Mixture of Benzene + 1-Propanol

Datasets

1. Mole fraction (2)
2. Excess molar enthalpy (molar enthalpy (2)
3. P_vap - Vapor or sublimation pressure, kPa (6)
4. n₀ - Refractive index (Na D-line) (2)
5. ρ_l - Mass density, kg/m3 (4)
6. c_sound,fluid - Speed of Sound, m/s (2)

Mole fraction of 1-Propanol (2) [ref]

Operational condition: Temperature, K = 323.15 (Liquid)

Mole fraction of 1-Propanol (2) - Gas	Mole fraction of 1-Propanol (2) - Liquid
0.0151	0.0062
0.0248	0.0107
0.0688	0.0391
0.0883	0.0586
0.1271	0.1205
0.1470	0.1702
0.1666	0.2296
0.1865	0.2900
0.1972	0.3495
0.2126	0.4097
0.2271	0.4709
0.2462	0.5307
0.2599	0.5899
0.2866	0.6509
0.3206	0.7112
0.3480	0.7711
0.4192	0.8306
0.4854	0.8801
0.5734	0.9201
0.6355	0.9398

Mole fraction of 1-Propanol (2) [ref]

Operational condition: Temperature, K = 323.15 (Liquid)

Mole fraction of 1-Propanol (2) - Gas	Mole fraction of 1-Propanol (2) - Liquid
0.0151	0.0062
0.0248	0.0107
0.0688	0.0391
0.0883	0.0586
0.1271	0.1205
0.1470	0.1702
0.1666	0.2296
0.1865	0.2900
0.1972	0.3495
0.2126	0.4097
0.2271	0.4709
0.2462	0.5307
0.2599	0.5899
0.2866	0.6509
0.3206	0.7112
0.3480	0.7711
0.4192	0.8306
0.4854	0.8801
0.5734	0.9201
0.6355	0.9398

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

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Benzene (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15	0.0492	0.1060
298.15	0.0993	0.2190
298.15	0.1503	0.3340
298.15	0.2006	0.4440
298.15	0.2499	0.5510
298.15	0.3001	0.6520
298.15	0.3493	0.7450
298.15	0.3994	0.8300
298.15	0.4505	0.9060
298.15	0.5004	0.9680
298.15	0.5491	1.018
298.15	0.5987	1.051
298.15	0.6492	1.07
298.15	0.7006	1.067
298.15	0.7507	1.041
298.15	0.7994	0.9900
298.15	0.8489	0.9060
298.15	0.8992	0.7680
298.15	0.9504	0.5350
313.15	0.0493	0.1360
313.15	0.0995	0.2770
313.15	0.1506	0.4200
313.15	0.2009	0.5550
313.15	0.2503	0.6780
313.15	0.3005	0.7980
313.15	0.3498	0.9060
313.15	0.3999	1.006
313.15	0.4510	1.095
313.15	0.5009	1.165
313.15	0.5497	1.218
313.15	0.5993	1.253
313.15	0.6497	1.267
313.15	0.7010	1.257
313.15	0.7511	1.219
313.15	0.7997	1.154
313.15	0.8491	1.046
313.15	0.8994	0.8750
313.15	0.9505	0.5850

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

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Benzene (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15	0.0492	0.1060
298.15	0.0993	0.2190
298.15	0.1503	0.3340
298.15	0.2006	0.4440
298.15	0.2499	0.5510
298.15	0.3001	0.6520
298.15	0.3493	0.7450
298.15	0.3994	0.8300
298.15	0.4505	0.9060
298.15	0.5004	0.9680
298.15	0.5491	1.018
298.15	0.5987	1.051
298.15	0.6492	1.07
298.15	0.7006	1.067
298.15	0.7507	1.041
298.15	0.7994	0.9900
298.15	0.8489	0.9060
298.15	0.8992	0.7680
298.15	0.9504	0.5350
313.15	0.0493	0.1360
313.15	0.0995	0.2770
313.15	0.1506	0.4200
313.15	0.2009	0.5550
313.15	0.2503	0.6780
313.15	0.3005	0.7980
313.15	0.3498	0.9060
313.15	0.3999	1.006
313.15	0.4510	1.095
313.15	0.5009	1.165
313.15	0.5497	1.218
313.15	0.5993	1.253
313.15	0.6497	1.267
313.15	0.7010	1.257
313.15	0.7511	1.219
313.15	0.7997	1.154
313.15	0.8491	1.046
313.15	0.8994	0.8750
313.15	0.9505	0.5850

