Mixture of Propanoic acid, ethyl ester + Nonane
Datasets
-
Excess molar enthalpy (molar enthalpy (2)
-
ρl - Mass density, kg/m3 (2)
-
Excess molar volume, m3/mol (2)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 318.15 (Liquid)
Mole fraction of Propanoic acid, ethyl ester (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.0817 |
0.3848 |
0.1719 |
0.7047 |
0.2598 |
0.9665 |
0.3403 |
1.1385 |
0.4145 |
1.2435 |
0.4797 |
1.2916 |
0.4909 |
1.3019 |
0.5379 |
1.2961 |
0.5764 |
1.275 |
0.5876 |
1.2673 |
0.6277 |
1.2176 |
0.6791 |
1.133 |
0.7320 |
1.0156 |
0.7883 |
0.8664 |
0.8451 |
0.6801 |
0.9016 |
0.4641 |
0.9517 |
0.2466 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 318.15 (Liquid)
Mole fraction of Propanoic acid, ethyl ester (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.0817 |
0.3848 |
0.1719 |
0.7047 |
0.2598 |
0.9665 |
0.3403 |
1.1385 |
0.4145 |
1.2435 |
0.4797 |
1.2916 |
0.4909 |
1.3019 |
0.5379 |
1.2961 |
0.5764 |
1.275 |
0.5876 |
1.2673 |
0.6277 |
1.2176 |
0.6791 |
1.133 |
0.7320 |
1.0156 |
0.7883 |
0.8664 |
0.8451 |
0.6801 |
0.9016 |
0.4641 |
0.9517 |
0.2466 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Propanoic acid, ethyl ester (1) - Liquid |
Mass density, kg/m3 - Liquid |
288.15 |
0.0000 |
721.65 |
288.15 |
0.0545 |
727.07 |
288.15 |
0.1159 |
733.36 |
288.15 |
0.1434 |
736.52 |
288.15 |
0.2218 |
745.49 |
288.15 |
0.2412 |
747.88 |
288.15 |
0.3158 |
757.46 |
288.15 |
0.3579 |
763.17 |
288.15 |
0.4121 |
770.89 |
288.15 |
0.4620 |
778.51 |
288.15 |
0.5039 |
785.25 |
288.15 |
0.5537 |
793.58 |
288.15 |
0.6035 |
802.47 |
288.15 |
0.6328 |
807.91 |
288.15 |
0.6935 |
819.81 |
288.15 |
0.7463 |
830.79 |
288.15 |
0.7907 |
840.69 |
288.15 |
0.8950 |
866.09 |
288.15 |
0.9488 |
880.62 |
288.15 |
1.0000 |
895.58 |
298.15 |
0.0000 |
713.85 |
298.15 |
0.0538 |
718.94 |
298.15 |
0.0883 |
722.45 |
298.15 |
0.1420 |
728.05 |
298.15 |
0.2152 |
736.31 |
298.15 |
0.3007 |
746.83 |
298.15 |
0.3555 |
754.11 |
298.15 |
0.4078 |
761.4 |
298.15 |
0.4592 |
769.02 |
298.15 |
0.4988 |
775.19 |
298.15 |
0.5511 |
783.72 |
298.15 |
0.5917 |
790.84 |
298.15 |
0.6562 |
802.56 |
298.15 |
0.6962 |
810.32 |
298.15 |
0.7410 |
819.48 |
298.15 |
0.7883 |
829.57 |
298.15 |
0.8559 |
845.47 |
298.15 |
0.9034 |
857.27 |
298.15 |
0.9521 |
870.29 |
298.15 |
1.0000 |
884.15 |
308.15 |
0.0000 |
705.96 |
308.15 |
0.0558 |
711.17 |
308.15 |
0.0890 |
714.43 |
308.15 |
0.1555 |
721.34 |
308.15 |
0.2171 |
728.16 |
308.15 |
0.2586 |
733.03 |
308.15 |
0.3081 |
739.12 |
308.15 |
0.3829 |
748.94 |
308.15 |
0.4013 |
751.5 |
308.15 |
0.4533 |
759.02 |
308.15 |
0.5068 |
767.11 |
308.15 |
0.5509 |
774.2 |
308.15 |
0.6035 |
783.03 |
308.15 |
0.6525 |
791.81 |
