Datasets
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Mole fraction (14)
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Excess molar enthalpy (molar enthalpy (4)
-
Liquid-liquid equilibrium temperature, K (2)
Mole fraction of Cyclohexane, methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Cyclohexane, methyl- (1) - Liquid mixture 1 |
298.15 |
0.8130 |
303.15 |
0.7860 |
Mole fraction of Cyclohexane, methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Cyclohexane, methyl- (1) - Liquid mixture 2 |
298.15 |
0.1520 |
303.15 |
0.1750 |
Mole fraction of Cyclohexane, methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 2)
Temperature, K - Liquid mixture 1 |
Mole fraction of Cyclohexane, methyl- (1) - Liquid mixture 1 |
293.15 |
0.1350 |
298.15 |
0.1500 |
303.15 |
0.1740 |
308.15 |
0.2020 |
313.15 |
0.2510 |
Mole fraction of Cyclohexane, methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 1)
Temperature, K - Liquid mixture 2 |
Mole fraction of Cyclohexane, methyl- (1) - Liquid mixture 2 |
293.15 |
0.8310 |
298.15 |
0.8120 |
303.15 |
0.7920 |
308.15 |
0.7500 |
313.15 |
0.6800 |
Mole fraction of Cyclohexane, methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 2)
Temperature, K - Liquid mixture 1 |
Mole fraction of Cyclohexane, methyl- (1) - Liquid mixture 1 |
288.15 |
0.1260 |
293.15 |
0.1390 |
295.15 |
0.1450 |
298.15 |
0.1540 |
301.15 |
0.1670 |
303.15 |
0.1770 |
305.15 |
0.1840 |
307.15 |
0.1960 |
Mole fraction of Cyclohexane, methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 1)
Temperature, K - Liquid mixture 2 |
Mole fraction of Cyclohexane, methyl- (1) - Liquid mixture 2 |
288.15 |
0.8610 |
293.15 |
0.8370 |
295.15 |
0.8280 |
298.15 |
0.8140 |
301.15 |
0.7930 |
303.15 |
0.7800 |
305.15 |
0.7670 |
307.15 |
0.7580 |
Mole fraction of Methyl Alcohol (2)
[ref]
Operational condition: Temperature, K =
313.15 (Liquid)
Mole fraction of Methyl Alcohol (2) - Liquid |
Mole fraction of Methyl Alcohol (2) - Gas |
0.0166 |
0.5596 |
0.0471 |
0.6660 |
0.0757 |
0.6866 |
0.0976 |
0.6913 |
0.1503 |
0.7158 |
0.2010 |
0.7363 |
0.2474 |
0.7296 |
0.2988 |
0.7324 |
0.3493 |
0.7326 |
0.4013 |
0.7306 |
0.4501 |
0.7420 |
0.4992 |
0.7326 |
0.5503 |
0.7299 |
0.6021 |
0.7355 |
0.6496 |
0.7391 |
0.6997 |
0.7459 |
0.7499 |
0.7382 |
0.8001 |
0.7470 |
0.8498 |
0.7610 |
0.8996 |
0.7820 |
0.9251 |
0.8062 |
0.9497 |
0.8389 |
0.9799 |
0.9102 |
Mole fraction of Cyclohexane, methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Cyclohexane, methyl- (1) - Liquid mixture 1 |
298.15 |
0.8130 |
303.15 |
0.7860 |
Mole fraction of Cyclohexane, methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Cyclohexane, methyl- (1) - Liquid mixture 2 |
298.15 |
0.1520 |
303.15 |
0.1750 |
Mole fraction of Cyclohexane, methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 2)
Temperature, K - Liquid mixture 1 |
Mole fraction of Cyclohexane, methyl- (1) - Liquid mixture 1 |
293.15 |
0.1350 |
298.15 |
0.1500 |
303.15 |