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Benzene (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	7.00
0.0503	10.78
0.0993	13.77
0.1492	16.24
0.1985	18.21
0.2493	19.84
0.2987	21.10
0.3490	22.12
0.3990	22.94
0.3999	22.95
0.4491	23.59
0.4501	23.61
0.4994	24.12
0.4997	24.12
0.5487	24.55
0.5510	24.53
0.5992	24.91
0.6001	24.89
0.6505	25.21
0.7003	25.46
0.7502	25.67
0.7998	25.81
0.8488	25.91
0.9025	25.90
0.9487	25.63
1.0000	24.39

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 1-Propanol (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.3000	25.46
0.7003	21.11

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 323.15 (Liquid)

Mole fraction of 1-Propanol (2) - Gas	Vapor or sublimation pressure, kPa - Liquid
0.0151	38.52
0.0248	38.73
0.0688	39.59
0.0883	39.89
0.1271	39.56
0.1470	38.95
0.1666	38.72
0.1865	38.31
0.1972	37.79
0.2126	37.20
0.2271	36.15
0.2462	35.29
0.2599	34.06
0.2866	32.92
0.3206	31.09
0.3480	28.71
0.4192	25.16
0.4854	22.31
0.5734	19.56
0.6355	17.98

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Benzene (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	7.00
0.0503	10.78
0.0993	13.77
0.1492	16.24
0.1985	18.21
0.2493	19.84
0.2987	21.10
0.3490	22.12
0.3990	22.94
0.3999	22.95
0.4491	23.59
0.4501	23.61
0.4994	24.12
0.4997	24.12
0.5487	24.55
0.5510	24.53
0.5992	24.91
0.6001	24.89
0.6505	25.21
0.7003	25.46
0.7502	25.67
0.7998	25.81
0.8488	25.91
0.9025	25.90
0.9487	25.63
1.0000	24.39

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 1-Propanol (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.3000	25.46
0.7003	21.11

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 323.15 (Liquid)

Mole fraction of 1-Propanol (2) - Gas	Vapor or sublimation pressure, kPa - Liquid
0.0151	38.52
0.0248	38.73
0.0688	39.59
0.0883	39.89
0.1271	39.56
0.1470	38.95
0.1666	38.72
0.1865	38.31
0.1972	37.79
0.2126	37.20
0.2271	36.15
0.2462	35.29
0.2599	34.06
0.2866	32.92
0.3206	31.09
0.3480	28.71
0.4192	25.16
0.4854	22.31
0.5734	19.56
0.6355	17.98

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of 1-Propanol (2) - Liquid	Refractive index (Na D-line) - Liquid
0.0495	1.4926
0.1012	1.4869
0.1997	1.4761
0.3007	1.4653
0.4002	1.4546
0.4999	1.4437
0.6002	1.4324
0.7000	1.4206
0.8004	1.4086
0.8999	1.396
0.9496	1.3897

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of 1-Propanol (2) - Liquid	Refractive index (Na D-line) - Liquid
0.0495	1.4926
0.1012	1.4869
0.1997	1.4761
0.3007	1.4653
0.4002	1.4546
0.4999	1.4437
0.6002	1.4324
0.7000	1.4206
0.8004	1.4086
0.8999	1.396
0.9496	1.3897

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of 1-Propanol (2) - Liquid	Mass density, kg/m3 - Liquid
0.0495	869.79
0.1012	866.16
0.1997	859.49
0.3007	852.8
0.4002	846.08
0.4999	839.22
0.6002	832.14
0.7000	824.83
0.8004	817.26
0.8999	809.29
0.9496	805.03

