Mixture of 1-Propanol + Pyrrole

Datasets

1. Mole fraction (4)
2. Excess molar enthalpy (molar enthalpy (2)
3. P_vap - Vapor or sublimation pressure, kPa (2)
4. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of Pyrrole (2) [ref]

Fixed		Measured
Mole fraction of Pyrrole (2) - Liquid	Temperature, K - Liquid	Mole fraction of Pyrrole (2) - Gas
0.0000	348.20	0.0000
0.0000	358.20	0.0000
0.0000	368.20	0.0000
0.0560	358.20	0.0290
0.1000	368.20	0.0500
0.1340	358.20	0.0700
0.1550	348.20	0.0820
0.1560	358.20	0.0820
0.1810	358.20	0.0960
0.2000	368.20	0.0990
0.2300	358.20	0.1270
0.2400	348.20	0.1290
0.2650	368.20	0.1410
0.3290	348.20	0.1760
0.3290	358.20	0.1740
0.3380	368.20	0.1800
0.3450	348.20	0.1860
0.3510	358.20	0.1830
0.4010	358.20	0.2150
0.4050	368.20	0.2210
0.4190	348.20	0.2260
0.4740	358.20	0.2540
0.5350	368.20	0.2970
0.5360	348.20	0.2950
0.5390	358.20	0.2960
0.6100	358.20	0.3400
0.6400	348.20	0.3660
0.6400	368.20	0.3600
0.7160	348.20	0.4340
0.7360	358.20	0.4510
0.7650	368.20	0.4720
0.7670	348.20	0.4870
0.7890	358.20	0.5050
0.7980	368.20	0.5170
0.8130	348.20	0.5350
0.8300	358.20	0.5600
0.8480	348.20	0.6000
0.8690	368.20	0.6150
0.8730	358.20	0.6350
0.8970	348.20	0.6810
0.9080	358.20	0.7040
0.9190	368.20	0.7230
0.9290	348.20	0.7520
0.9390	368.20	0.7780
0.9400	358.20	0.7850
0.9650	348.20	0.8580
0.9680	358.20	0.8710
0.9830	358.20	0.9290
0.9890	358.20	0.9560
0.9890	368.20	0.9340
1.0000	348.20	1.0000
1.0000	358.20	1.0000
1.0000	368.20	1.0000

Mole fraction of Pyrrole (2) [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of Pyrrole (2) - Liquid	Mole fraction of Pyrrole (2) - Gas
0.0000	0.0000
0.0450	0.0230
0.1080	0.0580
0.1710	0.0910
0.2300	0.1220
0.2650	0.1420
0.3540	0.1910
0.3850	0.2110
0.5650	0.3140
0.6520	0.3780
0.7360	0.4630
0.8010	0.5370
0.8020	0.5410
0.8460	0.6090
0.8820	0.6650
0.9040	0.7180
0.9640	0.8720
1.0000	1.0000

Mole fraction of Pyrrole (2) [ref]

Fixed		Measured
Mole fraction of Pyrrole (2) - Liquid	Temperature, K - Liquid	Mole fraction of Pyrrole (2) - Gas
0.0000	348.20	0.0000
0.0000	358.20	0.0000
0.0000	368.20	0.0000
0.0560	358.20	0.0290
0.1000	368.20	0.0500
0.1340	358.20	0.0700
0.1550	348.20	0.0820
0.1560	358.20	0.0820
0.1810	358.20	0.0960
0.2000	368.20	0.0990
0.2300	358.20	0.1270
0.2400	348.20	0.1290
0.2650	368.20	0.1410
0.3290	348.20	0.1760
0.3290	358.20	0.1740
0.3380	368.20	0.1800
0.3450	348.20	0.1860
0.3510	358.20	0.1830
0.4010	358.20	0.2150
0.4050	368.20	0.2210
0.4190	348.20	0.2260
0.4740	358.20	0.2540
0.5350	368.20	0.2970
0.5360	348.20	0.2950
0.5390	358.20	0.2960
0.6100	358.20	0.3400
0.6400	348.20	0.3660
0.6400	368.20	0.3600
0.7160	348.20	0.4340
0.7360	358.20	0.4510
0.7650	368.20	0.4720
0.7670	348.20	0.4870
0.7890	358.20	0.5050
0.7980	368.20	0.5170
0.8130	348.20	0.5350
0.8300	358.20	0.5600
0.8480	348.20	0.6000
0.8690	368.20	0.6150
0.8730	358.20	0.6350
0.8970	348.20	0.6810
0.9080	358.20	0.7040
0.9190	368.20	0.7230
0.9290	348.20	0.7520
0.9390	368.20	0.7780
0.9400	358.20	0.7850
0.9650	348.20	0.8580
0.9680	358.20	0.8710
0.9830	358.20	0.9290
0.9890	358.20	0.9560
0.9890	368.20	0.9340
1.0000	348.20	1.0000
1.0000	358.20	1.0000
1.0000	368.20	1.0000

