Mixture of 1-Propanol + Acetic acid, butyl ester + Water

Datasets

1. Mole fraction (4)
2. η - Viscosity, Pa*s (2)
3. Interfacial tension, N/m (2)
4. ρ_l - Mass density, kg/m3 (2)
5. γ - Surface tension liquid-gas, N/m (4)

Mole fraction of Water (3) [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid mixture 2)
• Temperature, K = 323.15 (Liquid mixture 2)

Mole fraction of Acetic acid, butyl ester (2) - Liquid mixture 2	Mole fraction of Water (3) - Liquid mixture 2
0.0008	0.9899
0.0008	0.9811
0.0012	0.9568
0.0029	0.9402
0.0029	0.9396
0.0044	0.9256
0.0064	0.9111
0.0079	0.8965
0.0097	0.8855
0.0118	0.8775
0.0120	0.8768
0.0150	0.8605
0.0152	0.8544
0.0197	0.8310
0.0266	0.7981
0.0346	0.7630
0.0460	0.7211
0.0611	0.6743
0.0824	0.6266
0.1048	0.5911
0.1208	0.5671
0.1234	0.5626
0.1244	0.5623
0.1485	0.5300
0.1786	0.4946
0.2110	0.4621
0.2434	0.4322
0.2728	0.4086
0.3321	0.3626
0.3349	0.3601
0.3956	0.3178
0.4687	0.2797
0.5197	0.2515
0.6204	0.2052
0.6499	0.1919
0.7187	0.1613
0.7636	0.1464
0.7938	0.1366
0.8155	0.1204
0.8207	0.1289
0.8555	0.1220
0.8790	0.1210

Mole fraction [ref]

Operational conditions:

• Temperature, K = 323.15 (Liquid mixture 2)
• Pressure, kPa = 101 (Liquid mixture 2)

Fixed	Measured
Mole fraction of Water (3) - Liquid mixture 1	Mole fraction of 1-Propanol (1) - Liquid mixture 1	Mole fraction of 1-Propanol (1) - Liquid mixture 2	Mole fraction of Water (3) - Liquid mixture 2
0.9998	0.0000	0.0000	0.1305
0.9842	0.0154	0.1664	0.2009
0.9757	0.0238	0.2593	0.2769
0.9643	0.0349	0.3279	0.4117
0.9580	0.0410	0.3363	0.4889

Mole fraction of Water (3) [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid mixture 2)
• Temperature, K = 323.15 (Liquid mixture 2)

Mole fraction of Acetic acid, butyl ester (2) - Liquid mixture 2	Mole fraction of Water (3) - Liquid mixture 2
0.0008	0.9899
0.0008	0.9811
0.0012	0.9568
0.0029	0.9402
0.0029	0.9396
0.0044	0.9256
0.0064	0.9111
0.0079	0.8965
0.0097	0.8855
0.0118	0.8775
0.0120	0.8768
0.0150	0.8605
0.0152	0.8544
0.0197	0.8310
0.0266	0.7981
0.0346	0.7630
0.0460	0.7211
0.0611	0.6743
0.0824	0.6266
0.1048	0.5911
0.1208	0.5671
0.1234	0.5626
0.1244	0.5623
0.1485	0.5300
0.1786	0.4946
0.2110	0.4621
0.2434	0.4322
0.2728	0.4086
0.3321	0.3626
0.3349	0.3601
0.3956	0.3178
0.4687	0.2797
0.5197	0.2515
0.6204	0.2052
0.6499	0.1919
0.7187	0.1613
0.7636	0.1464
0.7938	0.1366
0.8155	0.1204
0.8207	0.1289
0.8555	0.1220
0.8790	0.1210

Mole fraction [ref]

Operational conditions:

• Temperature, K = 323.15 (Liquid mixture 2)
• Pressure, kPa = 101 (Liquid mixture 2)

Fixed	Measured
Mole fraction of Water (3) - Liquid mixture 1	Mole fraction of 1-Propanol (1) - Liquid mixture 1	Mole fraction of 1-Propanol (1) - Liquid mixture 2	Mole fraction of Water (3) - Liquid mixture 2
0.9998	0.0000	0.0000	0.1305
0.9842	0.0154	0.1664	0.2009
0.9757	0.0238	0.2593	0.2769
0.9643	0.0349	0.3279	0.4117
0.9580	0.0410	0.3363	0.4889

