- Name
- Pentane, 2,2,4-trimethyl-
- InChI
- InChI=1S/C8H18/c1-7(2)6-8(3,4)5/h7H,6H2,1-5H3
- InChI Key
- NHTMVDHEPJAVLT-UHFFFAOYSA-N
- Formula
- C8H18
- SMILES
- CC(C)CC(C)(C)C
- Mol. Weight (g/mol)
- 114.23
- CAS
- 540-84-1
- Name
- Acetic acid, methyl ester
- InChI
- InChI=1S/C3H6O2/c1-3(4)5-2/h1-2H3
- InChI Key
- KXKVLQRXCPHEJC-UHFFFAOYSA-N
- Formula
- C3H6O2
- SMILES
- COC(C)=O
- Mol. Weight (g/mol)
- 74.08
- CAS
- 79-20-9
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Datasets
- Mole fraction (2)
- Excess molar enthalpy (molar enthalpy (2)
- ρl - Mass density, kg/m3 (4)
- Tboil - Boiling temperature at pressure P, K (2)
Mole fraction of Acetic acid, methyl ester (2) [ref]
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Gas | Mole fraction of Acetic acid, methyl ester (2) - Liquid | Mole fraction of Acetic acid, methyl ester (2) - Gas |
| 100.00 | 0.0000 | 0.0000 |
| 100.00 | 0.0390 | 0.2740 |
| 100.00 | 0.0640 | 0.3720 |
| 100.00 | 0.0890 | 0.4480 |
| 100.00 | 0.1130 | 0.5190 |
| 100.00 | 0.1410 | 0.5680 |
| 100.00 | 0.1760 | 0.6150 |
| 100.00 | 0.1990 | 0.6470 |
| 100.00 | 0.2310 | 0.6780 |
| 100.00 | 0.2560 | 0.6980 |
| 100.00 | 0.2870 | 0.7190 |
| 100.00 | 0.3210 | 0.7390 |
| 100.00 | 0.3620 | 0.7560 |
| 100.00 | 0.3870 | 0.7670 |
| 100.00 | 0.4170 | 0.7780 |
| 100.00 | 0.4360 | 0.7860 |
| 100.00 | 0.4570 | 0.7940 |
| 100.00 | 0.5010 | 0.8010 |
| 100.00 | 0.5190 | 0.8100 |
| 100.00 | 0.5710 | 0.8220 |
| 100.00 | 0.6180 | 0.8340 |
| 100.00 | 0.6600 | 0.8450 |
| 100.00 | 0.6940 | 0.8530 |
| 100.00 | 0.7340 | 0.8620 |
| 100.00 | 0.7670 | 0.8700 |
| 100.00 | 0.7940 | 0.8790 |
| 100.00 | 0.8270 | 0.8890 |
| 100.00 | 0.8530 | 0.8990 |
| 100.00 | 0.8830 | 0.9110 |
| 100.00 | 0.9060 | 0.9240 |
| 100.00 | 0.9300 | 0.9370 |
| 100.00 | 0.9460 | 0.9480 |
| 100.00 | 0.9570 | 0.9580 |
| 100.00 | 0.9680 | 0.9670 |
| 100.00 | 0.9830 | 0.9820 |
| 100.00 | 0.9950 | 0.9940 |
| 100.00 | 1.0000 | 1.0000 |
| 1500.00 | 0.0000 | 0.0000 |
| 1500.00 | 0.0260 | 0.0840 |
| 1500.00 | 0.0770 | 0.2190 |
| 1500.00 | 0.1120 | 0.2960 |
| 1500.00 | 0.1390 | 0.3440 |
| 1500.00 | 0.1730 | 0.4020 |
| 1500.00 | 0.2010 | 0.4400 |
| 1500.00 | 0.2280 | 0.4780 |
| 1500.00 | 0.2530 | 0.5150 |
| 1500.00 | 0.3050 | 0.5750 |
| 1500.00 | 0.3590 | 0.6240 |
| 1500.00 | 0.3850 | 0.6470 |
| 1500.00 | 0.4120 | 0.6700 |
| 1500.00 | 0.4620 | 0.7070 |
| 1500.00 | 0.4850 | 0.7210 |
| 1500.00 | 0.5100 | 0.7350 |
| 1500.00 | 0.5290 | 0.7450 |
| 1500.00 | 0.5550 | 0.7560 |
