0.2483 |
0.5082 |
| 323.15 |
0.2809 |
0.4952 |
| 323.15 |
0.3016 |
0.4864 |
| 323.15 |
0.3021 |
0.4885 |
| 323.15 |
0.3261 |
0.4695 |
| 323.15 |
0.3609 |
0.4534 |
| 323.15 |
0.4035 |
0.4249 |
| 323.15 |
0.4503 |
0.4032 |
| 323.15 |
0.4885 |
0.3762 |
| 323.15 |
0.6479 |
0.2651 |
Mole fraction of Phenol, 3-methyl- (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Phenol, 3-methyl- (1) - Liquid mixture 1 |
| 333.15 |
29.39 |
0.4840 |
| 363.15 |
100.50 |
0.5301 |
Mole fraction of Phenol, 3-methyl- (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Pressure, kPa - Gas |
Mole fraction of Phenol, 3-methyl- (1) - Gas |
| 333.15 |
29.39 |
0.0022 |
| 363.15 |
100.50 |
0.0033 |
Mole fraction of Octane (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Octane (2) - Liquid mixture 1 |
| 333.15 |
29.39 |
0.1139 |
| 363.15 |
100.50 |
0.1166 |
Mole fraction of Octane (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Pressure, kPa - Gas |
Mole fraction of Octane (2) - Gas |
| 333.15 |
29.39 |
0.2829 |
| 363.15 |
100.50 |
0.1706 |
Temperature, K x Pressure, kPa x Mole fraction
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Octane (2) - Gas |
Mole fraction of Phenol, 3-methyl- (1) - Gas |
Mole fraction of Octane (2) - Liquid |
Mole fraction of Phenol, 3-methyl- (1) - Liquid |
| 333.15 |
14.04 |
0.4352 |
0.0158 |
0.0492 |
0.8245 |
| 333.15 |
14.47 |
0.3925 |
0.0147 |
0.0445 |
0.7697 |
| 333.15 |
15.41 |
0.3806 |
0.0101 |
0.0534 |
0.7592 |
| 333.15 |
19.09 |
0.3079 |
0.0063 |
0.0446 |
0.7066 |
| 333.15 |
19.18 |
0.4252 |
0.0068 |
0.1103 |
0.6866 |
| 333.15 |
19.84 |
0.2789 |
0.0049 |
0.0542 |
0.6578 |
| 333.15 |
20.04 |
0.3084 |
0.0077 |
0.0493 |
0.6849 |
| 333.15 |
20.11 |
0.3591 |
0.0191 |
0.0746 |
0.6949 |
| 333.15 |
20.88 |
0.2424 |
0.0061 |
0.0983 |
0.6720 |
| 333.15 |
21.10 |
0.4652 |
0.0219 |
0.0933 |
0.6663 |
| 333.15 |
21.29 |
0.3488 |
0.0017 |
0.0705 |
0.6436 |
| 333.15 |
25.96 |
0.3394 |
0.0039 |
0.1295 |
0.5644 |
| 363.15 |
12.02 |
0.8791 |
0.0063 |
0.0537 |
0.9391 |
| 363.15 |
47.10 |
0.3050 |
0.0203 |
0.0486 |
0.7827 |
| 363.15 |
48.41 |
0.4219 |
0.0123 |
0.0547 |
0.7682 |
| 363.15 |
50.00 |
0.3151 |
0.0211 |
0.0481 |
0.7563 |
| 363.15 |
54.01 |
0.2978 |
0.0179 |
0.0584 |
0.7317 |
| 363.15 |
58.30 |
0.3053 |
0.0136 |
0.0756 |
0.7074 |
| 363.15 |
61.48 |
0.4171 |
0.0165 |
0.1211 |
0.6932 |
| 363.15 |
63.49 |
0.2363 |
0.0122 |
0.0454 |
0.6932 |
| 363.15 |