0.1740 |
308.15 |
0.2020 |
313.15 |
0.2510 |
Mole fraction of Cyclohexane, methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 1)
Temperature, K - Liquid mixture 2 |
Mole fraction of Cyclohexane, methyl- (1) - Liquid mixture 2 |
293.15 |
0.8310 |
298.15 |
0.8120 |
303.15 |
0.7920 |
308.15 |
0.7500 |
313.15 |
0.6800 |
Mole fraction of Cyclohexane, methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 2)
Temperature, K - Liquid mixture 1 |
Mole fraction of Cyclohexane, methyl- (1) - Liquid mixture 1 |
288.15 |
0.1260 |
293.15 |
0.1390 |
295.15 |
0.1450 |
298.15 |
0.1540 |
301.15 |
0.1670 |
303.15 |
0.1770 |
305.15 |
0.1840 |
307.15 |
0.1960 |
Mole fraction of Cyclohexane, methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 1)
Temperature, K - Liquid mixture 2 |
Mole fraction of Cyclohexane, methyl- (1) - Liquid mixture 2 |
288.15 |
0.8610 |
293.15 |
0.8370 |
295.15 |
0.8280 |
298.15 |
0.8140 |
301.15 |
0.7930 |
303.15 |
0.7800 |
305.15 |
0.7670 |
307.15 |
0.7580 |
Mole fraction of Methyl Alcohol (2)
[ref]
Operational condition: Temperature, K =
313.15 (Liquid)
Mole fraction of Methyl Alcohol (2) - Liquid |
Mole fraction of Methyl Alcohol (2) - Gas |
0.0166 |
0.5596 |
0.0471 |
0.6660 |
0.0757 |
0.6866 |
0.0976 |
0.6913 |
0.1503 |
0.7158 |
0.2010 |
0.7363 |
0.2474 |
0.7296 |
0.2988 |
0.7324 |
0.3493 |
0.7326 |
0.4013 |
0.7306 |
0.4501 |
0.7420 |
0.4992 |
0.7326 |
0.5503 |
0.7299 |
0.6021 |
0.7355 |
0.6496 |
0.7391 |
0.6997 |
0.7459 |
0.7499 |
0.7382 |
0.8001 |
0.7470 |
0.8498 |
0.7610 |
0.8996 |
0.7820 |
0.9251 |
0.8062 |
0.9497 |
0.8389 |
0.9799 |
0.9102 |
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- (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.15 |
0.0166 |
0.0773 |
298.15 |
0.0345 |
0.1495 |
298.15 |
0.0537 |
0.2175 |
298.15 |
0.0743 |
0.2763 |
298.15 |
0.0967 |
0.3320 |
298.15 |
0.1210 |
0.3812 |
298.15 |
0.8590 |
0.4217 |
298.15 |
0.9056 |
0.3711 |
313.15 |
0.0166 |
0.0837 |
313.15 |
0.0343 |
0.1594 |
313.15 |
0.0534 |
0.2337 |
313.15 |
0.0741 |
0.3006 |
313.15 |
0.0964 |
0.3633 |
313.15 |
0.1206 |
0.4216 |
313.15 |
0.1470 |
0.4750 |
313.15 |
0.1758 |
0.5212 |
313.15 |
0.2075 |
0.5592 |
313.15 |
0.2411 |
0.5833 |
313.15 |
0.2424 |
0.5886 |
313.15 |
0.7423 |
0.6699 |
313.15 |
0.8057 |
0.6372 |
313.15 |
0.8588 |
0.5769 |
313.15 |
0.9055 |
0.5134 |
313.15 |
0.9410 |
0.4524 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Mole fraction of Cyclohexane, methyl- (1) - Liquid mixture 1 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid mixture 1 |
298.15 |
0.1475 |
0.4169 |
298.15 |
0.1764 |
0.4308 |
298.15 |
0.2082 |
0.4346 |
298.15 |
0.2411 |
0.4375 |
298.15 |
0.2432 |
0.4380 |
298.15 |
0.2819 |
0.4411 |
298.15 |
0.3251 |
0.4428 |
298.15 |
0.3736 |
0.4452 |
298.15 |
0.4283 |
0.4497 |
298.15 |
0.4907 |
0.4520 |
298.15 |
0.5623 |
0.4530 |
298.15 |
0.6453 |
0.4567 |
298.15 |
0.7429 |
0.4632 |
298.15 |
0.8061 |
0.4559 |
313.15 |
0.2812 |
0.6057 |
313.15 |
0.3244 |
0.6164 |