| 1500.00 | 0.5780 | 0.7700 |
| 1500.00 | 0.6140 | 0.7840 |
| 1500.00 | 0.6380 | 0.7980 |
| 1500.00 | 0.6630 | 0.8110 |
| 1500.00 | 0.6920 | 0.8260 |
| 1500.00 | 0.7240 | 0.8390 |
| 1500.00 | 0.7520 | 0.8540 |
| 1500.00 | 0.7850 | 0.8690 |
| 1500.00 | 0.8250 | 0.8920 |
| 1500.00 | 0.8640 | 0.9070 |
| 1500.00 | 0.8960 | 0.9270 |
| 1500.00 | 0.9180 | 0.9420 |
| 1500.00 | 0.9480 | 0.9590 |
| 1500.00 | 0.9840 | 0.9880 |
| 1500.00 | 0.9950 | 0.9960 |
| 1500.00 | 1.0000 | 1.0000 |
Mole fraction of Acetic acid, methyl ester (2) [ref]
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Gas | Mole fraction of Acetic acid, methyl ester (2) - Liquid | Mole fraction of Acetic acid, methyl ester (2) - Gas |
| 100.00 | 0.0000 | 0.0000 |
| 100.00 | 0.0390 | 0.2740 |
| 100.00 | 0.0640 | 0.3720 |
| 100.00 | 0.0890 | 0.4480 |
| 100.00 | 0.1130 | 0.5190 |
| 100.00 | 0.1410 | 0.5680 |
| 100.00 | 0.1760 | 0.6150 |
| 100.00 | 0.1990 | 0.6470 |
| 100.00 | 0.2310 | 0.6780 |
| 100.00 | 0.2560 | 0.6980 |
| 100.00 | 0.2870 | 0.7190 |
| 100.00 | 0.3210 | 0.7390 |
| 100.00 | 0.3620 | 0.7560 |
| 100.00 | 0.3870 | 0.7670 |
| 100.00 | 0.4170 | 0.7780 |
| 100.00 | 0.4360 | 0.7860 |
| 100.00 | 0.4570 | 0.7940 |
| 100.00 | 0.5010 | 0.8010 |
| 100.00 | 0.5190 | 0.8100 |
| 100.00 | 0.5710 | 0.8220 |
| 100.00 | 0.6180 | 0.8340 |
| 100.00 | 0.6600 | 0.8450 |
| 100.00 | 0.6940 | 0.8530 |
| 100.00 | 0.7340 | 0.8620 |
| 100.00 | 0.7670 | 0.8700 |
| 100.00 | 0.7940 | 0.8790 |
| 100.00 | 0.8270 | 0.8890 |
| 100.00 | 0.8530 | 0.8990 |
| 100.00 | 0.8830 | 0.9110 |
| 100.00 | 0.9060 | 0.9240 |
| 100.00 | 0.9300 | 0.9370 |
| 100.00 | 0.9460 | 0.9480 |
| 100.00 | 0.9570 | 0.9580 |
| 100.00 | 0.9680 | 0.9670 |
| 100.00 | 0.9830 | 0.9820 |
| 100.00 | 0.9950 | 0.9940 |
| 100.00 | 1.0000 | 1.0000 |
| 1500.00 | 0.0000 | 0.0000 |
| 1500.00 | 0.0260 | 0.0840 |
| 1500.00 | 0.0770 | 0.2190 |
| 1500.00 | 0.1120 | 0.2960 |
| 1500.00 | 0.1390 | 0.3440 |
| 1500.00 | 0.1730 | 0.4020 |
| 1500.00 | 0.2010 | 0.4400 |
| 1500.00 | 0.2280 | 0.4780 |
| 1500.00 | 0.2530 | 0.5150 |
| 1500.00 | 0.3050 | 0.5750 |
| 1500.00 | 0.3590 | 0.6240 |
| 1500.00 | 0.3850 | 0.6470 |
| 1500.00 | 0.4120 | 0.6700 |
| 1500.00 | 0.4620 | 0.7070 |
| 1500.00 | 0.4850 | 0.7210 |
| 1500.00 | 0.5100 | 0.7350 |
| 1500.00 | 0.5290 | 0.7450 |
| 1500.00 | 0.5550 | 0.7560 |
| 1500.00 | 0.5780 | 0.7700 |
| 1500.00 | 0.6140 | 0.7840 |
| 1500.00 | 0.6380 | 0.7980 |
| 1500.00 | 0.6630 | 0.8110 |
| 1500.00 | 0.6920 | 0.8260 |
