Datasets
-
Mole fraction (8)
-
ρl - Mass density, kg/m3 (4)
-
Tboil - Boiling temperature at pressure P, K (4)
Mole fraction of Butanoic acid, methyl ester (1)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
Mole fraction of Butanoic acid, methyl ester (1) - Liquid |
Mole fraction of Butanoic acid, methyl ester (1) - Gas |
0.0137 |
0.0239 |
0.0320 |
0.0488 |
0.0594 |
0.0835 |
0.0848 |
0.1159 |
0.1157 |
0.1501 |
0.1460 |
0.1831 |
0.1793 |
0.2168 |
0.2169 |
0.2519 |
0.2684 |
0.2976 |
0.3037 |
0.3271 |
0.3339 |
0.3489 |
0.3629 |
0.3706 |
0.4376 |
0.4290 |
0.4623 |
0.4462 |
0.4938 |
0.4648 |
0.5344 |
0.4977 |
0.5759 |
0.5262 |
0.6212 |
0.5634 |
0.6499 |
0.5858 |
0.6932 |
0.6242 |
0.7213 |
0.6503 |
0.7651 |
0.6916 |
0.8003 |
0.7273 |
0.8514 |
0.7855 |
0.8930 |
0.8387 |
0.9406 |
0.9077 |
Azeotropic composition: mole fraction of Butanoic acid, methyl ester (1)
[ref]
Temperature, K - Liquid |
Azeotropic composition: mole fraction of Butanoic acid, methyl ester (1) - Liquid |
368.22 |
0.3980 |
Azeotropic composition: mole fraction of Butanoic acid, methyl ester (1)
[ref]
Pressure, kPa - Liquid |
Azeotropic composition: mole fraction of Butanoic acid, methyl ester (1) - Liquid |
101.32 |
0.3980 |
Mole fraction of Butanoic acid, methyl ester (1)
[ref]
Operational condition: Pressure, kPa =
101.32 (Liquid)
Mole fraction of Butanoic acid, methyl ester (1) - Liquid |
Mole fraction of Butanoic acid, methyl ester (1) - Gas |
0.0000 |
0.0000 |
0.0180 |
0.0290 |
0.0280 |
0.0430 |
0.0360 |
0.0540 |
0.0440 |
0.0660 |
0.0480 |
0.0710 |
0.0570 |
0.0830 |
0.0780 |
0.1100 |
0.0920 |
0.1280 |
0.1070 |
0.1450 |
0.1170 |
0.1580 |
0.1470 |
0.1900 |
0.1560 |
0.1990 |
0.1860 |
0.2280 |
0.1960 |
0.2380 |
0.2050 |
0.2470 |
0.2180 |
0.2590 |
0.2300 |
0.2680 |
0.2460 |
0.2830 |
0.2630 |
0.2970 |
0.2800 |
0.3110 |
0.2990 |
0.3260 |
0.3170 |
0.3400 |
0.3340 |
0.3530 |
0.3570 |
0.3690 |
0.3790 |
0.3860 |
0.4040 |
0.4040 |
0.4260 |
0.4190 |
0.4470 |
0.4330 |
0.4660 |
0.4470 |
0.4860 |
0.4610 |
0.5050 |
0.4740 |
0.5240 |
0.4880 |
0.5410 |
0.4990 |
0.5590 |
0.5110 |
0.5760 |
0.5240 |
0.5910 |
0.5340 |
0.6290 |
0.5630 |
0.6630 |
0.5890 |
0.6980 |
0.6160 |
0.7360 |
0.6490 |
0.7590 |
0.6710 |
0.7820 |
0.6930 |
0.8030 |
0.7140 |
0.8300 |
0.7420 |
0.8480 |
0.7650 |
0.8610 |
0.7800 |
0.8760 |
0.7970 |
0.8880 |
0.8140 |
0.8970 |
0.8250 |
0.9050 |
0.8370 |
0.9140 |
0.8500 |
0.9480 |
0.9020 |
0.9570 |
0.9180 |
0.9690 |
0.9390 |
0.9810 |
0.9600 |
0.9920 |
0.9830 |
1.0000 |
1.0000 |