64.42 |
0.3182 |
0.0138 |
0.0534 |
0.6642 |
| 363.15 |
67.91 |
0.3292 |
0.0161 |
0.0989 |
0.6545 |
| 363.15 |
68.22 |
0.2594 |
0.0105 |
0.0626 |
0.6633 |
| 363.15 |
68.68 |
0.3476 |
0.0140 |
0.0414 |
0.7040 |
| 363.15 |
91.20 |
0.2808 |
0.0060 |
0.1295 |
0.4162 |
Mole fraction of Phenol, 3-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Phenol, 3-methyl- (1) - Liquid mixture 1 |
| 289.15 |
0.0647 |
| 323.15 |
0.1669 |
Mole fraction of Phenol, 3-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mole fraction of Phenol, 3-methyl- (1) - Liquid mixture 2 |
| 289.15 |
0.4931 |
| 323.15 |
0.4552 |
Mole fraction of Octane (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Octane (2) - Liquid mixture 1 |
| 289.15 |
0.9193 |
| 323.15 |
0.7484 |
Mole fraction of Octane (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mole fraction of Octane (2) - Liquid mixture 2 |
| 289.15 |
0.0736 |
| 323.15 |
0.1109 |
Mole fraction of Phenol, 3-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Mole fraction of Octane (2) - Liquid mixture 1 |
Mole fraction of Phenol, 3-methyl- (1) - Liquid mixture 1 |
| 298.15 |
0.0000 |
0.5184 |
| 298.15 |
0.0340 |
0.5211 |
| 298.15 |
0.0462 |
0.5227 |
| 298.15 |
0.1016 |
0.5534 |
| 298.15 |
0.1057 |
0.5598 |
| 298.15 |
0.1392 |
0.5835 |
| 298.15 |
0.1680 |
0.6044 |
| 298.15 |
0.1749 |
0.6074 |
| 298.15 |
0.1885 |
0.6114 |
| 298.15 |
0.1989 |
0.6079 |
| 298.15 |
0.2115 |
0.6078 |
| 298.15 |
0.2225 |
0.6084 |
| 298.15 |
0.2265 |
0.6032 |
| 298.15 |
0.2609 |
0.5914 |
| 298.15 |
0.2882 |
0.5816 |
| 298.15 |
0.3180 |
0.5612 |
| 298.15 |
0.3549 |
0.5308 |
| 298.15 |
0.4018 |
0.5012 |
| 298.15 |
0.4053 |
0.5030 |
| 298.15 |
0.4163 |
0.4886 |
| 298.15 |
0.5275 |
0.4036 |
| 298.15 |
0.6151 |
0.3227 |
| 298.15 |
0.6543 |
0.2887 |
| 298.15 |
0.7793 |
0.1872 |
| 323.15 |
0.0000 |
0.4742 |
| 323.15 |
0.0299 |
0.4842 |
| 323.15 |
0.1119 |
0.4911 |
| 323.15 |
0.1324 |
0.5080 |
| 323.15 |
0.1677 |
0.5213 |
| 323.15 |
0.1938 |
0.5202 |
| 323.15 |
0.2401 |
0.5138 |
| 323.15 |
0.2440 |
0.5139 |
| 323.15 |
0.2483 |
0.5082 |
| 323.15 |
0.2809 |
0.4952 |
| 323.15 |
0.3016 |
0.4864 |
| 323.15 |
0.3021 |
0.4885 |
| 323.15 |
0.3261 |
0.4695 |
| 323.15 |
0.3609 |
0.4534 |
| 323.15 |
0.4035 |
0.4249 |
| 323.15 |
0.4503 |
0.4032 |
| 323.15 |
0.4885 |
0.3762 |
| 323.15 |
0.6479 |
0.2651 |
Mole fraction of Phenol, 3-methyl- (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Phenol, 3-methyl- (1) - Liquid mixture 1 |