Mole fraction of Pyrrole (2) [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of Pyrrole (2) - Liquid	Mole fraction of Pyrrole (2) - Gas
0.0000	0.0000
0.0450	0.0230
0.1080	0.0580
0.1710	0.0910
0.2300	0.1220
0.2650	0.1420
0.3540	0.1910
0.3850	0.2110
0.5650	0.3140
0.6520	0.3780
0.7360	0.4630
0.8010	0.5370
0.8020	0.5410
0.8460	0.6090
0.8820	0.6650
0.9040	0.7180
0.9640	0.8720
1.0000	1.0000

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mole fraction of Pyrrole (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0299	0.0296
0.0598	0.0602
0.0897	0.1067
0.1197	0.1641
0.1497	0.2288
0.1796	0.2971
0.2096	0.3668
0.2396	0.4360
0.2696	0.5034
0.3896	0.7310
0.4197	0.7735
0.4497	0.8084
0.4652	0.8328
0.4797	0.8363
0.4902	0.8583
0.5202	0.8826
0.5502	0.8996
0.5803	0.9090
0.7003	0.8633
0.7303	0.8293
0.7603	0.7853
0.7903	0.7307
0.8203	0.6649
0.8503	0.5872
0.8802	0.4974
0.9101	0.3941
0.9401	0.2755
0.2996	0.5675
0.3296	0.6272
0.3596	0.6820
0.6103	0.9104
0.6403	0.9035
0.6703	0.8879
0.9700	0.1416

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mole fraction of Pyrrole (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0299	0.0296
0.0598	0.0602
0.0897	0.1067
0.1197	0.1641
0.1497	0.2288
0.1796	0.2971
0.2096	0.3668
0.2396	0.4360
0.2696	0.5034
0.3896	0.7310
0.4197	0.7735
0.4497	0.8084
0.4652	0.8328
0.4797	0.8363
0.4902	0.8583
0.5202	0.8826
0.5502	0.8996
0.5803	0.9090
0.7003	0.8633
0.7303	0.8293
0.7603	0.7853
0.7903	0.7307
0.8203	0.6649
0.8503	0.5872
0.8802	0.4974
0.9101	0.3941
0.9401	0.2755
0.2996	0.5675
0.3296	0.6272
0.3596	0.6820
0.6103	0.9104
0.6403	0.9035
0.6703	0.8879
0.9700	0.1416