Mole fraction of Butanoic acid, methyl ester (1)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
Mole fraction of Butanoic acid, methyl ester (1) - Liquid |
Mole fraction of Butanoic acid, methyl ester (1) - Gas |
0.0137 |
0.0239 |
0.0320 |
0.0488 |
0.0594 |
0.0835 |
0.0848 |
0.1159 |
0.1157 |
0.1501 |
0.1460 |
0.1831 |
0.1793 |
0.2168 |
0.2169 |
0.2519 |
0.2684 |
0.2976 |
0.3037 |
0.3271 |
0.3339 |
0.3489 |
0.3629 |
0.3706 |
0.4376 |
0.4290 |
0.4623 |
0.4462 |
0.4938 |
0.4648 |
0.5344 |
0.4977 |
0.5759 |
0.5262 |
0.6212 |
0.5634 |
0.6499 |
0.5858 |
0.6932 |
0.6242 |
0.7213 |
0.6503 |
0.7651 |
0.6916 |
0.8003 |
0.7273 |
0.8514 |
0.7855 |
0.8930 |
0.8387 |
0.9406 |
0.9077 |
Azeotropic composition: mole fraction of Butanoic acid, methyl ester (1)
[ref]
Temperature, K - Liquid |
Azeotropic composition: mole fraction of Butanoic acid, methyl ester (1) - Liquid |
368.22 |
0.3980 |
Azeotropic composition: mole fraction of Butanoic acid, methyl ester (1)
[ref]
Pressure, kPa - Liquid |
Azeotropic composition: mole fraction of Butanoic acid, methyl ester (1) - Liquid |
101.32 |
0.3980 |
Mole fraction of Butanoic acid, methyl ester (1)
[ref]
Operational condition: Pressure, kPa =
101.32 (Liquid)
Mole fraction of Butanoic acid, methyl ester (1) - Liquid |
Mole fraction of Butanoic acid, methyl ester (1) - Gas |
0.0000 |
0.0000 |
0.0180 |
0.0290 |
0.0280 |
0.0430 |
0.0360 |
0.0540 |
0.0440 |
0.0660 |
0.0480 |
0.0710 |
0.0570 |
0.0830 |
0.0780 |
0.1100 |
0.0920 |
0.1280 |
0.1070 |
0.1450 |
0.1170 |
0.1580 |
0.1470 |
0.1900 |
0.1560 |
0.1990 |
0.1860 |
0.2280 |
0.1960 |
0.2380 |
0.2050 |
0.2470 |
0.2180 |
0.2590 |
0.2300 |
0.2680 |
0.2460 |
0.2830 |
0.2630 |
0.2970 |
0.2800 |
0.3110 |
0.2990 |
0.3260 |
0.3170 |
0.3400 |
0.3340 |
0.3530 |
0.3570 |
0.3690 |
0.3790 |
0.3860 |
0.4040 |
0.4040 |
0.4260 |
0.4190 |
0.4470 |
0.4330 |
0.4660 |
0.4470 |
0.4860 |
0.4610 |
0.5050 |
0.4740 |
0.5240 |
0.4880 |
0.5410 |
0.4990 |
0.5590 |
0.5110 |
0.5760 |
0.5240 |
0.5910 |
0.5340 |
0.6290 |
0.5630 |
0.6630 |
0.5890 |
0.6980 |
0.6160 |
0.7360 |
0.6490 |
0.7590 |
0.6710 |
0.7820 |
0.6930 |
0.8030 |
0.7140 |
0.8300 |
0.7420 |
0.8480 |
0.7650 |
0.8610 |
0.7800 |
0.8760 |
0.7970 |
0.8880 |
0.8140 |
0.8970 |
0.8250 |
0.9050 |
0.8370 |
0.9140 |
0.8500 |
0.9480 |
0.9020 |
0.9570 |
0.9180 |
0.9690 |
0.9390 |
0.9810 |
0.9600 |
0.9920 |
0.9830 |
1.0000 |
1.0000 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.325 (Liquid)
Mole fraction of Butanoic acid, methyl ester (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0337 |