| 1500.00 | 0.7240 | 0.8390 |
| 1500.00 | 0.7520 | 0.8540 |
| 1500.00 | 0.7850 | 0.8690 |
| 1500.00 | 0.8250 | 0.8920 |
| 1500.00 | 0.8640 | 0.9070 |
| 1500.00 | 0.8960 | 0.9270 |
| 1500.00 | 0.9180 | 0.9420 |
| 1500.00 | 0.9480 | 0.9590 |
| 1500.00 | 0.9840 | 0.9880 |
| 1500.00 | 0.9950 | 0.9960 |
| 1500.00 | 1.0000 | 1.0000 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Pentane, 2,2,4-trimethyl- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0200 | 0.1550 |
| 0.0525 | 0.4140 |
| 0.0892 | 0.6600 |
| 0.1241 | 0.8580 |
| 0.1687 | 1.047 |
| 0.2084 | 1.217 |
| 0.2560 | 1.385 |
| 0.3079 | 1.544 |
| 0.3608 | 1.659 |
| 0.3915 | 1.712 |
| 0.4323 | 1.763 |
| 0.4764 | 1.789 |
| 0.5406 | 1.759 |
| 0.6163 | 1.644 |
| 0.6888 | 1.456 |
| 0.7833 | 1.149 |
| 0.8597 | 0.7920 |
| 0.9422 | 0.3560 |
Mole fraction of Pentane, 2,2,4-trimethyl- (1)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
0
0.5
1
1.5
0
0.5
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Pentane, 2,2,4-trimethyl- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0200 | 0.1550 |
| 0.0525 | 0.4140 |
| 0.0892 | 0.6600 |
| 0.1241 | 0.8580 |
| 0.1687 | 1.047 |
| 0.2084 | 1.217 |
| 0.2560 | 1.385 |
| 0.3079 | 1.544 |
| 0.3608 | 1.659 |
| 0.3915 | 1.712 |
| 0.4323 | 1.763 |
| 0.4764 | 1.789 |
| 0.5406 | 1.759 |
| 0.6163 | 1.644 |
| 0.6888 | 1.456 |
| 0.7833 | 1.149 |
| 0.8597 | 0.7920 |
| 0.9422 | 0.3560 |
Mole fraction of Pentane, 2,2,4-trimethyl- (1)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
0
0.5
1
1.5
0
0.5
Mass density, kg/m3 [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 100 (Liquid)
| Mole fraction of Pentane, 2,2,4-trimethyl- (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0000 | 927.16 |
| 0.0375 | 906.89 |
| 0.1025 | 876.58 |
| 0.1652 | 851.09 |
| 0.1775 | 846.59 |
| 0.2189 | 832.07 |
| 0.2615 | 818.03 |
| 0.3020 | 805.95 |
| 0.3902 | 782.41 |
| 0.4061 | 778.52 |
| 0.4249 | 774.09 |
| 0.4627 | 765.54 |
| 0.5239 | 752.92 |
| 0.5411 | 749.57 |
| 0.6100 | 737.18 |
| 0.6612 | 728.76 |
| 0.6786 | 726.1 |
| 0.7359 | 717.6 |
| 0.8086 | 708.07 |
| 0.8803 | 699.86 |
| 0.9521 | 692.07 |
| 1.0000 | 687.75 |
Mole fraction of Pentane, 2,2,4-trimethyl- (1)
Mass density, kg/m3
700
750
800
850
900
950
0
0.5
1
Mass density, kg/m3 [ref]
Operational conditions:
- Pressure, kPa = 101.3 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Acetic acid, methyl ester (2) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0000 | 687.8 |
| 0.0646 | 693.5 |
