Mixture of 1-Pentanol + 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	353.20	0.0000
0.0000	363.20	0.0000
0.0000	373.20	0.0000
0.0090	373.20	0.0180
0.0280	363.20	0.0600
0.0520	373.20	0.0930
0.0630	353.20	0.1420
0.0660	363.20	0.1310
0.1080	353.20	0.2190
0.1140	373.20	0.1980
0.1190	353.20	0.2430
0.1400	363.20	0.2440
0.1470	373.20	0.2400
0.1570	353.20	0.3050
0.1900	373.20	0.3080
0.2120	353.20	0.3900
0.2160	373.20	0.3320
0.2260	363.20	0.3740
0.2270	363.20	0.3830
0.2530	373.20	0.3940
0.2940	353.20	0.4820
0.3120	363.20	0.4670
0.3220	373.20	0.4500
0.3290	363.20	0.4970
0.3680	353.20	0.5430
0.3810	373.20	0.5050
0.3900	363.20	0.5540
0.4090	373.20	0.5450
0.4410	353.20	0.6050
0.4650	363.20	0.6120
0.4730	373.20	0.5930
0.5060	353.20	0.6540
0.5220	363.20	0.6550
0.5550	353.20	0.6850
0.5620	373.20	0.6690
0.5810	363.20	0.6930
0.6120	353.20	0.7200
0.6180	373.20	0.6930
0.6320	363.20	0.7260
0.6620	353.20	0.7490
0.6830	363.20	0.7590
0.7210	353.20	0.7780
0.7310	373.20	0.7770
0.7330	363.20	0.7900
0.7630	363.20	0.8070
0.7980	373.20	0.8170
0.8240	353.20	0.8550
0.8500	373.20	0.8690
0.8780	373.20	0.8920
0.8970	353.20	0.9090
0.9020	353.20	0.9160
0.9020	363.20	0.9050
0.9380	373.20	0.9410
0.9770	373.20	0.9770
0.9910	373.20	0.9820
1.0000	353.20	1.0000
1.0000	363.20	1.0000
1.0000	373.20	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
0.0340	0.0800
0.0460	0.1070
0.0640	0.1440
0.1150	0.2360
0.1470	0.2860
0.1840	0.3380
0.1990	0.3570
0.2290	0.3940
0.2890	0.4580
0.2910	0.4590
0.3790	0.5380
0.4040	0.5570
0.4760	0.6090
0.5140	0.6330
0.5630	0.6640
0.6510	0.7160
0.6730	0.7290
0.7890	0.8000
0.8880	0.8740
0.9280	0.9110
0.9330	0.9160
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	353.20	0.0000
0.0000	363.20	0.0000
0.0000	373.20	0.0000
0.0090	373.20	0.0180
0.0280	363.20	0.0600
0.0520	373.20	0.0930
0.0630	353.20	0.1420
0.0660	363.20	0.1310
0.1080	353.20	0.2190
0.1140	373.20	0.1980
0.1190	353.20	0.2430
0.1400	363.20	0.2440
0.1470	373.20	0.2400
0.1570	353.20	0.3050
0.1900	373.20	0.3080
0.2120	353.20	0.3900
0.2160	373.20	0.3320
0.2260	363.20	0.3740
0.2270	363.20	0.3830
0.2530	373.20	0.3940
0.2940	353.20	0.4820
0.3120	363.20	0.4670
0.3220	373.20	0.4500
0.3290	363.20	0.4970
0.3680	353.20	0.5430
0.3810	373.20	0.5050
0.3900	363.20	0.5540
0.4090	373.20	0.5450
0.4410	353.20	0.6050
0.4650	363.20	0.6120
0.4730	373.20	0.5930
0.5060	353.20	0.6540
0.5220	363.20	0.6550
0.5550	353.20	0.6850
0.5620	373.20	0.6690
0.5810	363.20	0.6930
0.6120	353.20	0.7200
0.6180	373.20	0.6930
0.6320	363.20	0.7260
0.6620	353.20	0.7490
0.6830	363.20	0.7590
0.7210	353.20	0.7780