684.36 |
0.0689 |
689.75 |
0.1020 |
694.93 |
0.1531 |
703.25 |
0.2487 |
719.6 |
0.3261 |
733.58 |
0.3824 |
744.29 |
0.4586 |
759.5 |
0.5333 |
775.25 |
0.6085 |
791.88 |
0.6618 |
804.18 |
0.7161 |
817.1 |
0.7869 |
834.67 |
0.8394 |
848.24 |
0.8882 |
861.22 |
0.9255 |
871.41 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of Butanoic acid, methyl ester (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
288.15 |
688.16 |
0.0000 |
298.15 |
679.62 |
0.0000 |
308.15 |
670.96 |
0.0000 |
318.15 |
662.33 |
0.0000 |
328.15 |
653.61 |
0.0440 |
328.15 |
659.99 |
0.0478 |
288.15 |
695.54 |
0.0485 |
298.15 |
686.88 |
0.0630 |
308.15 |
680.36 |
0.0768 |
318.15 |
673.72 |
0.0876 |
298.15 |
693.0 |
0.0890 |
318.15 |
675.62 |
0.0921 |
328.15 |
667.12 |
0.0940 |
288.15 |
702.79 |
0.1170 |
308.15 |
688.78 |
0.1388 |
328.15 |
674.29 |
0.1389 |
298.15 |
701.34 |
0.1411 |
288.15 |
710.56 |
0.1535 |
318.15 |
685.7 |
0.1870 |
308.15 |
700.22 |
0.1890 |
328.15 |
682.37 |
0.2025 |
288.15 |
720.91 |
0.2117 |
318.15 |
695.29 |
0.2122 |
298.15 |
713.65 |
0.2476 |
288.15 |
728.91 |
0.2567 |
318.15 |
702.97 |
0.2586 |
298.15 |
721.76 |
0.2611 |
328.15 |
694.33 |
0.2996 |
288.15 |
738.37 |
0.3006 |
328.15 |
701.19 |
0.3020 |
298.15 |
729.67 |
0.3025 |
308.15 |
720.34 |
0.3050 |
318.15 |
711.44 |
0.3531 |
288.15 |
748.53 |
0.3544 |
318.15 |
720.36 |
0.3571 |
298.15 |
739.98 |
0.4019 |
298.15 |
748.57 |
0.4042 |
318.15 |
729.76 |
0.4098 |
328.15 |
721.06 |
0.4112 |
288.15 |
759.9 |
0.4170 |
308.15 |
741.86 |
0.4351 |
318.15 |
735.72 |
0.4484 |
288.15 |
767.46 |
0.4492 |
298.15 |
758.07 |
0.4532 |
328.15 |
729.42 |
0.5011 |
318.15 |
748.89 |
0.5017 |
298.15 |
768.87 |
0.5023 |
288.15 |
778.63 |
0.5031 |
328.15 |
739.32 |
0.5047 |
308.15 |
759.48 |
0.5487 |
318.15 |
758.83 |
0.5522 |
328.15 |
749.41 |
0.5526 |
288.15 |
789.52 |
0.5573 |
298.15 |
780.67 |
0.5651 |
308.15 |
772.28 |
0.5933 |
308.15 |
778.47 |
0.5952 |
298.15 |
789.01 |
0.5962 |
318.15 |
768.97 |
0.5979 |
328.15 |
759.1 |
0.5984 |
288.15 |
799.7 |
0.6466 |
298.15 |
800.69 |
0.6471 |
288.15 |
810.83 |
0.6473 |
328.15 |
769.85 |
0.6532 |
308.15 |
791.9 |
0.6971 |
318.15 |
791.66 |
0.7045 |
308.15 |
803.77 |
0.7060 |
328.15 |
783.28 |
0.7063 |
298.15 |
814.61 |
0.7077 |
288.15 |
825.2 |
0.7424 |
298.15 |
823.41 |
0.7456 |
328.15 |
792.62 |
0.7463 |
288.15 |
834.68 |
0.7469 |
318.15 |
803.4 |
0.7487 |
308.15 |
814.31 |
0.7648 |
308.15 |
818.37 |
0.7890 |
308.15 |
824.36 |
0.7926 |
328.15 |
803.93 |
0.7973 |