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Pyrrole (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	348.20	40.90
0.0000	358.20	62.69
0.0000	368.20	94.03
0.0560	358.20	61.17
0.1000	368.20	88.72
0.1340	358.20	58.69
0.1550	348.20	37.07
0.1560	358.20	57.74
0.1810	358.20	57.17
0.2000	368.20	85.03
0.2300	358.20	55.29
0.2400	348.20	35.61
0.2650	368.20	82.61
0.3290	348.20	34.05
0.3290	358.20	52.39
0.3380	368.20	78.71
0.3450	348.20	33.73
0.3510	358.20	51.68
0.4010	358.20	50.17
0.4050	368.20	74.42
0.4190	348.20	32.31
0.4740	358.20	47.74
0.5350	368.20	69.35
0.5360	348.20	30.35
0.5390	358.20	45.60
0.6100	358.20	42.98
0.6400	348.20	28.64
0.6400	368.20	64.12
0.7160	348.20	26.89
0.7360	358.20	37.68
0.7650	368.20	56.46
0.7670	348.20	25.21
0.7890	358.20	35.33
0.7980	368.20	53.16
0.8130	348.20	23.91
0.8300	358.20	33.19
0.8480	348.20	22.43
0.8690	368.20	47.72
0.8730	358.20	30.61
0.8970	348.20	20.34
0.9080	358.20	28.54
0.9190	368.20	42.08
0.9290	348.20	19.02
0.9390	368.20	39.56
0.9400	358.20	26.18
0.9650	348.20	16.86
0.9680	358.20	24.25
0.9830	358.20	22.98
0.9890	358.20	22.46
0.9890	368.20	32.94
1.0000	348.20	14.40
1.0000	358.20	21.80
1.0000	368.20	32.06

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Pyrrole (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	348.20	40.90
0.0000	358.20	62.69
0.0000	368.20	94.03
0.0560	358.20	61.17
0.1000	368.20	88.72
0.1340	358.20	58.69
0.1550	348.20	37.07
0.1560	358.20	57.74
0.1810	358.20	57.17
0.2000	368.20	85.03
0.2300	358.20	55.29
0.2400	348.20	35.61
0.2650	368.20	82.61
0.3290	348.20	34.05
0.3290	358.20	52.39
0.3380	368.20	78.71
0.3450	348.20	33.73
0.3510	358.20	51.68
0.4010	358.20	50.17
0.4050	368.20	74.42
0.4190	348.20	32.31
0.4740	358.20	47.74
0.5350	368.20	69.35
0.5360	348.20	30.35
0.5390	358.20	45.60
0.6100	358.20	42.98
0.6400	348.20	28.64
0.6400	368.20	64.12
0.7160	348.20	26.89
0.7360	358.20	37.68
0.7650	368.20	56.46
0.7670	348.20	25.21
0.7890	358.20	35.33
0.7980	368.20	53.16
0.8130	348.20	23.91
0.8300	358.20	33.19
0.8480	348.20	22.43
0.8690	368.20	47.72
0.8730	358.20	30.61
0.8970	348.20	20.34
0.9080	358.20	28.54
0.9190	368.20	42.08
0.9290	348.20	19.02
0.9390	368.20	39.56
0.9400	358.20	26.18
0.9650	348.20	16.86
0.9680	358.20	24.25
0.9830	358.20	22.98
0.9890	358.20	22.46
0.9890	368.20	32.94
1.0000	348.20	14.40
1.0000	358.20	21.80
1.0000	368.20	32.06

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of Pyrrole (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	347.60
0.0450	347.90
0.1080	348.50
0.1710	349.40
0.2300	350.10
0.2650	350.40
0.3540	351.70
0.3850	352.10
0.5650	355.10
0.6520	356.80
0.7360	359.60
0.8010	361.90
0.8020	361.90
0.8460	363.60
0.8820	365.30
0.9040	366.90
0.9640	370.80
1.0000	374.70

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of Pyrrole (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	347.60
0.0450	347.90
0.1080	348.50
0.1710	349.40
0.2300	350.10
0.2650	350.40
0.3540	351.70
0.3850	352.10
0.5650	355.10
0.6520	356.80
0.7360	359.60
0.8010	361.90
0.8020	361.90
0.8460	363.60
0.8820	365.30
0.9040	366.90
0.9640	370.80
1.0000	374.70

Sources

• Phase equilibria and excess molar enthalpies study of the binary systems (pyrrole + hydrocarbon, or an alcohol) and modeling
• Vapor Liquid Equilibrium Data for Binary Systems of 1H-Pyrrole with Butan-1-ol, Propan-1-ol, or Pentan-1-ol