Viscosity, Pa*s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 323.15 (Liquid)

Fixed		Measured
Mole fraction of Water (3) - Liquid	Mole fraction of Acetic acid, butyl ester (2) - Liquid	Viscosity, Pa*s - Liquid
0.0000	0.1000	0.0009
0.0000	0.2000	0.0007
0.0000	0.3000	0.0007
0.0000	0.4000	0.0006
0.0000	0.5000	0.0006
0.0000	0.6000	0.0005
0.0000	0.7000	0.0005
0.0000	0.8000	0.0005
0.0000	0.9000	0.0005
0.0100	0.9000	0.0005
0.0200	0.8000	0.0005
0.0200	0.9800	0.0005
0.0300	0.9000	0.0005
0.0400	0.6000	0.0005
0.0400	0.9600	0.0005
0.0500	0.0000	0.0011
0.0500	0.9000	0.0005
0.0600	0.4000	0.0006
0.0600	0.7000	0.0005
0.0600	0.8000	0.0005
0.0600	0.9400	0.0005
0.0800	0.2000	0.0008
0.0800	0.9200	0.0005
0.0900	0.1000	0.0009
0.1000	0.0000	0.0011
0.1000	0.5000	0.0006
0.1000	0.8000	0.0005
0.1200	0.6000	0.0006
0.1200	0.7000	0.0005
0.1400	0.3000	0.0007
0.1800	0.1000	0.0009
0.1800	0.4000	0.0006
0.2000	0.0000	0.0011
0.2000	0.5000	0.0006
0.2000	0.6000	0.0006
0.2400	0.2000	0.0008
0.2800	0.3000	0.0007
0.3000	0.0000	0.0012
0.3000	0.4000	0.0007
0.3600	0.1000	0.0010
0.4000	0.0000	0.0012
0.4000	0.2000	0.0008
0.4500	0.1000	0.0010
0.5000	0.0000	0.0013
0.5100	0.1500	0.0009
0.5700	0.0500	0.0012
0.6000	0.0000	0.0013
0.6650	0.0500	0.0012
0.7000	0.0000	0.0013
0.7800	0.0250	0.0013
0.8000	0.0000	0.0013
0.9000	0.0000	0.0010
0.9500	0.0000	0.0008

Viscosity, Pa*s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 323.15 (Liquid)

Fixed		Measured
Mole fraction of Water (3) - Liquid	Mole fraction of Acetic acid, butyl ester (2) - Liquid	Viscosity, Pa*s - Liquid
0.0000	0.1000	0.0009
0.0000	0.2000	0.0007
0.0000	0.3000	0.0007
0.0000	0.4000	0.0006
0.0000	0.5000	0.0006
0.0000	0.6000	0.0005
0.0000	0.7000	0.0005
0.0000	0.8000	0.0005
0.0000	0.9000	0.0005
0.0100	0.9000	0.0005
0.0200	0.8000	0.0005
0.0200	0.9800	0.0005
0.0300	0.9000	0.0005
0.0400	0.6000	0.0005
0.0400	0.9600	0.0005
0.0500	0.0000	0.0011
0.0500	0.9000	0.0005
0.0600	0.4000	0.0006
0.0600	0.7000	0.0005
0.0600	0.8000	0.0005
0.0600	0.9400	0.0005
0.0800	0.2000	0.0008
0.0800	0.9200	0.0005
0.0900	0.1000	0.0009
0.1000	0.0000	0.0011
0.1000	0.5000	0.0006
0.1000	0.8000	0.0005
0.1200	0.6000	0.0006
0.1200	0.7000	0.0005
0.1400	0.3000	0.0007
0.1800	0.1000	0.0009
0.1800	0.4000	0.0006
0.2000	0.0000	0.0011
0.2000	0.5000	0.0006
0.2000	0.6000	0.0006
0.2400	0.2000	0.0008
0.2800	0.3000	0.0007
0.3000	0.0000	0.0012
0.3000	0.4000	0.0007
0.3600	0.1000	0.0010
0.4000	0.0000	0.0012
0.4000	0.2000	0.0008
0.4500	0.1000	0.0010
0.5000	0.0000	0.0013
0.5100	0.1500	0.0009
0.5700	0.0500	0.0012
0.6000	0.0000	0.0013
0.6650	0.0500	0.0012
0.7000	0.0000	0.0013
0.7800	0.0250	0.0013
0.8000	0.0000	0.0013
0.9000	0.0000	0.0010
0.9500	0.0000	0.0008