318.15 |
815.75 |
0.7980 |
288.15 |
847.73 |
0.7993 |
298.15 |
837.66 |
0.8454 |
318.15 |
827.9 |
0.8514 |
308.15 |
840.37 |
0.8600 |
328.15 |
820.85 |
0.8623 |
298.15 |
853.85 |
0.8818 |
308.15 |
848.32 |
0.8912 |
288.15 |
872.29 |
0.8948 |
318.15 |
840.81 |
0.9015 |
298.15 |
864.37 |
0.9028 |
328.15 |
832.08 |
0.9257 |
308.15 |
860.13 |
0.9493 |
288.15 |
888.46 |
0.9507 |
298.15 |
878.23 |
0.9508 |
328.15 |
845.05 |
0.9513 |
318.15 |
856.25 |
0.9603 |
308.15 |
869.83 |
1.0000 |
288.15 |
903.31 |
1.0000 |
298.15 |
892.31 |
1.0000 |
308.15 |
881.19 |
1.0000 |
318.15 |
870.06 |
1.0000 |
328.15 |
858.8 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.325 (Liquid)
Mole fraction of Butanoic acid, methyl ester (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0337 |
684.36 |
0.0689 |
689.75 |
0.1020 |
694.93 |
0.1531 |
703.25 |
0.2487 |
719.6 |
0.3261 |
733.58 |
0.3824 |
744.29 |
0.4586 |
759.5 |
0.5333 |
775.25 |
0.6085 |
791.88 |
0.6618 |
804.18 |
0.7161 |
817.1 |
0.7869 |
834.67 |
0.8394 |
848.24 |
0.8882 |
861.22 |
0.9255 |
871.41 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of Butanoic acid, methyl ester (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
288.15 |
688.16 |
0.0000 |
298.15 |
679.62 |
0.0000 |
308.15 |
670.96 |
0.0000 |
318.15 |
662.33 |
0.0000 |
328.15 |
653.61 |
0.0440 |
328.15 |
659.99 |
0.0478 |
288.15 |
695.54 |
0.0485 |
298.15 |
686.88 |
0.0630 |
308.15 |
680.36 |
0.0768 |
318.15 |
673.72 |
0.0876 |
298.15 |
693.0 |
0.0890 |
318.15 |
675.62 |
0.0921 |
328.15 |
667.12 |
0.0940 |
288.15 |
702.79 |
0.1170 |
308.15 |
688.78 |
0.1388 |
328.15 |
674.29 |
0.1389 |
298.15 |
701.34 |
0.1411 |
288.15 |
710.56 |
0.1535 |
318.15 |
685.7 |
0.1870 |
308.15 |
700.22 |
0.1890 |
328.15 |
682.37 |
0.2025 |
288.15 |
720.91 |
0.2117 |
318.15 |
695.29 |
0.2122 |
298.15 |
713.65 |
0.2476 |
288.15 |
728.91 |
0.2567 |
318.15 |
702.97 |
0.2586 |
298.15 |
721.76 |
0.2611 |
328.15 |
694.33 |
0.2996 |
288.15 |
738.37 |
0.3006 |
328.15 |
701.19 |
0.3020 |
298.15 |
729.67 |
0.3025 |
308.15 |
720.34 |
0.3050 |
318.15 |
711.44 |
0.3531 |
288.15 |
748.53 |
0.3544 |
318.15 |
720.36 |
0.3571 |
298.15 |
739.98 |
0.4019 |
298.15 |
748.57 |
0.4042 |
318.15 |
729.76 |
0.4098 |
328.15 |
721.06 |
0.4112 |
288.15 |
759.9 |
0.4170 |
308.15 |
741.86 |
0.4351 |
318.15 |
735.72 |
0.4484 |
288.15 |
767.46 |
0.4492 |
298.15 |
758.07 |
0.4532 |
328.15 |
729.42 |
0.5011 |
318.15 |
748.89 |
0.5017 |
298.15 |
768.87 |
0.5023 |
288.15 |
778.63 |
0.5031 |
328.15 |
739.32 |
