Datasets
-
Interfacial tension, N/m (6)
-
ρl - Mass density, kg/m3 (8)
-
Tboil - Boiling temperature at pressure P, K (2)
Interfacial tension, N/m
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Decane (2) - Liquid |
Interfacial tension, N/m - Liquid |
| 298.15 |
0.0080 |
0.0335 |
| 298.15 |
0.0110 |
0.0331 |
| 298.15 |
0.0140 |
0.0322 |
| 298.15 |
0.0200 |
0.0305 |
| 298.15 |
0.0260 |
0.0294 |
| 298.15 |
0.9560 |
0.0231 |
| 298.15 |
0.9600 |
0.0231 |
| 298.15 |
0.9670 |
0.0233 |
| 298.15 |
0.9690 |
0.0231 |
| 298.15 |
0.9730 |
0.0231 |
| 298.15 |
0.9820 |
0.0230 |
| 298.15 |
1.0000 |
0.0234 |
| 318.15 |
0.0110 |
0.0312 |
| 318.15 |
0.0120 |
0.0310 |
| 318.15 |
0.0140 |
0.0305 |
| 318.15 |
0.0200 |
0.0290 |
| 318.15 |
0.0300 |
0.0272 |
| 318.15 |
0.9560 |
0.0217 |
| 318.15 |
0.9600 |
0.0218 |
| 318.15 |
0.9670 |
0.0218 |
| 318.15 |
0.9690 |
0.0216 |
| 318.15 |
0.9840 |
0.0216 |
| 318.15 |
1.0000 |
0.0216 |
Interfacial tension, N/m
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Interfacial tension, N/m - Liquid mixture 1 |
| 298.15 |
0.0034 |
| 298.68 |
0.0033 |
| 305.65 |
0.0029 |
| 313.15 |
0.0025 |
| 320.65 |
0.0021 |
| 328.15 |
0.0016 |
Interfacial tension, N/m
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Interfacial tension, N/m - Liquid mixture 1 |
| 292.78 |
0.0038 |
| 297.77 |
0.0034 |
| 302.79 |
0.0031 |
| 307.81 |
0.0027 |
| 312.79 |
0.0024 |
| 317.80 |
0.0021 |
| 322.78 |
0.0018 |
| 327.81 |
0.0015 |
| 332.81 |
0.0012 |
| 337.76 |
0.0009 |
| 342.78 |
0.0007 |
| 346.80 |
0.0005 |
| 348.32 |
0.0004 |
| 350.11 |
0.0003 |
| 352.77 |
0.0002 |
| 353.65 |
0.0001 |
| 354.76 |
0.0001 |
| 355.31 |
0.0001 |
| 355.62 |
0.0001 |
| 356.15 |
0.0001 |
| 356.72 |
0.0000 |
| 357.15 |
0.0000 |
| 357.45 |
0.0000 |
Interfacial tension, N/m
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Decane (2) - Liquid |
Interfacial tension, N/m - Liquid |
| 298.15 |
0.0080 |
0.0335 |
| 298.15 |
0.0110 |
0.0331 |
| 298.15 |
0.0140 |
0.0322 |
| 298.15 |
0.0200 |
0.0305 |
| 298.15 |
0.0260 |
0.0294 |
| 298.15 |
0.9560 |
0.0231 |
| 298.15 |
0.9600 |
0.0231 |
| 298.15 |
0.9670 |
0.0233 |
| 298.15 |
0.9690 |
0.0231 |
| 298.15 |
0.9730 |
0.0231 |
| 298.15 |
0.9820 |
0.0230 |
| 298.15 |
1.0000 |
0.0234 |
| 318.15 |
0.0110 |
0.0312 |
| 318.15 |
0.0120 |
0.0310 |
| 318.15 |
0.0140 |
0.0305 |
| 318.15 |
0.0200 |
0.0290 |
| 318.15 |
0.0300 |
0.0272 |
| 318.15 |
0.9560 |
0.0217 |
| 318.15 |
0.9600 |
0.0218 |
| 318.15 |
0.9670 |
0.0218 |