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Propanol (2) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	884.246
288.15	0.0220	882.511
288.15	0.0557	880.03
288.15	0.0984	876.959
288.15	0.1632	872.435
288.15	0.2186	868.541
288.15	0.2385	867.148
288.15	0.3046	862.546
288.15	0.3993	855.836
288.15	0.4505	852.174
288.15	0.5023	848.393
288.15	0.6035	840.846
288.15	0.6600	836.494
288.15	0.7035	833.115
288.15	0.7453	829.801
288.15	0.8016	825.211
288.15	0.8447	821.474
288.15	0.8981	816.954
288.15	0.9495	812.375
288.15	1.0000	807.69
293.15	0.0000	878.918
293.15	0.0220	877.177
293.15	0.0557	874.714
293.15	0.0984	871.673
293.15	0.1632	867.203
293.15	0.2186	863.367
293.15	0.2385	861.999
293.15	0.3046	857.468
293.15	0.3993	850.881
293.15	0.4505	847.288
293.15	0.5023	843.581
293.15	0.6035	836.186
293.15	0.6600	831.916
293.15	0.7035	828.615
293.15	0.7453	825.366
293.15	0.8016	820.875
293.15	0.8447	817.209
293.15	0.8981	812.786
293.15	0.9495	808.313
293.15	1.0000	803.703
298.15	0.0000	873.582
298.15	0.0220	871.937
298.15	0.0557	869.383
298.15	0.0984	866.369
298.15	0.1632	861.955
298.15	0.2186	858.172
298.15	0.2385	856.826
298.15	0.3046	852.368
298.15	0.3993	845.896
298.15	0.4505	842.37
298.15	0.5023	838.736
298.15	0.6035	831.492
298.15	0.6600	827.312
298.15	0.7035	824.081
298.15	0.7453	820.902
298.15	0.8016	816.507
298.15	0.8447	812.998
298.15	0.8981	808.589
298.15	0.9495	804.141
298.15	1.0000	799.692
303.15	0.0000	868.233
303.15	0.0220	866.489
303.15	0.0557	864.034
303.15	0.0984	861.047
303.15	0.1632	856.682
303.15	0.2186	852.95
303.15	0.2385	851.625
303.15	0.3046	847.234
303.15	0.3993	840.877
303.15	0.4505	837.417
303.15	0.5023	833.856
303.15	0.6035	826.762
303.15	0.6600	822.69
303.15	0.7035	819.512
303.15	0.7453	816.4
303.15	0.8016	812.105
303.15	0.8447	808.593
303.15	0.8981	804.36
303.15	0.9495	800.008
303.15	1.0000	795.65
308.15	0.0000	862.871
308.15	0.0220	861.124
308.15	0.0557	858.669
308.15	0.0984	855.699
308.15	0.1632	851.38
308.15	0.2186	847.699
308.15	0.2385	846.396
308.15	0.3046	842.067
308.15	0.3993	835.823
308.15	0.4505	832.428
308.15	0.5023	828.935
308.15	0.6035	821.989
308.15	0.6600	817.981
308.15	0.7035	814.9
308.15	0.7453	811.856
308.15	0.8016	807.61
308.15	0.8447	804.229
308.15	0.8981	800.093
308.15	0.9495	795.838
308.15	1.0000	791.576
313.15	0.0000	857.498
313.15	0.0220	855.764
313.15	0.0557	853.296
313.15	0.0984	850.343
313.15	0.1632	846.063
313.15	0.2186	842.427
313.15	0.2385	841.156
313.15	0.3046	836.875
313.15	0.3993	830.744
313.15	0.4505	827.425
313.15	0.5023	823.986
313.15	0.6035	817.183
313.15	0.6600	813.261
313.15	0.7035	810.256
313.15	0.7453	807.285
313.15	0.8016	803.184
313.15	0.8447	799.833
313.15	0.8981	795.804
313.15	0.9495	791.644
313.15	1.0000	787.466

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of 1-Propanol (2) - Liquid	Mass density, kg/m3 - Liquid
0.0495	869.79
0.1012	866.16
0.1997	859.49
0.3007	852.8
0.4002	846.08
0.4999	839.22
0.6002	832.14
0.7000	824.83
0.8004	817.26
0.8999	809.29
0.9496	805.03