0.5047 |
308.15 |
759.48 |
0.5487 |
318.15 |
758.83 |
0.5522 |
328.15 |
749.41 |
0.5526 |
288.15 |
789.52 |
0.5573 |
298.15 |
780.67 |
0.5651 |
308.15 |
772.28 |
0.5933 |
308.15 |
778.47 |
0.5952 |
298.15 |
789.01 |
0.5962 |
318.15 |
768.97 |
0.5979 |
328.15 |
759.1 |
0.5984 |
288.15 |
799.7 |
0.6466 |
298.15 |
800.69 |
0.6471 |
288.15 |
810.83 |
0.6473 |
328.15 |
769.85 |
0.6532 |
308.15 |
791.9 |
0.6971 |
318.15 |
791.66 |
0.7045 |
308.15 |
803.77 |
0.7060 |
328.15 |
783.28 |
0.7063 |
298.15 |
814.61 |
0.7077 |
288.15 |
825.2 |
0.7424 |
298.15 |
823.41 |
0.7456 |
328.15 |
792.62 |
0.7463 |
288.15 |
834.68 |
0.7469 |
318.15 |
803.4 |
0.7487 |
308.15 |
814.31 |
0.7648 |
308.15 |
818.37 |
0.7890 |
308.15 |
824.36 |
0.7926 |
328.15 |
803.93 |
0.7973 |
318.15 |
815.75 |
0.7980 |
288.15 |
847.73 |
0.7993 |
298.15 |
837.66 |
0.8454 |
318.15 |
827.9 |
0.8514 |
308.15 |
840.37 |
0.8600 |
328.15 |
820.85 |
0.8623 |
298.15 |
853.85 |
0.8818 |
308.15 |
848.32 |
0.8912 |
288.15 |
872.29 |
0.8948 |
318.15 |
840.81 |
0.9015 |
298.15 |
864.37 |
0.9028 |
328.15 |
832.08 |
0.9257 |
308.15 |
860.13 |
0.9493 |
288.15 |
888.46 |
0.9507 |
298.15 |
878.23 |
0.9508 |
328.15 |
845.05 |
0.9513 |
318.15 |
856.25 |
0.9603 |
308.15 |
869.83 |
1.0000 |
288.15 |
903.31 |
1.0000 |
298.15 |
892.31 |
1.0000 |
308.15 |
881.19 |
1.0000 |
318.15 |
870.06 |
1.0000 |
328.15 |
858.8 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
Mole fraction of Butanoic acid, methyl ester (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0137 |
371.28 |
0.0320 |
370.95 |
0.0594 |
370.50 |
0.0848 |
370.08 |
0.1157 |
369.73 |
0.1460 |
369.39 |
0.1793 |
369.07 |
0.2169 |
368.76 |
0.2684 |
368.46 |
0.3037 |
368.36 |
0.3339 |
368.25 |
0.3629 |
368.23 |
0.4376 |
368.20 |
0.4623 |
368.24 |
0.4938 |
368.32 |
0.5344 |
368.47 |
0.5759 |
368.68 |
0.6212 |
368.98 |
0.6499 |
369.21 |
0.6932 |
369.62 |
0.7213 |
369.93 |
0.7651 |
370.49 |
0.8003 |
371.01 |
0.8514 |
371.90 |
0.8930 |
372.75 |
0.9406 |
373.89 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.32 (Liquid)
Mole fraction of Butanoic acid, methyl ester (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
371.38 |
0.0180 |
370.85 |
0.0280 |
370.64 |
0.0360 |
370.47 |
0.0440 |
370.32 |
0.0480 |
370.28 |
0.0570 |
370.11 |
0.0780 |
369.76 |
0.0920 |
369.55 |
0.1070 |
369.36 |
0.1170 |
369.23 |
0.1470 |
368.88 |
0.1560 |
368.81 |
0.1860 |
368.53 |
0.1960 |
368.45 |
0.2050 |
368.38 |
0.2180 |
368.30 |
0.2300 |
368.23 |
0.2460 |
368.13 |
0.2630 |
368.03 |