Interfacial tension, N/m [ref]

Operational condition: Temperature, K = 323.15 (Liquid mixture 1)

Fixed		Measured
Mole fraction of Water (3) - Liquid mixture 1	Mole fraction of 1-Propanol (1) - Liquid mixture 1	Interfacial tension, N/m - Liquid mixture 1
0.9580	0.0410	0.0000
0.9643	0.0349	0.0028
0.9757	0.0238	0.0054
0.9842	0.0154	0.0073
0.9998	0.0000	0.0142

Interfacial tension, N/m [ref]

Operational condition: Temperature, K = 323.15 (Liquid mixture 1)

Fixed		Measured
Mole fraction of Water (3) - Liquid mixture 1	Mole fraction of 1-Propanol (1) - Liquid mixture 1	Interfacial tension, N/m - Liquid mixture 1
0.9580	0.0410	0.0000
0.9643	0.0349	0.0028
0.9757	0.0238	0.0054
0.9842	0.0154	0.0073
0.9998	0.0000	0.0142

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 323.15 (Liquid)

Fixed		Measured
Mole fraction of Water (3) - Liquid	Mole fraction of Acetic acid, butyl ester (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	0.1000	790.07
0.0000	0.2000	799.51
0.0000	0.3000	807.87
0.0000	0.4000	815.42
0.0000	0.5000	822.21
0.0000	0.6000	828.46
0.0000	0.7000	834.3
0.0000	0.8000	839.71
0.0000	0.9000	844.84
0.0100	0.9000	845.52
0.0200	0.8000	841.05
0.0200	0.9800	850.18
0.0300	0.9000	846.96
0.0400	0.6000	831.4
0.0400	0.9600	850.62
0.0500	0.0000	782.94
0.0500	0.9000	848.39
0.0600	0.4000	819.88
0.0600	0.7000	838.57
0.0600	0.8000	843.96
0.0600	0.9400	851.07
0.0800	0.2000	805.43
0.0800	0.9200	851.57
0.0900	0.1000	796.69
0.1000	0.0000	786.61
0.1000	0.5000	829.79
0.1000	0.8000	847.01
0.1200	0.6000	837.5
0.1200	0.7000	843.22
0.1400	0.3000	818.69
0.1800	0.1000	804.03
0.1800	0.4000	829.64
0.2000	0.0000	794.62
0.2000	0.5000	838.12
0.2000	0.6000	844.23
0.2400	0.2000	818.98
0.2800	0.3000	831.54
0.3000	0.0000	803.64
0.3000	0.4000	840.95
0.3600	0.1000	821.79
0.4000	0.0000	814.4
0.4000	0.2000	836.12
0.4500	0.1000	832.58
0.5000	0.0000	827.68
0.5100	0.1500	845.85
0.5700	0.0500	845.07
0.6000	0.0000	844.41
0.6650	0.0500	863.01
0.7000	0.0000	865.87
0.7800	0.0250	889.99
0.8000	0.0000	894.61
0.9000	0.0000	935.04
0.9500	0.0000	959.71

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 323.15 (Liquid)