| 333.15 |
29.39 |
0.4840 |
| 363.15 |
100.50 |
0.5301 |
Mole fraction of Phenol, 3-methyl- (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Pressure, kPa - Gas |
Mole fraction of Phenol, 3-methyl- (1) - Gas |
| 333.15 |
29.39 |
0.0022 |
| 363.15 |
100.50 |
0.0033 |
Mole fraction of Octane (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Octane (2) - Liquid mixture 1 |
| 333.15 |
29.39 |
0.1139 |
| 363.15 |
100.50 |
0.1166 |
Mole fraction of Octane (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Pressure, kPa - Gas |
Mole fraction of Octane (2) - Gas |
| 333.15 |
29.39 |
0.2829 |
| 363.15 |
100.50 |
0.1706 |
Temperature, K x Pressure, kPa x Mole fraction
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Octane (2) - Gas |
Mole fraction of Phenol, 3-methyl- (1) - Gas |
Mole fraction of Octane (2) - Liquid |
Mole fraction of Phenol, 3-methyl- (1) - Liquid |
| 333.15 |
14.04 |
0.4352 |
0.0158 |
0.0492 |
0.8245 |
| 333.15 |
14.47 |
0.3925 |
0.0147 |
0.0445 |
0.7697 |
| 333.15 |
15.41 |
0.3806 |
0.0101 |
0.0534 |
0.7592 |
| 333.15 |
19.09 |
0.3079 |
0.0063 |
0.0446 |
0.7066 |
| 333.15 |
19.18 |
0.4252 |
0.0068 |
0.1103 |
0.6866 |
| 333.15 |
19.84 |
0.2789 |
0.0049 |
0.0542 |
0.6578 |
| 333.15 |
20.04 |
0.3084 |
0.0077 |
0.0493 |
0.6849 |
| 333.15 |
20.11 |
0.3591 |
0.0191 |
0.0746 |
0.6949 |
| 333.15 |
20.88 |
0.2424 |
0.0061 |
0.0983 |
0.6720 |
| 333.15 |
21.10 |
0.4652 |
0.0219 |
0.0933 |
0.6663 |
| 333.15 |
21.29 |
0.3488 |
0.0017 |
0.0705 |
0.6436 |
| 333.15 |
25.96 |
0.3394 |
0.0039 |
0.1295 |
0.5644 |
| 363.15 |
12.02 |
0.8791 |
0.0063 |
0.0537 |
0.9391 |
| 363.15 |
47.10 |
0.3050 |
0.0203 |
0.0486 |
0.7827 |
| 363.15 |
48.41 |
0.4219 |
0.0123 |
0.0547 |
0.7682 |
| 363.15 |
50.00 |
0.3151 |
0.0211 |
0.0481 |
0.7563 |
| 363.15 |
54.01 |
0.2978 |
0.0179 |
0.0584 |
0.7317 |
| 363.15 |
58.30 |
0.3053 |
0.0136 |
0.0756 |
0.7074 |
| 363.15 |
61.48 |
0.4171 |
0.0165 |
0.1211 |
0.6932 |
| 363.15 |
63.49 |
0.2363 |
0.0122 |
0.0454 |
0.6932 |
| 363.15 |
64.42 |
0.3182 |
0.0138 |
0.0534 |
0.6642 |
| 363.15 |
67.91 |
0.3292 |
0.0161 |
0.0989 |
0.6545 |
| 363.15 |
68.22 |
0.2594 |
0.0105 |
0.0626 |
0.6633 |
| 363.15 |
68.68 |
0.3476 |
0.0140 |
0.0414 |
0.7040 |
| 363.15 |
91.20 |
0.2808 |
0.0060 |
0.1295 |
0.4162 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Octane (2) - Liquid |