| 0.0822 | 695.3 |
| 0.0859 | 695.7 |
| 0.0992 | 697.0 |
| 0.1566 | 703.6 |
| 0.1941 | 707.9 |
| 0.2080 | 709.7 |
| 0.2240 | 711.7 |
| 0.2636 | 717.1 |
| 0.2688 | 717.7 |
| 0.2957 | 721.6 |
| 0.3211 | 725.4 |
| 0.3319 | 727.0 |
| 0.3956 | 737.4 |
| 0.5015 | 757.3 |
| 0.5780 | 774.0 |
| 0.5792 | 774.3 |
| 0.6528 | 792.8 |
| 0.6958 | 804.5 |
| 0.7268 | 813.9 |
| 0.7611 | 824.8 |
| 0.7834 | 832.2 |
| 0.8161 | 843.6 |
| 0.8466 | 855.3 |
| 0.8480 | 855.8 |
| 0.8628 | 861.6 |
| 0.8632 | 861.9 |
| 0.8889 | 872.5 |
| 0.9179 | 885.5 |
| 0.9388 | 895.1 |
| 0.9406 | 895.7 |
| 0.9456 | 898.3 |
| 0.9574 | 904.3 |
| 1.0000 | 927.1 |
Mole fraction of Acetic acid, methyl ester (2)
Mass density, kg/m3
700
750
800
850
900
950
0
0.5
1
Mass density, kg/m3 [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 100 (Liquid)
| Mole fraction of Pentane, 2,2,4-trimethyl- (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0000 | 927.16 |
| 0.0375 | 906.89 |
| 0.1025 | 876.58 |
| 0.1652 | 851.09 |
| 0.1775 | 846.59 |
| 0.2189 | 832.07 |
| 0.2615 | 818.03 |
| 0.3020 | 805.95 |
| 0.3902 | 782.41 |
| 0.4061 | 778.52 |
| 0.4249 | 774.09 |
| 0.4627 | 765.54 |
| 0.5239 | 752.92 |
| 0.5411 | 749.57 |
| 0.6100 | 737.18 |
| 0.6612 | 728.76 |
| 0.6786 | 726.1 |
| 0.7359 | 717.6 |
| 0.8086 | 708.07 |
| 0.8803 | 699.86 |
| 0.9521 | 692.07 |
| 1.0000 | 687.75 |
Mole fraction of Pentane, 2,2,4-trimethyl- (1)
Mass density, kg/m3
700
750
800
850
900
950
0
0.5
1
Mass density, kg/m3 [ref]
Operational conditions:
- Pressure, kPa = 101.3 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Acetic acid, methyl ester (2) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0000 | 687.8 |
| 0.0646 | 693.5 |
| 0.0822 | 695.3 |
| 0.0859 | 695.7 |
| 0.0992 | 697.0 |
| 0.1566 | 703.6 |
| 0.1941 | 707.9 |
| 0.2080 | 709.7 |
| 0.2240 | 711.7 |
| 0.2636 | 717.1 |
| 0.2688 | 717.7 |
| 0.2957 | 721.6 |
| 0.3211 | 725.4 |
| 0.3319 | 727.0 |
| 0.3956 | 737.4 |
| 0.5015 | 757.3 |
| 0.5780 | 774.0 |
| 0.5792 | 774.3 |
| 0.6528 | 792.8 |
| 0.6958 | 804.5 |
| 0.7268 | 813.9 |
| 0.7611 | 824.8 |
| 0.7834 | 832.2 |
| 0.8161 | 843.6 |
| 0.8466 | 855.3 |
| 0.8480 | 855.8 |
| 0.8628 | 861.6 |
| 0.8632 | 861.9 |
| 0.8889 | 872.5 |
| 0.9179 | 885.5 |
| 0.9388 | 895.1 |
| 0.9406 | 895.7 |
| 0.9456 | 898.3 |
| 0.9574 | 904.3 |
| 1.0000 | 927.1 |
Mole fraction of Acetic acid, methyl ester (2)
Mass density, kg/m3
700
750
800
850
900
950
0
0.5
1
Boiling temperature at pressure P, K [ref]