308.15 |
0.6998 |
800.82 |
308.15 |
0.7473 |
810.39 |
308.15 |
0.7940 |
820.41 |
308.15 |
0.8533 |
833.93 |
308.15 |
0.9006 |
845.51 |
308.15 |
0.9506 |
858.66 |
308.15 |
1.0000 |
872.62 |
318.15 |
0.0000 |
698.06 |
318.15 |
0.0516 |
702.64 |
318.15 |
0.0909 |
706.6 |
318.15 |
0.1617 |
713.7 |
318.15 |
0.2190 |
719.88 |
318.15 |
0.2413 |
722.49 |
318.15 |
0.2923 |
728.44 |
318.15 |
0.3518 |
735.96 |
318.15 |
0.4062 |
743.15 |
318.15 |
0.4541 |
749.92 |
318.15 |
0.5056 |
757.57 |
318.15 |
0.5560 |
765.57 |
318.15 |
0.6001 |
772.83 |
318.15 |
0.6514 |
781.78 |
318.15 |
0.6939 |
789.72 |
318.15 |
0.7552 |
801.69 |
318.15 |
0.7988 |
810.87 |
318.15 |
0.8559 |
823.94 |
318.15 |
0.9062 |
835.91 |
318.15 |
0.9524 |
847.95 |
318.15 |
1.0000 |
861.08 |
328.15 |
0.0000 |
690.17 |
328.15 |
0.0514 |
694.83 |
328.15 |
0.0965 |
699.04 |
328.15 |
0.1572 |
705.05 |
328.15 |
0.2061 |
710.14 |
328.15 |
0.2627 |
716.42 |
328.15 |
0.3163 |
722.76 |
328.15 |
0.3619 |
728.36 |
328.15 |
0.4059 |
734.14 |
328.15 |
0.4602 |
741.6 |
328.15 |
0.5053 |
748.09 |
328.15 |
0.5543 |
755.65 |
328.15 |
0.6024 |
763.42 |
328.15 |
0.6525 |
772.01 |
328.15 |
0.6996 |
780.61 |
328.15 |
0.7535 |
791.02 |
328.15 |
0.8019 |
801.0 |
328.15 |
0.8606 |
813.96 |
328.15 |
0.8933 |
821.83 |
328.15 |
0.9504 |
836.0 |
328.15 |
1.0000 |
849.41 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Propanoic acid, ethyl ester (1) - Liquid |
Mass density, kg/m3 - Liquid |
288.15 |
0.0000 |
721.65 |
288.15 |
0.0545 |
727.07 |
288.15 |
0.1159 |
733.36 |
288.15 |
0.1434 |
736.52 |
288.15 |
0.2218 |
745.49 |
288.15 |
0.2412 |
747.88 |
288.15 |
0.3158 |
757.46 |
288.15 |
0.3579 |
763.17 |
288.15 |
0.4121 |
770.89 |
288.15 |
0.4620 |
778.51 |
288.15 |
0.5039 |
785.25 |
288.15 |
0.5537 |
793.58 |
288.15 |
0.6035 |
802.47 |
288.15 |
0.6328 |
807.91 |
288.15 |
0.6935 |
819.81 |
288.15 |
0.7463 |
830.79 |
288.15 |
0.7907 |
840.69 |
288.15 |
0.8950 |
866.09 |
288.15 |
0.9488 |
880.62 |
288.15 |
1.0000 |
895.58 |
298.15 |
0.0000 |
713.85 |
298.15 |
0.0538 |
718.94 |
298.15 |
0.0883 |
722.45 |
298.15 |
0.1420 |
728.05 |
298.15 |
0.2152 |
736.31 |
298.15 |
0.3007 |
746.83 |
298.15 |
0.3555 |
754.11 |
298.15 |
0.4078 |
761.4 |
298.15 |
0.4592 |
769.02 |
298.15 |
0.4988 |
775.19 |
298.15 |
0.5511 |
783.72 |
298.15 |
0.5917 |
790.84 |
298.15 |
0.6562 |
802.56 |
298.15 |
0.6962 |
810.32 |
298.15 |
0.7410 |
819.48 |
298.15 |
0.7883 |
829.57 |
298.15 |
0.8559 |
845.47 |
298.15 |
0.9034 |
857.27 |
298.15 |
0.9521 |
870.29 |
298.15 |
1.0000 |
884.15 |
308.15 |
0.0000 |
705.96 |
308.15 |
0.0558 |
711.17 |
308.15 |
0.0890 |
714.43 |
308.15 |
0.1555 |
721.34 |
308.15 |
0.2171 |
728.16 |
308.15 |
0.2586 |
733.03 |