| 318.15 |
0.9690 |
0.0216 |
| 318.15 |
0.9840 |
0.0216 |
| 318.15 |
1.0000 |
0.0216 |
Interfacial tension, N/m
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Interfacial tension, N/m - Liquid mixture 1 |
| 298.15 |
0.0034 |
| 298.68 |
0.0033 |
| 305.65 |
0.0029 |
| 313.15 |
0.0025 |
| 320.65 |
0.0021 |
| 328.15 |
0.0016 |
Interfacial tension, N/m
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Interfacial tension, N/m - Liquid mixture 1 |
| 292.78 |
0.0038 |
| 297.77 |
0.0034 |
| 302.79 |
0.0031 |
| 307.81 |
0.0027 |
| 312.79 |
0.0024 |
| 317.80 |
0.0021 |
| 322.78 |
0.0018 |
| 327.81 |
0.0015 |
| 332.81 |
0.0012 |
| 337.76 |
0.0009 |
| 342.78 |
0.0007 |
| 346.80 |
0.0005 |
| 348.32 |
0.0004 |
| 350.11 |
0.0003 |
| 352.77 |
0.0002 |
| 353.65 |
0.0001 |
| 354.76 |
0.0001 |
| 355.31 |
0.0001 |
| 355.62 |
0.0001 |
| 356.15 |
0.0001 |
| 356.72 |
0.0000 |
| 357.15 |
0.0000 |
| 357.45 |
0.0000 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Decane (2) - Liquid |
Mass density, kg/m3 - Liquid |
| 298.15 |
0.0080 |
939.869 |
| 298.15 |
0.0110 |
937.865 |
| 298.15 |
0.0120 |
937.754 |
| 298.15 |
0.0140 |
935.997 |
| 298.15 |
0.0200 |
932.672 |
| 298.15 |
0.0260 |
929.604 |
| 298.15 |
0.0270 |
928.627 |
| 298.15 |
0.0270 |
928.403 |
| 298.15 |
0.9520 |
729.502 |
| 298.15 |
0.9560 |
729.111 |
| 298.15 |
0.9560 |
729.084 |
| 298.15 |
0.9600 |
728.92 |
| 298.15 |
0.9650 |
728.525 |
| 298.15 |
0.9670 |
728.316 |
| 298.15 |
0.9690 |
728.15 |
| 298.15 |
0.9730 |
727.882 |
| 298.15 |
0.9820 |
726.924 |
| 298.15 |
1.0000 |
725.808 |
| 318.15 |
0.0080 |
920.158 |
| 318.15 |
0.0110 |
918.716 |
| 318.15 |
0.0120 |
918.34 |
| 318.15 |
0.0140 |
916.657 |
| 318.15 |
0.0200 |
913.554 |
| 318.15 |
0.0260 |
910.926 |
| 318.15 |
0.0270 |
910.315 |
| 318.15 |
0.0300 |
908.389 |
| 318.15 |
0.9250 |
715.777 |
| 318.15 |
0.9520 |
713.975 |
| 318.15 |
0.9560 |
713.547 |
| 318.15 |
0.9560 |
713.589 |
| 318.15 |
0.9600 |
713.428 |
| 318.15 |
0.9650 |
713.114 |
| 318.15 |
0.9670 |
712.779 |
| 318.15 |
0.9690 |
712.744 |
| 318.15 |
0.9730 |
712.535 |
| 318.15 |
0.9820 |
711.547 |
| 318.15 |
0.9840 |
711.771 |
| 318.15 |
1.0000 |
710.486 |
Mass density, kg/m3
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Mass density, kg/m3 - Liquid mixture 2 |
Mass density, kg/m3 - Liquid mixture 1 |
| 298.15 |
926.81 |
731.66 |
| 298.68 |
926.07 |
731.37 |
| 305.65 |
916.16 |
727.15 |
| 313.15 |
905.72 |
722.45 |
| 320.65 |
894.2 |
719.66 |
| 328.15 |
