Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Formamide, N,N-dimethyl- (1) - Liquid mixture 1 |
---|---|
298.15 | 0.0660 |
303.15 | 0.0830 |
Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Pentane, 2-methyl- (2) - Liquid mixture 2 |
---|---|
298.15 | 0.1030 |
303.15 | 0.1210 |
Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Pentane, 2-methyl- (2) - Liquid mixture 1 |
---|---|
283.15 | 0.0700 |
288.15 | 0.0810 |
293.15 | 0.0960 |
298.15 | 0.1020 |
303.15 | 0.1190 |
308.15 | 0.1420 |
313.15 | 0.1540 |
Operational condition: Pressure, kPa = 101.325 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 | Mole fraction of Pentane, 2-methyl- (2) - Liquid mixture 2 |
---|---|
283.15 | 0.9590 |
288.15 | 0.9590 |
293.15 | 0.9410 |
298.15 | 0.9320 |
303.15 | 0.9210 |
308.15 | 0.9000 |
313.15 | 0.8850 |
Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Pentane, 2-methyl- (2) - Liquid mixture 1 |
---|---|
293.15 | 0.0980 |
298.15 | 0.1040 |
303.15 | 0.1230 |
308.15 | 0.1420 |
313.15 | 0.1580 |
318.15 | 0.1780 |
323.15 | 0.2040 |
Operational condition: Pressure, kPa = 101.325 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 | Mole fraction of Pentane, 2-methyl- (2) - Liquid mixture 2 |
---|---|
293.15 | 0.9450 |
298.15 | 0.9350 |
303.15 | 0.9130 |
308.15 | 0.9060 |
313.15 | 0.8880 |
318.15 | 0.8690 |
323.15 | 0.8380 |
Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Formamide, N,N-dimethyl- (1) - Liquid mixture 1 |
---|---|
298.15 | 0.0660 |
303.15 | 0.0830 |
Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Pentane, 2-methyl- (2) - Liquid mixture 2 |
---|---|
298.15 | 0.1030 |
303.15 | 0.1210 |
Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Pentane, 2-methyl- (2) - Liquid mixture 1 |
---|---|
283.15 | 0.0700 |
288.15 | 0.0810 |
293.15 | 0.0960 |
298.15 | 0.1020 |
303.15 | 0.1190 |
308.15 | 0.1420 |
313.15 | 0.1540 |
Operational condition: Pressure, kPa = 101.325 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 | Mole fraction of Pentane, 2-methyl- (2) - Liquid mixture 2 |
---|---|
283.15 | 0.9590 |
288.15 | 0.9590 |
293.15 | 0.9410 |
298.15 | 0.9320 |
303.15 | 0.9210 |
308.15 | 0.9000 |
313.15 | 0.8850 |
Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Pentane, 2-methyl- (2) - Liquid mixture 1 |
---|---|
293.15 | 0.0980 |
298.15 | 0.1040 |
303.15 | 0.1230 |
308.15 | 0.1420 |
313.15 | 0.1580 |
318.15 | 0.1780 |
323.15 | 0.2040 |
Operational condition: Pressure, kPa = 101.325 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 | Mole fraction of Pentane, 2-methyl- (2) - Liquid mixture 2 |
---|---|
293.15 | 0.9450 |
298.15 | 0.9350 |
303.15 | 0.9130 |
308.15 | 0.9060 |
313.15 | 0.8880 |
318.15 | 0.8690 |
323.15 | 0.8380 |
Operational condition: Pressure, kPa = 101.325 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Pentane, 2-methyl- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.15 | 0.0300 | 0.2304 |
298.15 | 0.0611 | 0.4386 |
298.15 | 0.0613 | 0.4410 |
298.15 | 0.0940 | 0.6452 |
298.15 | 0.9462 | 0.4672 |
313.15 | 0.0300 | 0.2307 |
313.15 | 0.0611 | 0.4485 |
313.15 | 0.0613 | 0.4513 |
313.15 | 0.0940 | 0.6565 |
313.15 | 0.1281 | 0.8458 |
313.15 | 0.9178 | 0.7285 |
313.15 | 0.9462 | 0.4730 |
313.15 | 0.9469 | 0.4614 |
Operational condition: Pressure, kPa = 101.325 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Pentane, 2-methyl- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.15 | 0.0300 | 0.2304 |
298.15 | 0.0611 | 0.4386 |
298.15 | 0.0613 | 0.4410 |
298.15 | 0.0940 | 0.6452 |
298.15 | 0.9462 | 0.4672 |
313.15 | 0.0300 | 0.2307 |
313.15 | 0.0611 | 0.4485 |
313.15 | 0.0613 | 0.4513 |
313.15 | 0.0940 | 0.6565 |
313.15 | 0.1281 | 0.8458 |
313.15 | 0.9178 | 0.7285 |
313.15 | 0.9462 | 0.4730 |
313.15 | 0.9469 | 0.4614 |
Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)
Mole fraction of Pentane, 2-methyl- (2) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
---|---|
0.2483 | 328.72 |
0.2749 | 331.42 |
0.3134 | 334.21 |
0.3518 | 335.90 |
0.3763 | 336.70 |
0.4107 | 337.32 |
0.4230 | 337.29 |
0.4590 | 337.62 |
0.5016 | 337.69 |
0.5523 | 337.66 |
0.6154 | 337.21 |
0.6620 | 336.25 |
0.7118 | 334.23 |
0.7924 | 328.28 |
0.8063 | 326.91 |
Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)
Mole fraction of Pentane, 2-methyl- (2) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
---|---|
0.2483 | 328.72 |
0.2749 | 331.42 |
0.3134 | 334.21 |
0.3518 | 335.90 |
0.3763 | 336.70 |
0.4107 | 337.32 |
0.4230 | 337.29 |
0.4590 | 337.62 |
0.5016 | 337.69 |
0.5523 | 337.66 |
0.6154 | 337.21 |
0.6620 | 336.25 |
0.7118 | 334.23 |
0.7924 | 328.28 |
0.8063 | 326.91 |