0.2800 |
367.97 |
0.2990 |
367.87 |
0.3170 |
367.82 |
0.3340 |
367.80 |
0.3570 |
367.75 |
0.3790 |
367.66 |
0.4040 |
367.65 |
0.4260 |
367.65 |
0.4470 |
367.66 |
0.4660 |
367.69 |
0.4860 |
367.72 |
0.5050 |
367.79 |
0.5240 |
367.84 |
0.5410 |
367.91 |
0.5590 |
367.99 |
0.5760 |
368.10 |
0.5910 |
368.18 |
0.6290 |
368.45 |
0.6630 |
368.62 |
0.6980 |
368.83 |
0.7360 |
369.17 |
0.7590 |
369.43 |
0.7820 |
369.71 |
0.8030 |
370.03 |
0.8300 |
370.46 |
0.8480 |
370.85 |
0.8610 |
371.04 |
0.8760 |
371.35 |
0.8880 |
371.63 |
0.8970 |
371.78 |
0.9050 |
372.03 |
0.9140 |
372.24 |
0.9480 |
373.22 |
0.9570 |
373.35 |
0.9690 |
373.90 |
0.9810 |
374.43 |
0.9920 |
374.97 |
1.0000 |
375.74 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
Mole fraction of Butanoic acid, methyl ester (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0137 |
371.28 |
0.0320 |
370.95 |
0.0594 |
370.50 |
0.0848 |
370.08 |
0.1157 |
369.73 |
0.1460 |
369.39 |
0.1793 |
369.07 |
0.2169 |
368.76 |
0.2684 |
368.46 |
0.3037 |
368.36 |
0.3339 |
368.25 |
0.3629 |
368.23 |
0.4376 |
368.20 |
0.4623 |
368.24 |
0.4938 |
368.32 |
0.5344 |
368.47 |
0.5759 |
368.68 |
0.6212 |
368.98 |
0.6499 |
369.21 |
0.6932 |
369.62 |
0.7213 |
369.93 |
0.7651 |
370.49 |
0.8003 |
371.01 |
0.8514 |
371.90 |
0.8930 |
372.75 |
0.9406 |
373.89 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.32 (Liquid)
Mole fraction of Butanoic acid, methyl ester (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
371.38 |
0.0180 |
370.85 |
0.0280 |
370.64 |
0.0360 |
370.47 |
0.0440 |
370.32 |
0.0480 |
370.28 |
0.0570 |
370.11 |
0.0780 |
369.76 |
0.0920 |
369.55 |
0.1070 |
369.36 |
0.1170 |
369.23 |
0.1470 |
368.88 |
0.1560 |
368.81 |
0.1860 |
368.53 |
0.1960 |
368.45 |
0.2050 |
368.38 |
0.2180 |
368.30 |
0.2300 |
368.23 |
0.2460 |
368.13 |
0.2630 |
368.03 |
0.2800 |
367.97 |
0.2990 |
367.87 |
0.3170 |
367.82 |
0.3340 |
367.80 |
0.3570 |
367.75 |
0.3790 |
367.66 |
0.4040 |
367.65 |
0.4260 |
367.65 |
0.4470 |
367.66 |
0.4660 |
367.69 |
0.4860 |
367.72 |
0.5050 |
367.79 |
0.5240 |
367.84 |
0.5410 |
367.91 |
0.5590 |
367.99 |
0.5760 |
368.10 |
0.5910 |
368.18 |
0.6290 |
368.45 |
0.6630 |
368.62 |
0.6980 |
368.83 |
0.7360 |
369.17 |
0.7590 |
369.43 |
0.7820 |
369.71 |
0.8030 |
370.03 |
0.8300 |
370.46 |
0.8480 |
370.85 |
0.8610 |
371.04 |
0.8760 |
371.35 |
0.8880 |
371.63 |
0.8970 |
371.78 |
0.9050 |
372.03 |
0.9140 |
372.24 |
0.9480 |
373.22 |
0.9570 |
373.35 |
0.9690 |
373.90 |
0.9810 |
374.43 |
0.9920 |
374.97 |
1.0000 |
375.74 |
Sources