Datasets
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Mole fraction (16)
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Excess molar enthalpy (molar enthalpy (4)
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Liquid-liquid equilibrium temperature, K (2)
Mole fraction of Cyclohexane, methyl- (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Cyclohexane, methyl- (2) - Liquid mixture 1 |
| 303.15 |
101.33 |
0.1761 |
Mole fraction of Cyclohexane, methyl- (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mole fraction of Cyclohexane, methyl- (2) - Liquid mixture 2 |
| 303.15 |
101.33 |
0.8823 |
Mole fraction of Cyclohexane, methyl- (2)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Cyclohexane, methyl- (2) - Liquid mixture 1 |
| 298.15 |
0.9010 |
| 303.15 |
0.8820 |
Mole fraction of Cyclohexane, methyl- (2)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Cyclohexane, methyl- (2) - Liquid mixture 2 |
| 298.15 |
0.1550 |
| 303.15 |
0.1770 |
Mole fraction of Cyclohexane, methyl- (2)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Cyclohexane, methyl- (2) - Liquid mixture 1 |
| 293.15 |
0.1380 |
| 298.15 |
0.1560 |
| 303.15 |
0.1800 |
| 308.15 |
0.2050 |
| 313.15 |
0.2420 |
Mole fraction of Cyclohexane, methyl- (2)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 1)
| Temperature, K - Liquid mixture 2 |
Mole fraction of Cyclohexane, methyl- (2) - Liquid mixture 2 |
| 293.15 |
0.9200 |
| 298.15 |
0.9030 |
| 303.15 |
0.8810 |
| 308.15 |
0.8540 |
| 313.15 |
0.8160 |
Mole fraction of Cyclohexane, methyl- (2)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Cyclohexane, methyl- (2) - Liquid mixture 1 |
| 288.15 |
0.1240 |
| 293.15 |
0.1360 |
| 295.15 |
0.1450 |
| 298.15 |
0.1540 |
| 301.15 |
0.1660 |
| 303.15 |
0.1740 |
| 305.15 |
0.1840 |
| 307.15 |
0.1940 |
Mole fraction of Cyclohexane, methyl- (2)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 1)
| Temperature, K - Liquid mixture 2 |
Mole fraction of Cyclohexane, methyl- (2) - Liquid mixture 2 |
| 288.15 |
0.9320 |
| 293.15 |
0.9180 |
| 295.15 |
0.9110 |
| 298.15 |
0.9000 |
| 301.15 |
0.8890 |
| 303.15 |
0.8830 |
| 305.15 |
0.8750 |
| 307.15 |
0.8590 |
Mole fraction of Cyclohexane, methyl- (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Cyclohexane, methyl- (2) - Liquid mixture 1 |
| 303.15 |
101.33 |
0.1761 |
Mole fraction of Cyclohexane, methyl- (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mole fraction of Cyclohexane, methyl- (2) - Liquid mixture 2 |
| 303.15 |
101.33 |
0.8823 |
Mole fraction of Cyclohexane, methyl- (2)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Cyclohexane, methyl- (2) - Liquid mixture 1 |
| 298.15 |
0.9010 |
| 303.15 |
0.8820 |
Mole fraction of Cyclohexane, methyl- (2)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Cyclohexane, methyl- (2) - Liquid mixture 2 |
| 298.15 |
0.1550 |
| 303.15 |
0.1770 |