882.61 |
718.11 |
Mass density, kg/m3
[ref]
| Temperature, K - Liquid mixture 1 |
Mass density, kg/m3 - Liquid mixture 1 |
| 298.16 |
731.5 |
| 303.15 |
728.3 |
| 308.15 |
726.0 |
| 313.15 |
723.8 |
| 318.16 |
721.7 |
| 323.16 |
719.4 |
| 328.15 |
718.0 |
| 333.15 |
716.3 |
| 338.15 |
716.2 |
| 340.66 |
716.6 |
| 343.15 |
717.0 |
| 345.65 |
717.7 |
| 348.15 |
719.0 |
| 348.16 |
719.0 |
| 350.66 |
721.0 |
| 350.66 |
721.0 |
| 353.15 |
724.8 |
| 354.15 |
726.9 |
| 355.15 |
729.5 |
| 356.16 |
733.3 |
| 357.16 |
739.7 |
| 357.65 |
744.9 |
| 357.75 |
746.2 |
| 357.85 |
746.3 |
| 357.96 |
749.1 |
Mass density, kg/m3
[ref]
| Temperature, K - Liquid mixture 2 |
Mass density, kg/m3 - Liquid mixture 2 |
| 298.16 |
925.6 |
| 303.15 |
918.8 |
| 308.15 |
911.8 |
| 313.15 |
904.6 |
| 318.16 |
897.0 |
| 323.16 |
889.0 |
| 328.15 |
880.5 |
| 333.15 |
871.2 |
| 338.15 |
861.4 |
| 340.66 |
855.7 |
| 343.15 |
849.6 |
| 345.65 |
842.9 |
| 348.15 |
836.2 |
| 348.16 |
835.7 |
| 350.66 |
827.4 |
| 350.66 |
828.0 |
| 353.15 |
817.7 |
| 354.15 |
813.4 |
| 355.15 |
807.8 |
| 356.16 |
801.5 |
| 357.16 |
792.6 |
| 357.65 |
785.6 |
| 357.75 |
784.1 |
| 357.85 |
784.0 |
| 357.96 |
780.9 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Decane (2) - Liquid |
Mass density, kg/m3 - Liquid |
| 298.15 |
0.0080 |
939.869 |
| 298.15 |
0.0110 |
937.865 |
| 298.15 |
0.0120 |
937.754 |
| 298.15 |
0.0140 |
935.997 |
| 298.15 |
0.0200 |
932.672 |
| 298.15 |
0.0260 |
929.604 |
| 298.15 |
0.0270 |
928.627 |
| 298.15 |
0.0270 |
928.403 |
| 298.15 |
0.9520 |
729.502 |
| 298.15 |
0.9560 |
729.111 |
| 298.15 |
0.9560 |
729.084 |
| 298.15 |
0.9600 |
728.92 |
| 298.15 |
0.9650 |
728.525 |
| 298.15 |
0.9670 |
728.316 |
| 298.15 |
0.9690 |
728.15 |
| 298.15 |
0.9730 |
727.882 |
| 298.15 |
0.9820 |
726.924 |
| 298.15 |
1.0000 |
725.808 |
| 318.15 |
0.0080 |
920.158 |
| 318.15 |
0.0110 |
918.716 |
| 318.15 |
0.0120 |
918.34 |
| 318.15 |
0.0140 |
916.657 |
| 318.15 |
0.0200 |
913.554 |
| 318.15 |
0.0260 |
910.926 |
| 318.15 |
0.0270 |
910.315 |
| 318.15 |
0.0300 |
908.389 |
| 318.15 |
0.9250 |
715.777 |
| 318.15 |
0.9520 |
713.975 |
| 318.15 |
0.9560 |
713.547 |
| 318.15 |
0.9560 |
713.589 |
| 318.15 |
0.9600 |
713.428 |
| 318.15 |
0.9650 |
713.114 |
| 318.15 |
0.9670 |
712.779 |
| 318.15 |
0.9690 |
712.744 |
| 318.15 |
0.9730 |
712.535 |
| 318.15 |
0.9820 |
711.547 |
| 318.15 |
0.9840 |
711.771 |
| 318.15 |
1.0000 |
710.486 |
Mass density, kg/m3