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Propanol (2) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	884.246
288.15	0.0220	882.511
288.15	0.0557	880.03
288.15	0.0984	876.959
288.15	0.1632	872.435
288.15	0.2186	868.541
288.15	0.2385	867.148
288.15	0.3046	862.546
288.15	0.3993	855.836
288.15	0.4505	852.174
288.15	0.5023	848.393
288.15	0.6035	840.846
288.15	0.6600	836.494
288.15	0.7035	833.115
288.15	0.7453	829.801
288.15	0.8016	825.211
288.15	0.8447	821.474
288.15	0.8981	816.954
288.15	0.9495	812.375
288.15	1.0000	807.69
293.15	0.0000	878.918
293.15	0.0220	877.177
293.15	0.0557	874.714
293.15	0.0984	871.673
293.15	0.1632	867.203
293.15	0.2186	863.367
293.15	0.2385	861.999
293.15	0.3046	857.468
293.15	0.3993	850.881
293.15	0.4505	847.288
293.15	0.5023	843.581
293.15	0.6035	836.186
293.15	0.6600	831.916
293.15	0.7035	828.615
293.15	0.7453	825.366
293.15	0.8016	820.875
293.15	0.8447	817.209
293.15	0.8981	812.786
293.15	0.9495	808.313
293.15	1.0000	803.703
298.15	0.0000	873.582
298.15	0.0220	871.937
298.15	0.0557	869.383
298.15	0.0984	866.369
298.15	0.1632	861.955
298.15	0.2186	858.172
298.15	0.2385	856.826
298.15	0.3046	852.368
298.15	0.3993	845.896
298.15	0.4505	842.37
298.15	0.5023	838.736
298.15	0.6035	831.492
298.15	0.6600	827.312
298.15	0.7035	824.081
298.15	0.7453	820.902
298.15	0.8016	816.507
298.15	0.8447	812.998
298.15	0.8981	808.589
298.15	0.9495	804.141
298.15	1.0000	799.692
303.15	0.0000	868.233
303.15	0.0220	866.489
303.15	0.0557	864.034
303.15	0.0984	861.047
303.15	0.1632	856.682
303.15	0.2186	852.95
303.15	0.2385	851.625
303.15	0.3046	847.234
303.15	0.3993	840.877
303.15	0.4505	837.417
303.15	0.5023	833.856
303.15	0.6035	826.762
303.15	0.6600	822.69
303.15	0.7035	819.512
303.15	0.7453	816.4
303.15	0.8016	812.105
303.15	0.8447	808.593
303.15	0.8981	804.36
303.15	0.9495	800.008
303.15	1.0000	795.65
308.15	0.0000	862.871
308.15	0.0220	861.124
308.15	0.0557	858.669
308.15	0.0984	855.699
308.15	0.1632	851.38
308.15	0.2186	847.699
308.15	0.2385	846.396
308.15	0.3046	842.067
308.15	0.3993	835.823
308.15	0.4505	832.428
308.15	0.5023	828.935
308.15	0.6035	821.989
308.15	0.6600	817.981
308.15	0.7035	814.9
308.15	0.7453	811.856
308.15	0.8016	807.61
308.15	0.8447	804.229
308.15	0.8981	800.093
308.15	0.9495	795.838
308.15	1.0000	791.576
313.15	0.0000	857.498
313.15	0.0220	855.764
313.15	0.0557	853.296
313.15	0.0984	850.343
313.15	0.1632	846.063
313.15	0.2186	842.427
313.15	0.2385	841.156
313.15	0.3046	836.875
313.15	0.3993	830.744
313.15	0.4505	827.425
313.15	0.5023	823.986
313.15	0.6035	817.183
313.15	0.6600	813.261
313.15	0.7035	810.256
313.15	0.7453	807.285
313.15	0.8016	803.184
313.15	0.8447	799.833
313.15	0.8981	795.804
313.15	0.9495	791.644
313.15	1.0000	787.466

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 308.15 (Liquid)
• Frequency, MHz = 2 (Liquid)

Mole fraction of Benzene (1) - Liquid	Speed of sound, m/s - Liquid
0.0852	1192.0
0.1733	1196.0
0.2644	1200.0
0.3059	1201.0
0.3586	1203.0
0.3995	1204.0
0.4561	1206.0
0.5274	1208.0
0.5820	1210.0
0.6618	1213.0
0.7267	1216.0
0.7703	1219.0
0.8830	1233.0
0.9335	1242.0

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 308.15 (Liquid)
• Frequency, MHz = 2 (Liquid)

Mole fraction of Benzene (1) - Liquid	Speed of sound, m/s - Liquid
0.0852	1192.0
0.1733	1196.0
0.2644	1200.0
0.3059	1201.0
0.3586	1203.0
0.3995	1204.0
0.4561	1206.0
0.5274	1208.0
0.5820	1210.0
0.6618	1213.0
0.7267	1216.0
0.7703	1219.0
0.8830	1233.0
0.9335	1242.0

Sources

• Topological Investigations of Excess Molar Volumes and Excess Isentropic Compressibilities of Ternary Mixtures Containing Pyrrolidin-2-one at 308.15 K
• Total pressure and excess Gibbs energy for the ternary mixture di-isopropyl ether + 1-propanol + benzene and its corresponding binary systems at 313.15K
• Isothermal vapor liquid equilibrium at 323.15K and excess molar volumes and refractive indices at 298.15K for the ternary system propyl vinyl ether + 1-propanol + benzene and its binary sub-systems
• Excess enthalpies of ternary mixtures of (oxygenated additives + aromatic hydrocarbon) mixtures in fuels and bio-fuels: (Dibutyl-ether + 1-propanol + benzene), or toluene, at T = (298.15 and 313.15) K
• Densities and Excess Molar Volumes of the Binary 1-Propanol + Chloroform and 1-Propanol + Benzene and Ternary 1-Propanol + Chloroform + Benzene Mixtures at (288.15, 293.15, 298.15, 303.15, 308.15, and 313.15) K