0.7310	373.20	0.7770
0.7330	363.20	0.7900
0.7630	363.20	0.8070
0.7980	373.20	0.8170
0.8240	353.20	0.8550
0.8500	373.20	0.8690
0.8780	373.20	0.8920
0.8970	353.20	0.9090
0.9020	353.20	0.9160
0.9020	363.20	0.9050
0.9380	373.20	0.9410
0.9770	373.20	0.9770
0.9910	373.20	0.9820
1.0000	353.20	1.0000
1.0000	363.20	1.0000
1.0000	373.20	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
0.0340	0.0800
0.0460	0.1070
0.0640	0.1440
0.1150	0.2360
0.1470	0.2860
0.1840	0.3380
0.1990	0.3570
0.2290	0.3940
0.2890	0.4580
0.2910	0.4590
0.3790	0.5380
0.4040	0.5570
0.4760	0.6090
0.5140	0.6330
0.5630	0.6640
0.6510	0.7160
0.6730	0.7290
0.7890	0.8000
0.8880	0.8740
0.9280	0.9110
0.9330	0.9160
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
0.0374	0.0355
0.0962	0.1561
0.1388	0.2694
0.1801	0.3879
0.2202	0.5041
0.2590	0.6144
0.2967	0.7160
0.3333	0.8074
0.3689	0.8880
0.4034	0.9575
0.4370	1.016
0.4696	1.0635
0.5014	1.1005
0.5323	1.1272
0.5604	1.1328
0.5624	1.144
0.5804	1.1395
0.5916	1.1512
0.6004	1.142
0.6202	1.1491
0.6204	1.1399
0.6404	1.1332
0.6480	1.1381
0.6604	1.1218
0.6616	1.1294
0.6804	1.1055
0.7004	1.0841
0.7204	1.0574
0.7404	1.0252
0.7604	0.9873
0.7804	0.9435
0.8004	0.8938
0.8204	0.8377
0.8404	0.7750
0.8603	0.7056
0.8803	0.6286
0.9002	0.5442
0.9202	0.4516
0.9401	0.3513
0.9601	0.2409
0.9800	0.1208

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
0.0374	0.0355
0.0962	0.1561
0.1388	0.2694
0.1801	0.3879
0.2202	0.5041
0.2590	0.6144
0.2967	0.7160
0.3333	0.8074
0.3689	0.8880
0.4034	0.9575
0.4370	1.016
0.4696	1.0635
0.5014	1.1005
0.5323	1.1272
0.5604	1.1328
0.5624	1.144
0.5804	1.1395
0.5916	1.1512
0.6004	1.142
0.6202	1.1491
0.6204	1.1399
0.6404	1.1332
0.6480	1.1381
0.6604	1.1218
0.6616	1.1294
0.6804	1.1055
0.7004	1.0841
0.7204	1.0574
0.7404	1.0252
0.7604	0.9873
0.7804	0.9435
0.8004	0.8938
0.8204	0.8377
0.8404	0.7750
0.8603	0.7056
0.8803	0.6286
0.9002	0.5442
0.9202	0.4516
0.9401	0.3513
0.9601	0.2409
0.9800	0.1208

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	353.20	9.83
0.0000	363.20	15.58
0.0000	373.20	24.26
0.0090	373.20	24.51
0.0280	363.20	16.16
0.0520	373.20	26.43
0.0630	353.20	10.72
0.0660	363.20	16.92
0.1080	353.20	11.59
0.1140	373.20	28.02
0.1190	353.20	11.82
0.1400	363.20	18.36
0.1470	373.20	29.03
0.1570	353.20	12.33
0.1900	373.20	30.22
0.2120	353.20	13.12
0.2160	373.20	30.89
0.2260	363.20	19.86
0.2270	363.20	19.94
0.2530	373.20	31.82
0.2940	353.20	14.06
0.3120	363.20	21.10
0.3220	373.20	33.21
0.3290	363.20	21.65
0.3680	353.20	14.79
0.3810	373.20	34.18
0.3900	363.20	22.57
0.4090	373.20	34.69
0.4410	353.20	15.48