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Mass density, kg/m3 - Liquid mixture 2 |
Mass density, kg/m3 - Liquid mixture 1 |
| 298.15 |
926.81 |
731.66 |
| 298.68 |
926.07 |
731.37 |
| 305.65 |
916.16 |
727.15 |
| 313.15 |
905.72 |
722.45 |
| 320.65 |
894.2 |
719.66 |
| 328.15 |
882.61 |
718.11 |
Mass density, kg/m3
[ref]
| Temperature, K - Liquid mixture 1 |
Mass density, kg/m3 - Liquid mixture 1 |
| 298.16 |
731.5 |
| 303.15 |
728.3 |
| 308.15 |
726.0 |
| 313.15 |
723.8 |
| 318.16 |
721.7 |
| 323.16 |
719.4 |
| 328.15 |
718.0 |
| 333.15 |
716.3 |
| 338.15 |
716.2 |
| 340.66 |
716.6 |
| 343.15 |
717.0 |
| 345.65 |
717.7 |
| 348.15 |
719.0 |
| 348.16 |
719.0 |
| 350.66 |
721.0 |
| 350.66 |
721.0 |
| 353.15 |
724.8 |
| 354.15 |
726.9 |
| 355.15 |
729.5 |
| 356.16 |
733.3 |
| 357.16 |
739.7 |
| 357.65 |
744.9 |
| 357.75 |
746.2 |
| 357.85 |
746.3 |
| 357.96 |
749.1 |
Mass density, kg/m3
[ref]
| Temperature, K - Liquid mixture 2 |
Mass density, kg/m3 - Liquid mixture 2 |
| 298.16 |
925.6 |
| 303.15 |
918.8 |
| 308.15 |
911.8 |
| 313.15 |
904.6 |
| 318.16 |
897.0 |
| 323.16 |
889.0 |
| 328.15 |
880.5 |
| 333.15 |
871.2 |
| 338.15 |
861.4 |
| 340.66 |
855.7 |
| 343.15 |
849.6 |
| 345.65 |
842.9 |
| 348.15 |
836.2 |
| 348.16 |
835.7 |
| 350.66 |
827.4 |
| 350.66 |
828.0 |
| 353.15 |
817.7 |
| 354.15 |
813.4 |
| 355.15 |
807.8 |
| 356.16 |
801.5 |
| 357.16 |
792.6 |
| 357.65 |
785.6 |
| 357.75 |
784.1 |
| 357.85 |
784.0 |
| 357.96 |
780.9 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
95.1 (Liquid)
| Mole fraction of Formamide, N,N-dimethyl- (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
444.95 |
| 0.2192 |
425.85 |
| 0.3597 |
421.25 |
| 0.4573 |
419.35 |
| 0.5291 |
418.45 |
| 0.5841 |
417.95 |
| 0.6740 |
417.45 |
| 0.6946 |
417.35 |
| 0.7165 |
417.25 |
| 0.7398 |
417.25 |
| 0.7697 |
417.15 |
| 0.7913 |
417.15 |
| 0.8198 |
417.15 |
| 0.8504 |
417.25 |
| 0.8834 |
417.45 |
| 0.8991 |
417.65 |
| 0.9578 |
418.75 |
| 1.0000 |
420.95 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
95.1 (Liquid)
| Mole fraction of Formamide, N,N-dimethyl- (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
444.95 |
| 0.2192 |
425.85 |
| 0.3597 |
421.25 |
| 0.4573 |
419.35 |
| 0.5291 |
418.45 |
| 0.5841 |
417.95 |
| 0.6740 |
417.45 |
| 0.6946 |
417.35 |
| 0.7165 |
417.25 |
| 0.7398 |
417.25 |
| 0.7697 |
417.15 |
| 0.7913 |
417.15 |
| 0.8198 |
417.15 |
| 0.8504 |
417.25 |
| 0.8834 |
417.45 |
| 0.8991 |
417.65 |
| 0.9578 |
418.75 |
| 1.0000 |
420.95 |
Sources