Mole fraction of Cyclohexane, methyl- (2)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Cyclohexane, methyl- (2) - Liquid mixture 1 |
| 293.15 |
0.1380 |
| 298.15 |
0.1560 |
| 303.15 |
0.1800 |
| 308.15 |
0.2050 |
| 313.15 |
0.2420 |
Mole fraction of Cyclohexane, methyl- (2)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 1)
| Temperature, K - Liquid mixture 2 |
Mole fraction of Cyclohexane, methyl- (2) - Liquid mixture 2 |
| 293.15 |
0.9200 |
| 298.15 |
0.9030 |
| 303.15 |
0.8810 |
| 308.15 |
0.8540 |
| 313.15 |
0.8160 |
Mole fraction of Cyclohexane, methyl- (2)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Cyclohexane, methyl- (2) - Liquid mixture 1 |
| 288.15 |
0.1240 |
| 293.15 |
0.1360 |
| 295.15 |
0.1450 |
| 298.15 |
0.1540 |
| 301.15 |
0.1660 |
| 303.15 |
0.1740 |
| 305.15 |
0.1840 |
| 307.15 |
0.1940 |
Mole fraction of Cyclohexane, methyl- (2)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 1)
| Temperature, K - Liquid mixture 2 |
Mole fraction of Cyclohexane, methyl- (2) - Liquid mixture 2 |
| 288.15 |
0.9320 |
| 293.15 |
0.9180 |
| 295.15 |
0.9110 |
| 298.15 |
0.9000 |
| 301.15 |
0.8890 |
| 303.15 |
0.8830 |
| 305.15 |
0.8750 |
| 307.15 |
0.8590 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Cyclohexane, methyl- (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 298.15 |
0.0310 |
0.2481 |
| 298.15 |
0.0633 |
0.4337 |
| 298.15 |
0.0969 |
0.6793 |
| 298.15 |
0.1320 |
0.8753 |
| 298.15 |
0.9240 |
0.7128 |
| 298.15 |
0.9274 |
0.6830 |
| 298.15 |
0.9305 |
0.6659 |
| 298.15 |
0.9383 |
0.6136 |
| 313.15 |
0.0310 |
0.2425 |
| 313.15 |
0.0634 |
0.4763 |
| 313.15 |
0.0970 |
0.6966 |
| 313.15 |
0.1321 |
0.9012 |
| 313.15 |
0.1687 |
1.0866 |
| 313.15 |
0.2069 |
1.2461 |
| 313.15 |
0.9204 |
0.7626 |
| 313.15 |
0.9383 |
0.6442 |
| 313.15 |
0.9552 |
0.4955 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Mole fraction of Cyclohexane, methyl- (2) - Liquid mixture 1 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid mixture 1 |
| 298.15 |
0.1685 |
0.9555 |
| 298.15 |
0.2068 |
0.9772 |
| 298.15 |
0.2467 |
0.9763 |
| 298.15 |
0.2893 |
0.9747 |
| 298.15 |
0.3322 |
0.9650 |
| 298.15 |
0.3781 |
0.9518 |
| 298.15 |
0.3782 |
0.9447 |
| 298.15 |
0.4264 |
0.9366 |
| 298.15 |
0.4771 |
0.9231 |
| 298.15 |
0.5304 |
0.9115 |
| 298.15 |
0.5867 |
0.8991 |
| 298.15 |
0.6460 |
0.8854 |
| 298.15 |
0.7087 |
0.8712 |
| 298.15 |
0.7751 |
0.8524 |
| 298.15 |
0.8455 |
0.8332 |
| 298.15 |
0.9204 |
0.7501 |
| 313.15 |
0.2469 |
1.3188 |
| 313.15 |
0.2887 |
1.3352 |
| 313.15 |
0.3325 |
1.328 |
| 313.15 |
0.3784 |
1.3219 |
| 313.15 |
0.4267 |
1.3132 |
| 313.15 |
0.4773 |
1.3067 |
| 313.15 |
0.5307 |
1.2867 |
| 313.15 |
0.5869 |
1.2805 |
| 313.15 |
0.6462 |
1.2723 |
| 313.15 |
0.7089 |
1.2584 |
| 313.15 |
0.7753 |
1.2408 |
| 313.15 |
0.8457 |
1.1558 |
| 313.15 |
0.2887 |
1.3248 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Cyclohexane, methyl- (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 298.15 |