Mole fraction of Phenol, 3-methyl- (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 333.15 |
0.0523 |
0.7394 |
15.93 |
| 363.15 |
0.0591 |
0.7436 |
63.63 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Octane (2) - Liquid |
Mole fraction of Phenol, 3-methyl- (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 333.15 |
0.0523 |
0.7394 |
15.93 |
| 363.15 |
0.0591 |
0.7436 |
63.63 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Fixed |
Measured |
| Mole fraction of Octane (2) - Liquid |
Mole fraction of Phenol, 3-methyl- (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0000 |
0.7997 |
1024.04 |
| 0.0000 |
0.8215 |
1024.36 |
| 0.0000 |
0.8450 |
1024.52 |
| 0.0000 |
0.8635 |
1024.3 |
| 0.0000 |
0.8759 |
1024.67 |
| 0.0000 |
0.9231 |
1025.3 |
| 0.0000 |
0.9426 |
1025.49 |
| 0.0000 |
0.9703 |
1025.78 |
| 0.0000 |
1.0000 |
1025.95 |
| 0.0512 |
0.7588 |
994.94 |
| 0.0558 |
0.7978 |
994.4 |
| 0.0565 |
0.8710 |
997.01 |
| 0.0597 |
0.8120 |
992.85 |
| 0.0663 |
0.8178 |
989.98 |
| 0.0670 |
0.9053 |
993.35 |
| 0.0773 |
0.8698 |
987.43 |
| 0.0803 |
0.7555 |
983.78 |
| 0.1036 |
0.7852 |
971.48 |
| 0.1040 |
0.7166 |
967.32 |
| 0.1093 |
0.7526 |
967.15 |
| 0.1098 |
0.7313 |
965.76 |
| 0.1122 |
0.8196 |
970.41 |
| 0.1149 |
0.7752 |
965.99 |
| 0.1180 |
0.7617 |
964.06 |
| 0.1197 |
0.8803 |
970.59 |
| 0.1217 |
0.8279 |
966.77 |
| 0.1364 |
0.8380 |
961.52 |
| 0.1643 |
0.6865 |
939.43 |
| 0.1672 |
0.7037 |
939.83 |
| 0.1754 |
0.7121 |
937.29 |
| 0.1804 |
0.7566 |
939.58 |
| 0.1858 |
0.7900 |
940.11 |
| 0.1862 |
0.7671 |
938.2 |
| 0.1874 |
0.6498 |
927.55 |
| 0.2284 |
0.6519 |
912.98 |
| 0.2298 |
0.6327 |
910.27 |
| 0.2347 |
0.6609 |
911.42 |
| 0.2354 |
0.6697 |
911.89 |
| 0.2439 |
0.6980 |
912.71 |
| 0.2473 |
0.7527 |
916.86 |
| 0.2519 |
0.7258 |
912.78 |
| 0.2552 |
0.7020 |
909.37 |
| 0.2899 |
0.6000 |
887.74 |
| 0.2956 |
0.6170 |
887.56 |
| 0.2961 |
0.5782 |
883.14 |
| 0.2993 |
0.6050 |
885.24 |
| 0.3074 |
0.6394 |
887.64 |
| 0.3200 |
0.6598 |
886.27 |
| 0.3536 |
0.6093 |
871.51 |
| 0.3543 |
0.5304 |
861.06 |
| 0.3559 |
0.5642 |
864.79 |
| 0.3588 |
0.5537 |
862.95 |
| 0.3620 |
0.5391 |
860.54 |
| 0.3763 |
0.5757 |
862.21 |
| 0.3868 |
0.6132 |
864.19 |
| 0.3875 |
0.5943 |
861.67 |
| 0.4068 |
0.5592 |
852.43 |
| 0.4084 |
0.5182 |
846.2 |
| 0.4180 |
0.5372 |
847.68 |
| 0.4227 |
0.4985 |
840.54 |
| 0.4305 |
0.4812 |
836.64 |
| 0.4350 |
0.5482 |
845.15 |
| 0.4553 |
0.5134 |