313.15 |
0.3728 |
0.6291 |
313.15 |
0.4275 |
0.6435 |
313.15 |
0.4898 |
0.6564 |
313.15 |
0.5615 |
0.6677 |
313.15 |
0.6446 |
0.6862 |
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- (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.15 |
0.0166 |
0.0773 |
298.15 |
0.0345 |
0.1495 |
298.15 |
0.0537 |
0.2175 |
298.15 |
0.0743 |
0.2763 |
298.15 |
0.0967 |
0.3320 |
298.15 |
0.1210 |
0.3812 |
298.15 |
0.8590 |
0.4217 |
298.15 |
0.9056 |
0.3711 |
313.15 |
0.0166 |
0.0837 |
313.15 |
0.0343 |
0.1594 |
313.15 |
0.0534 |
0.2337 |
313.15 |
0.0741 |
0.3006 |
313.15 |
0.0964 |
0.3633 |
313.15 |
0.1206 |
0.4216 |
313.15 |
0.1470 |
0.4750 |
313.15 |
0.1758 |
0.5212 |
313.15 |
0.2075 |
0.5592 |
313.15 |
0.2411 |
0.5833 |
313.15 |
0.2424 |
0.5886 |
313.15 |
0.7423 |
0.6699 |
313.15 |
0.8057 |
0.6372 |
313.15 |
0.8588 |
0.5769 |
313.15 |
0.9055 |
0.5134 |
313.15 |
0.9410 |
0.4524 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Mole fraction of Cyclohexane, methyl- (1) - Liquid mixture 1 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid mixture 1 |
298.15 |
0.1475 |
0.4169 |
298.15 |
0.1764 |
0.4308 |
298.15 |
0.2082 |
0.4346 |
298.15 |
0.2411 |
0.4375 |
298.15 |
0.2432 |
0.4380 |
298.15 |
0.2819 |
0.4411 |
298.15 |
0.3251 |
0.4428 |
298.15 |
0.3736 |
0.4452 |
298.15 |
0.4283 |
0.4497 |
298.15 |
0.4907 |
0.4520 |
298.15 |
0.5623 |
0.4530 |
298.15 |
0.6453 |
0.4567 |
298.15 |
0.7429 |
0.4632 |
298.15 |
0.8061 |
0.4559 |
313.15 |
0.2812 |
0.6057 |
313.15 |
0.3244 |
0.6164 |
313.15 |
0.3728 |
0.6291 |
313.15 |
0.4275 |
0.6435 |
313.15 |
0.4898 |
0.6564 |
313.15 |
0.5615 |
0.6677 |
313.15 |
0.6446 |
0.6862 |
Liquid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
Mole fraction of Cyclohexane, methyl- (1) - Liquid mixture 1 |
Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
0.1920 |
306.26 |
0.2119 |
309.43 |
0.2231 |
310.81 |
0.2399 |
312.59 |
0.2452 |
313.04 |
0.2604 |
314.13 |
0.2721 |
314.93 |
0.2955 |
316.06 |
0.3042 |
316.30 |
0.3263 |
316.92 |
0.3265 |
316.82 |
0.3389 |
317.07 |
0.3701 |
317.37 |
0.4463 |
317.62 |
0.4637 |
317.60 |
0.5044 |
317.34 |
0.5348 |
317.11 |
0.5424 |
317.00 |
0.5530 |
316.96 |
0.5764 |
316.51 |
0.6059 |
315.82 |
0.6365 |
314.79 |
0.6618 |
313.69 |
0.6836 |
312.53 |
0.7123 |
310.69 |
0.7442 |
308.02 |
0.7881 |
303.02 |
Liquid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
Mole fraction of Cyclohexane, methyl- (1) - Liquid mixture 1 |
Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
0.1920 |
306.26 |
0.2119 |
309.43 |
0.2231 |
310.81 |
0.2399 |
312.59 |
0.2452 |
313.04 |
0.2604 |
314.13 |
0.2721 |
314.93 |
0.2955 |
316.06 |
0.3042 |
316.30 |
0.3263 |
316.92 |
0.3265 |
316.82 |
0.3389 |
317.07 |
0.3701 |
317.37 |
0.4463 |
317.62 |
0.4637 |
317.60 |
0.5044 |
317.34 |
0.5348 |
317.11 |
0.5424 |
317.00 |
0.5530 |
316.96 |
0.5764 |
316.51 |
0.6059 |
315.82 |
0.6365 |
314.79 |
0.6618 |
313.69 |
0.6836 |
312.53 |
0.7123 |
310.69 |
0.7442 |
308.02 |
0.7881 |
303.02 |
Sources