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Acetic acid, methyl ester (2) - Liquid | Pressure, kPa - Liquid | Boiling temperature at pressure P, K - Liquid |
| 0.0000 | 100.00 | 371.91 |
| 0.0390 | 100.00 | 362.72 |
| 0.0640 | 100.00 | 358.41 |
| 0.0890 | 100.00 | 354.98 |
| 0.1130 | 100.00 | 351.68 |
| 0.1410 | 100.00 | 349.05 |
| 0.1760 | 100.00 | 346.17 |
| 0.1990 | 100.00 | 344.54 |
| 0.2310 | 100.00 | 342.49 |
| 0.2560 | 100.00 | 341.16 |
| 0.2870 | 100.00 | 339.82 |
| 0.3210 | 100.00 | 338.45 |
| 0.3620 | 100.00 | 337.32 |
| 0.3870 | 100.00 | 336.53 |
| 0.4170 | 100.00 | 335.80 |
| 0.4360 | 100.00 | 335.33 |
| 0.4570 | 100.00 | 334.85 |
| 0.5010 | 100.00 | 334.28 |
| 0.5190 | 100.00 | 333.77 |
| 0.5710 | 100.00 | 333.06 |
| 0.6180 | 100.00 | 332.41 |
| 0.6600 | 100.00 | 331.85 |
| 0.6940 | 100.00 | 331.50 |
| 0.7340 | 100.00 | 331.10 |
| 0.7670 | 100.00 | 330.79 |
| 0.7940 | 100.00 | 330.47 |
| 0.8270 | 100.00 | 330.20 |
| 0.8530 | 100.00 | 330.06 |
| 0.8830 | 100.00 | 329.84 |
| 0.9060 | 100.00 | 329.73 |
| 0.9300 | 100.00 | 329.61 |
| 0.9460 | 100.00 | 329.54 |
| 0.9570 | 100.00 | 329.52 |
| 0.9680 | 100.00 | 329.57 |
| 0.9830 | 100.00 | 329.71 |
| 0.9950 | 100.00 | 329.89 |
| 1.0000 | 100.00 | 329.99 |
| 0.0000 | 1500.00 | 504.65 |
| 0.0260 | 1500.00 | 499.45 |
| 0.0770 | 1500.00 | 490.75 |
| 0.1120 | 1500.00 | 485.75 |
| 0.1390 | 1500.00 | 482.05 |
| 0.1730 | 1500.00 | 477.95 |
| 0.2010 | 1500.00 | 474.85 |
| 0.2280 | 1500.00 | 471.76 |
| 0.2530 | 1500.00 | 468.88 |
| 0.3050 | 1500.00 | 464.20 |
| 0.3590 | 1500.00 | 459.75 |
| 0.3850 | 1500.00 | 457.78 |
| 0.4120 | 1500.00 | 456.09 |
| 0.4620 | 1500.00 | 452.91 |
| 0.4850 | 1500.00 | 451.60 |
| 0.5100 | 1500.00 | 450.36 |
| 0.5290 | 1500.00 | 449.62 |
| 0.5550 | 1500.00 | 448.73 |
| 0.5780 | 1500.00 | 447.79 |
| 0.6140 | 1500.00 | 446.38 |
| 0.6380 | 1500.00 | 445.63 |
| 0.6630 | 1500.00 | 444.45 |
| 0.6920 | 1500.00 | 443.54 |
| 0.7240 | 1500.00 | 442.73 |
| 0.7520 | 1500.00 | 441.92 |
| 0.7850 | 1500.00 | 441.01 |
| 0.8250 | 1500.00 | 439.94 |
| 0.8640 | 1500.00 | 438.80 |
| 0.8960 | 1500.00 | 437.97 |
| 0.9180 | 1500.00 | 437.59 |
| 0.9480 | 1500.00 | 436.85 |
| 0.9840 | 1500.00 | 436.34 |
| 0.9950 | 1500.00 | 436.17 |
| 1.0000 | 1500.00 | 436.08 |
Boiling temperature at pressure P, K [ref]
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Acetic acid, methyl ester (2) - Liquid | Pressure, kPa - Liquid | Boiling temperature at pressure P, K - Liquid |
| 0.0000 | 100.00 | 371.91 |