0.4650	363.20	23.53
0.4730	373.20	35.49
0.5060	353.20	16.04
0.5220	363.20	24.25
0.5550	353.20	16.29
0.5620	373.20	36.59
0.5810	363.20	24.89
0.6120	353.20	16.64
0.6180	373.20	36.98
0.6320	363.20	25.39
0.6620	353.20	16.79
0.6830	363.20	25.67
0.7210	353.20	17.01
0.7310	373.20	37.77
0.7330	363.20	25.99
0.7630	363.20	26.13
0.7980	373.20	38.21
0.8240	353.20	17.53
0.8500	373.20	38.62
0.8780	373.20	38.64
0.8970	353.20	17.64
0.9020	353.20	17.73
0.9020	363.20	26.47
0.9380	373.20	38.63
0.9770	373.20	38.41
0.9910	373.20	38.31
1.0000	353.20	18.02
1.0000	363.20	26.88
1.0000	373.20	38.24

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	353.20	9.83
0.0000	363.20	15.58
0.0000	373.20	24.26
0.0090	373.20	24.51
0.0280	363.20	16.16
0.0520	373.20	26.43
0.0630	353.20	10.72
0.0660	363.20	16.92
0.1080	353.20	11.59
0.1140	373.20	28.02
0.1190	353.20	11.82
0.1400	363.20	18.36
0.1470	373.20	29.03
0.1570	353.20	12.33
0.1900	373.20	30.22
0.2120	353.20	13.12
0.2160	373.20	30.89
0.2260	363.20	19.86
0.2270	363.20	19.94
0.2530	373.20	31.82
0.2940	353.20	14.06
0.3120	363.20	21.10
0.3220	373.20	33.21
0.3290	363.20	21.65
0.3680	353.20	14.79
0.3810	373.20	34.18
0.3900	363.20	22.57
0.4090	373.20	34.69
0.4410	353.20	15.48
0.4650	363.20	23.53
0.4730	373.20	35.49
0.5060	353.20	16.04
0.5220	363.20	24.25
0.5550	353.20	16.29
0.5620	373.20	36.59
0.5810	363.20	24.89
0.6120	353.20	16.64
0.6180	373.20	36.98
0.6320	363.20	25.39
0.6620	353.20	16.79
0.6830	363.20	25.67
0.7210	353.20	17.01
0.7310	373.20	37.77
0.7330	363.20	25.99
0.7630	363.20	26.13
0.7980	373.20	38.21
0.8240	353.20	17.53
0.8500	373.20	38.62
0.8780	373.20	38.64
0.8970	353.20	17.64
0.9020	353.20	17.73
0.9020	363.20	26.47
0.9380	373.20	38.63
0.9770	373.20	38.41
0.9910	373.20	38.31
1.0000	353.20	18.02
1.0000	363.20	26.88
1.0000	373.20	38.24

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	385.20
0.0340	383.60
0.0460	383.20
0.0640	382.80
0.1150	381.20
0.1470	380.50
0.1840	379.50
0.1990	379.20
0.2290	378.70
0.2890	377.70
0.2910	377.60
0.3790	376.40
0.4040	376.20
0.4760	375.30
0.5140	375.10
0.5630	374.60
0.6510	373.90
0.6730	373.80
0.7890	373.30
0.8880	373.60
0.9280	373.60
0.9330	373.80
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	385.20
0.0340	383.60
0.0460	383.20
0.0640	382.80
0.1150	381.20
0.1470	380.50
0.1840	379.50
0.1990	379.20
0.2290	378.70
0.2890	377.70
0.2910	377.60
0.3790	376.40
0.4040	376.20
0.4760	375.30
0.5140	375.10
0.5630	374.60
0.6510	373.90
0.6730	373.80
0.7890	373.30
0.8880	373.60
0.9280	373.60
0.9330	373.80
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