836.02 |
| 0.4818 |
0.4257 |
817.81 |
| 0.4878 |
0.4487 |
820.19 |
| 0.4924 |
0.4383 |
817.94 |
| 0.5012 |
0.4988 |
825.55 |
| 0.5107 |
0.4516 |
817.22 |
| 0.5196 |
0.4528 |
815.39 |
| 0.5206 |
0.4652 |
817.3 |
| 0.5298 |
0.4060 |
806.49 |
| 0.5487 |
0.3813 |
799.63 |
| 0.5552 |
0.3896 |
799.76 |
| 0.5572 |
0.4296 |
806.05 |
| 0.5676 |
0.4076 |
800.8 |
| 0.5724 |
0.3947 |
798.55 |
| 0.6096 |
0.3372 |
783.61 |
| 0.6157 |
0.3729 |
788.74 |
| 0.6167 |
0.3238 |
780.52 |
| 0.6269 |
0.3517 |
783.7 |
| 0.6279 |
0.3259 |
779.21 |
| 0.6387 |
0.3613 |
783.91 |
| 0.6610 |
0.3130 |
773.46 |
| 0.6847 |
0.2723 |
763.73 |
| 0.6915 |
0.2703 |
762.55 |
| 0.7055 |
0.2776 |
762.38 |
| 0.7060 |
0.2714 |
761.53 |
| 0.7104 |
0.2537 |
757.76 |
| 0.7248 |
0.2670 |
758.78 |
| 0.7365 |
0.2275 |
750.84 |
| 0.7572 |
0.2356 |
750.41 |
| 0.7602 |
0.2213 |
747.71 |
| 0.7628 |
0.2078 |
744.92 |
| 0.7716 |
0.1930 |
741.7 |
| 0.7789 |
0.2084 |
743.8 |
| 0.7818 |
0.2182 |
745.29 |
| 0.7836 |
0.1896 |
740.03 |
| 0.7967 |
0.1973 |
740.51 |
| 0.8089 |
0.1801 |
736.52 |
| 0.8154 |
0.1704 |
734.41 |
| 0.8301 |
0.1602 |
731.5 |
| 0.8382 |
0.1397 |
727.36 |
| 0.8431 |
0.1374 |
726.56 |
| 0.8446 |
0.1313 |
725.39 |
| 0.8750 |
0.1213 |
721.79 |
| 0.8773 |
0.1227 |
721.91 |
| 0.8957 |
0.0984 |
716.49 |
| 0.8989 |
0.0873 |
714.31 |
| 0.9057 |
0.0797 |
712.6 |
| 0.9205 |
0.0696 |
710.17 |
| 1.0000 |
0.0000 |
694.52 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Fixed |
Measured |
| Mole fraction of Octane (2) - Liquid |
Mole fraction of Phenol, 3-methyl- (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0000 |
0.7997 |
1024.04 |
| 0.0000 |
0.8215 |
1024.36 |
| 0.0000 |
0.8450 |
1024.52 |
| 0.0000 |
0.8635 |
1024.3 |
| 0.0000 |
0.8759 |
1024.67 |
| 0.0000 |
0.9231 |
1025.3 |
| 0.0000 |
0.9426 |
1025.49 |
| 0.0000 |
0.9703 |
1025.78 |
| 0.0000 |
1.0000 |
1025.95 |
| 0.0512 |
0.7588 |
994.94 |
| 0.0558 |
0.7978 |
994.4 |
| 0.0565 |
0.8710 |
997.01 |
| 0.0597 |
0.8120 |
992.85 |
| 0.0663 |
0.8178 |
989.98 |
| 0.0670 |
0.9053 |
993.35 |
| 0.0773 |
0.8698 |
987.43 |
| 0.0803 |
0.7555 |
983.78 |
| 0.1036 |
0.7852 |
971.48 |
| 0.1040 |
0.7166 |
967.32 |
| 0.1093 |
0.7526 |
967.15 |
| 0.1098 |
0.7313 |
965.76 |
| 0.1122 |
0.8196 |
970.41 |
| 0.1149 |
0.7752 |
965.99 |
| 0.1180 |
0.7617 |
964.06 |
| 0.1197 |
0.8803 |
970.59 |
| 0.1217 |
0.8279 |
966.77 |
| 0.1364 |
0.8380 |
961.52 |
| 0.1643 |
0.6865 |
939.43 |