308.15 |
0.3081 |
739.12 |
308.15 |
0.3829 |
748.94 |
308.15 |
0.4013 |
751.5 |
308.15 |
0.4533 |
759.02 |
308.15 |
0.5068 |
767.11 |
308.15 |
0.5509 |
774.2 |
308.15 |
0.6035 |
783.03 |
308.15 |
0.6525 |
791.81 |
308.15 |
0.6998 |
800.82 |
308.15 |
0.7473 |
810.39 |
308.15 |
0.7940 |
820.41 |
308.15 |
0.8533 |
833.93 |
308.15 |
0.9006 |
845.51 |
308.15 |
0.9506 |
858.66 |
308.15 |
1.0000 |
872.62 |
318.15 |
0.0000 |
698.06 |
318.15 |
0.0516 |
702.64 |
318.15 |
0.0909 |
706.6 |
318.15 |
0.1617 |
713.7 |
318.15 |
0.2190 |
719.88 |
318.15 |
0.2413 |
722.49 |
318.15 |
0.2923 |
728.44 |
318.15 |
0.3518 |
735.96 |
318.15 |
0.4062 |
743.15 |
318.15 |
0.4541 |
749.92 |
318.15 |
0.5056 |
757.57 |
318.15 |
0.5560 |
765.57 |
318.15 |
0.6001 |
772.83 |
318.15 |
0.6514 |
781.78 |
318.15 |
0.6939 |
789.72 |
318.15 |
0.7552 |
801.69 |
318.15 |
0.7988 |
810.87 |
318.15 |
0.8559 |
823.94 |
318.15 |
0.9062 |
835.91 |
318.15 |
0.9524 |
847.95 |
318.15 |
1.0000 |
861.08 |
328.15 |
0.0000 |
690.17 |
328.15 |
0.0514 |
694.83 |
328.15 |
0.0965 |
699.04 |
328.15 |
0.1572 |
705.05 |
328.15 |
0.2061 |
710.14 |
328.15 |
0.2627 |
716.42 |
328.15 |
0.3163 |
722.76 |
328.15 |
0.3619 |
728.36 |
328.15 |
0.4059 |
734.14 |
328.15 |
0.4602 |
741.6 |
328.15 |
0.5053 |
748.09 |
328.15 |
0.5543 |
755.65 |
328.15 |
0.6024 |
763.42 |
328.15 |
0.6525 |
772.01 |
328.15 |
0.6996 |
780.61 |
328.15 |
0.7535 |
791.02 |
328.15 |
0.8019 |
801.0 |
328.15 |
0.8606 |
813.96 |
328.15 |
0.8933 |
821.83 |
328.15 |
0.9504 |
836.0 |
328.15 |
1.0000 |
849.41 |
Excess molar volume, m3/mol
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 318.15 (Liquid)
Mole fraction of Propanoic acid, ethyl ester (1) - Liquid |
Excess molar volume, m3/mol - Liquid |
0.0376 |
1.6500e-07 |
0.0926 |
3.5800e-07 |
0.1744 |
6.1800e-07 |
0.2554 |
8.2000e-07 |
0.3255 |
9.4300e-07 |
0.3925 |
1.0220e-06 |
0.4570 |
1.0750e-06 |
0.5230 |
1.0770e-06 |
0.5826 |
1.0660e-06 |
0.6348 |
1.0270e-06 |
0.6882 |
9.4700e-07 |
0.7398 |
8.5200e-07 |
0.7883 |
7.5700e-07 |
0.8344 |
6.2600e-07 |
0.8780 |
5.0100e-07 |
0.9181 |
3.4100e-07 |
0.9584 |
1.8100e-07 |
Excess molar volume, m3/mol
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 318.15 (Liquid)
Mole fraction of Propanoic acid, ethyl ester (1) - Liquid |
Excess molar volume, m3/mol - Liquid |
0.0376 |
1.6500e-07 |
0.0926 |
3.5800e-07 |
0.1744 |
6.1800e-07 |
0.2554 |
8.2000e-07 |
0.3255 |
9.4300e-07 |
0.3925 |
1.0220e-06 |
0.4570 |
1.0750e-06 |
0.5230 |
1.0770e-06 |
0.5826 |
1.0660e-06 |
0.6348 |
1.0270e-06 |
0.6882 |
9.4700e-07 |
0.7398 |
8.5200e-07 |
0.7883 |
7.5700e-07 |
0.8344 |
6.2600e-07 |
0.8780 |
5.0100e-07 |
0.9181 |
3.4100e-07 |
0.9584 |
1.8100e-07 |
Sources