0.0310 |
0.2481 |
| 298.15 |
0.0633 |
0.4337 |
| 298.15 |
0.0969 |
0.6793 |
| 298.15 |
0.1320 |
0.8753 |
| 298.15 |
0.9240 |
0.7128 |
| 298.15 |
0.9274 |
0.6830 |
| 298.15 |
0.9305 |
0.6659 |
| 298.15 |
0.9383 |
0.6136 |
| 313.15 |
0.0310 |
0.2425 |
| 313.15 |
0.0634 |
0.4763 |
| 313.15 |
0.0970 |
0.6966 |
| 313.15 |
0.1321 |
0.9012 |
| 313.15 |
0.1687 |
1.0866 |
| 313.15 |
0.2069 |
1.2461 |
| 313.15 |
0.9204 |
0.7626 |
| 313.15 |
0.9383 |
0.6442 |
| 313.15 |
0.9552 |
0.4955 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Mole fraction of Cyclohexane, methyl- (2) - Liquid mixture 1 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid mixture 1 |
| 298.15 |
0.1685 |
0.9555 |
| 298.15 |
0.2068 |
0.9772 |
| 298.15 |
0.2467 |
0.9763 |
| 298.15 |
0.2893 |
0.9747 |
| 298.15 |
0.3322 |
0.9650 |
| 298.15 |
0.3781 |
0.9518 |
| 298.15 |
0.3782 |
0.9447 |
| 298.15 |
0.4264 |
0.9366 |
| 298.15 |
0.4771 |
0.9231 |
| 298.15 |
0.5304 |
0.9115 |
| 298.15 |
0.5867 |
0.8991 |
| 298.15 |
0.6460 |
0.8854 |
| 298.15 |
0.7087 |
0.8712 |
| 298.15 |
0.7751 |
0.8524 |
| 298.15 |
0.8455 |
0.8332 |
| 298.15 |
0.9204 |
0.7501 |
| 313.15 |
0.2469 |
1.3188 |
| 313.15 |
0.2887 |
1.3352 |
| 313.15 |
0.3325 |
1.328 |
| 313.15 |
0.3784 |
1.3219 |
| 313.15 |
0.4267 |
1.3132 |
| 313.15 |
0.4773 |
1.3067 |
| 313.15 |
0.5307 |
1.2867 |
| 313.15 |
0.5869 |
1.2805 |
| 313.15 |
0.6462 |
1.2723 |
| 313.15 |
0.7089 |
1.2584 |
| 313.15 |
0.7753 |
1.2408 |
| 313.15 |
0.8457 |
1.1558 |
| 313.15 |
0.2887 |
1.3248 |
Liquid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
| Mole fraction of Cyclohexane, methyl- (2) - Liquid mixture 1 |
Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
| 0.2135 |
309.50 |
| 0.2413 |
313.21 |
| 0.2590 |
315.06 |
| 0.2809 |
317.05 |
| 0.2926 |
317.91 |
| 0.3275 |
319.98 |
| 0.3584 |
321.28 |
| 0.3668 |
321.43 |
| 0.3939 |
322.18 |
| 0.4040 |
322.31 |
| 0.4196 |
322.50 |
| 0.4358 |
322.66 |
| 0.4497 |
322.73 |
| 0.4843 |
322.84 |
| 0.5125 |
322.85 |
| 0.5151 |
322.85 |
| 0.5348 |
322.81 |
| 0.5446 |
322.85 |
| 0.5999 |
322.64 |
| 0.6253 |
322.45 |
| 0.6602 |
321.91 |
| 0.7152 |
320.39 |
| 0.7404 |
319.29 |
| 0.7854 |
316.59 |
| 0.8156 |
313.95 |
| 0.8360 |
311.64 |
Liquid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
| Mole fraction of Cyclohexane, methyl- (2) - Liquid mixture 1 |
Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
| 0.2135 |
309.50 |
| 0.2413 |
313.21 |
| 0.2590 |
315.06 |
| 0.2809 |
317.05 |
| 0.2926 |
317.91 |
| 0.3275 |
319.98 |
| 0.3584 |
321.28 |
| 0.3668 |
321.43 |
| 0.3939 |
322.18 |
| 0.4040 |
322.31 |
| 0.4196 |
322.50 |
| 0.4358 |
322.66 |
| 0.4497 |
322.73 |
| 0.4843 |
322.84 |
| 0.5125 |
322.85 |
| 0.5151 |
322.85 |
| 0.5348 |
322.81 |
| 0.5446 |
322.85 |
| 0.5999 |
322.64 |
| 0.6253 |
322.45 |
| 0.6602 |
321.91 |
| 0.7152 |
320.39 |
| 0.7404 |
319.29 |
| 0.7854 |
316.59 |
| 0.8156 |
313.95 |
| 0.8360 |
311.64 |
Sources