| 0.0390 | 100.00 | 362.72 |
| 0.0640 | 100.00 | 358.41 |
| 0.0890 | 100.00 | 354.98 |
| 0.1130 | 100.00 | 351.68 |
| 0.1410 | 100.00 | 349.05 |
| 0.1760 | 100.00 | 346.17 |
| 0.1990 | 100.00 | 344.54 |
| 0.2310 | 100.00 | 342.49 |
| 0.2560 | 100.00 | 341.16 |
| 0.2870 | 100.00 | 339.82 |
| 0.3210 | 100.00 | 338.45 |
| 0.3620 | 100.00 | 337.32 |
| 0.3870 | 100.00 | 336.53 |
| 0.4170 | 100.00 | 335.80 |
| 0.4360 | 100.00 | 335.33 |
| 0.4570 | 100.00 | 334.85 |
| 0.5010 | 100.00 | 334.28 |
| 0.5190 | 100.00 | 333.77 |
| 0.5710 | 100.00 | 333.06 |
| 0.6180 | 100.00 | 332.41 |
| 0.6600 | 100.00 | 331.85 |
| 0.6940 | 100.00 | 331.50 |
| 0.7340 | 100.00 | 331.10 |
| 0.7670 | 100.00 | 330.79 |
| 0.7940 | 100.00 | 330.47 |
| 0.8270 | 100.00 | 330.20 |
| 0.8530 | 100.00 | 330.06 |
| 0.8830 | 100.00 | 329.84 |
| 0.9060 | 100.00 | 329.73 |
| 0.9300 | 100.00 | 329.61 |
| 0.9460 | 100.00 | 329.54 |
| 0.9570 | 100.00 | 329.52 |
| 0.9680 | 100.00 | 329.57 |
| 0.9830 | 100.00 | 329.71 |
| 0.9950 | 100.00 | 329.89 |
| 1.0000 | 100.00 | 329.99 |
| 0.0000 | 1500.00 | 504.65 |
| 0.0260 | 1500.00 | 499.45 |
| 0.0770 | 1500.00 | 490.75 |
| 0.1120 | 1500.00 | 485.75 |
| 0.1390 | 1500.00 | 482.05 |
| 0.1730 | 1500.00 | 477.95 |
| 0.2010 | 1500.00 | 474.85 |
| 0.2280 | 1500.00 | 471.76 |
| 0.2530 | 1500.00 | 468.88 |
| 0.3050 | 1500.00 | 464.20 |
| 0.3590 | 1500.00 | 459.75 |
| 0.3850 | 1500.00 | 457.78 |
| 0.4120 | 1500.00 | 456.09 |
| 0.4620 | 1500.00 | 452.91 |
| 0.4850 | 1500.00 | 451.60 |
| 0.5100 | 1500.00 | 450.36 |
| 0.5290 | 1500.00 | 449.62 |
| 0.5550 | 1500.00 | 448.73 |
| 0.5780 | 1500.00 | 447.79 |
| 0.6140 | 1500.00 | 446.38 |
| 0.6380 | 1500.00 | 445.63 |
| 0.6630 | 1500.00 | 444.45 |
| 0.6920 | 1500.00 | 443.54 |
| 0.7240 | 1500.00 | 442.73 |
| 0.7520 | 1500.00 | 441.92 |
| 0.7850 | 1500.00 | 441.01 |
| 0.8250 | 1500.00 | 439.94 |
| 0.8640 | 1500.00 | 438.80 |
| 0.8960 | 1500.00 | 437.97 |
| 0.9180 | 1500.00 | 437.59 |
| 0.9480 | 1500.00 | 436.85 |
| 0.9840 | 1500.00 | 436.34 |
| 0.9950 | 1500.00 | 436.17 |
| 1.0000 | 1500.00 | 436.08 |
Sources
- A Study on Alkane + Ester + Ester Systems. Physicochemical Behavior of Binaries and Ternaries of Octane or Iso-octane with Methyl Esters (Ethanoate, Butanoate, Pentanoate)
- Measurement of VLE Data by Using an Experimental Installation with Automatic Control: Modeling of Binary Systems of Methyl Acetate or Ethyl Acetate with n-Heptane or 2,2,4-Trimethylpentane at Both 0.1 and 1.5 MPa