| 0.1672 |
0.7037 |
939.83 |
| 0.1754 |
0.7121 |
937.29 |
| 0.1804 |
0.7566 |
939.58 |
| 0.1858 |
0.7900 |
940.11 |
| 0.1862 |
0.7671 |
938.2 |
| 0.1874 |
0.6498 |
927.55 |
| 0.2284 |
0.6519 |
912.98 |
| 0.2298 |
0.6327 |
910.27 |
| 0.2347 |
0.6609 |
911.42 |
| 0.2354 |
0.6697 |
911.89 |
| 0.2439 |
0.6980 |
912.71 |
| 0.2473 |
0.7527 |
916.86 |
| 0.2519 |
0.7258 |
912.78 |
| 0.2552 |
0.7020 |
909.37 |
| 0.2899 |
0.6000 |
887.74 |
| 0.2956 |
0.6170 |
887.56 |
| 0.2961 |
0.5782 |
883.14 |
| 0.2993 |
0.6050 |
885.24 |
| 0.3074 |
0.6394 |
887.64 |
| 0.3200 |
0.6598 |
886.27 |
| 0.3536 |
0.6093 |
871.51 |
| 0.3543 |
0.5304 |
861.06 |
| 0.3559 |
0.5642 |
864.79 |
| 0.3588 |
0.5537 |
862.95 |
| 0.3620 |
0.5391 |
860.54 |
| 0.3763 |
0.5757 |
862.21 |
| 0.3868 |
0.6132 |
864.19 |
| 0.3875 |
0.5943 |
861.67 |
| 0.4068 |
0.5592 |
852.43 |
| 0.4084 |
0.5182 |
846.2 |
| 0.4180 |
0.5372 |
847.68 |
| 0.4227 |
0.4985 |
840.54 |
| 0.4305 |
0.4812 |
836.64 |
| 0.4350 |
0.5482 |
845.15 |
| 0.4553 |
0.5134 |
836.02 |
| 0.4818 |
0.4257 |
817.81 |
| 0.4878 |
0.4487 |
820.19 |
| 0.4924 |
0.4383 |
817.94 |
| 0.5012 |
0.4988 |
825.55 |
| 0.5107 |
0.4516 |
817.22 |
| 0.5196 |
0.4528 |
815.39 |
| 0.5206 |
0.4652 |
817.3 |
| 0.5298 |
0.4060 |
806.49 |
| 0.5487 |
0.3813 |
799.63 |
| 0.5552 |
0.3896 |
799.76 |
| 0.5572 |
0.4296 |
806.05 |
| 0.5676 |
0.4076 |
800.8 |
| 0.5724 |
0.3947 |
798.55 |
| 0.6096 |
0.3372 |
783.61 |
| 0.6157 |
0.3729 |
788.74 |
| 0.6167 |
0.3238 |
780.52 |
| 0.6269 |
0.3517 |
783.7 |
| 0.6279 |
0.3259 |
779.21 |
| 0.6387 |
0.3613 |
783.91 |
| 0.6610 |
0.3130 |
773.46 |
| 0.6847 |
0.2723 |
763.73 |
| 0.6915 |
0.2703 |
762.55 |
| 0.7055 |
0.2776 |
762.38 |
| 0.7060 |
0.2714 |
761.53 |
| 0.7104 |
0.2537 |
757.76 |
| 0.7248 |
0.2670 |
758.78 |
| 0.7365 |
0.2275 |
750.84 |
| 0.7572 |
0.2356 |
750.41 |
| 0.7602 |
0.2213 |
747.71 |
| 0.7628 |
0.2078 |
744.92 |
| 0.7716 |
0.1930 |
741.7 |
| 0.7789 |
0.2084 |
743.8 |
| 0.7818 |
0.2182 |
745.29 |
| 0.7836 |
0.1896 |
740.03 |
| 0.7967 |
0.1973 |
740.51 |
| 0.8089 |
0.1801 |
736.52 |
| 0.8154 |
0.1704 |
734.41 |
| 0.8301 |
0.1602 |
731.5 |
| 0.8382 |
0.1397 |
727.36 |
| 0.8431 |
0.1374 |
726.56 |
| 0.8446 |
0.1313 |
725.39 |
| 0.8750 |
0.1213 |
721.79 |
| 0.8773 |
0.1227 |
721.91 |
| 0.8957 |
0.0984 |
716.49 |
| 0.8989 |
0.0873 |
714.31 |
| 0.9057 |
0.0797 |
712.6 |
| 0.9205 |
0.0696 |
710.17 |
| 1.0000 |
0.0000 |
694.52 |
Sources