Fixed		Measured
Mole fraction of Water (3) - Liquid	Mole fraction of Acetic acid, butyl ester (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	0.1000	790.07
0.0000	0.2000	799.51
0.0000	0.3000	807.87
0.0000	0.4000	815.42
0.0000	0.5000	822.21
0.0000	0.6000	828.46
0.0000	0.7000	834.3
0.0000	0.8000	839.71
0.0000	0.9000	844.84
0.0100	0.9000	845.52
0.0200	0.8000	841.05
0.0200	0.9800	850.18
0.0300	0.9000	846.96
0.0400	0.6000	831.4
0.0400	0.9600	850.62
0.0500	0.0000	782.94
0.0500	0.9000	848.39
0.0600	0.4000	819.88
0.0600	0.7000	838.57
0.0600	0.8000	843.96
0.0600	0.9400	851.07
0.0800	0.2000	805.43
0.0800	0.9200	851.57
0.0900	0.1000	796.69
0.1000	0.0000	786.61
0.1000	0.5000	829.79
0.1000	0.8000	847.01
0.1200	0.6000	837.5
0.1200	0.7000	843.22
0.1400	0.3000	818.69
0.1800	0.1000	804.03
0.1800	0.4000	829.64
0.2000	0.0000	794.62
0.2000	0.5000	838.12
0.2000	0.6000	844.23
0.2400	0.2000	818.98
0.2800	0.3000	831.54
0.3000	0.0000	803.64
0.3000	0.4000	840.95
0.3600	0.1000	821.79
0.4000	0.0000	814.4
0.4000	0.2000	836.12
0.4500	0.1000	832.58
0.5000	0.0000	827.68
0.5100	0.1500	845.85
0.5700	0.0500	845.07
0.6000	0.0000	844.41
0.6650	0.0500	863.01
0.7000	0.0000	865.87
0.7800	0.0250	889.99
0.8000	0.0000	894.61
0.9000	0.0000	935.04
0.9500	0.0000	959.71

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 323.15 (Liquid mixture 2)

Fixed		Measured
Mole fraction of Water (3) - Liquid mixture 2	Mole fraction of 1-Propanol (1) - Liquid mixture 2	Surface tension liquid-gas, N/m - Liquid mixture 2
0.1305	0.0000	0.0217
0.2009	0.1664	0.0224
0.2769	0.2593	0.0222
0.4117	0.3279	0.0224
0.4889	0.3363	0.0226

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 323.15 (Liquid)

Fixed		Measured
Mole fraction of Water (3) - Liquid	Mole fraction of Acetic acid, butyl ester (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
0.0000	0.1000	0.0216
0.0000	0.2000	0.0217
0.0000	0.3000	0.0218
0.0000	0.4000	0.0220
0.0000	0.5000	0.0221
0.0000	0.6000	0.0221
0.0000	0.7000	0.0222
0.0000	0.8000	0.0222
0.0000	0.9000	0.0222
0.0100	0.9000	0.0221
0.0200	0.8000	0.0221
0.0200	0.9800	0.0221
0.0300	0.9000	0.0223
0.0400	0.6000	0.0221
0.0400	0.9600	0.0222
0.0500	0.0000	0.0215
0.0500	0.9000	0.0224
0.0600	0.4000	0.0220
0.0600	0.7000	0.0222
0.0600	0.8000	0.0223
0.0600	0.9400	0.0222
0.0800	0.2000	0.0219
0.0800	0.9200	0.0222
0.0900	0.1000	0.0218
0.1000	0.0000	0.0217
0.1000	0.5000	0.0222
0.1000	0.8000	0.0225
0.1200	0.6000	0.0223
0.1200	0.7000	0.0224
0.1400	0.3000	0.0222
0.1800	0.1000	0.0221
0.1800	0.4000	0.0224
0.2000	0.0000	0.0219
0.2000	0.5000	0.0226
0.2000	0.6000	0.0225
0.2400	0.2000	0.0224
0.2800	0.3000	0.0226
0.3000	0.0000	0.0223
0.3000	0.4000	0.0227
0.3600	0.1000	0.0227
0.4000	0.0000	0.0227
0.4000	0.2000	0.0228
0.4500	0.1000	0.0230
0.5000	0.0000	0.0231
0.5100	0.1500	0.0230
0.5700	0.0500	0.0231
0.6000	0.0000	0.0234
0.6650	0.0500	0.0231
0.7000	0.0000	0.0237
0.7800	0.0250	0.0235
0.8000	0.0000	0.0241
0.9000	0.0000	0.0253
0.9200	0.0000	0.0264
0.9500	0.0000	0.0296
0.9800	0.0000	0.0444

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 323.15 (Liquid mixture 2)

Fixed		Measured
Mole fraction of Water (3) - Liquid mixture 2	Mole fraction of 1-Propanol (1) - Liquid mixture 2	Surface tension liquid-gas, N/m - Liquid mixture 2
0.1305	0.0000	0.0217
0.2009	0.1664	0.0224
0.2769	0.2593	0.0222
0.4117	0.3279	0.0224
0.4889	0.3363	0.0226

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 323.15 (Liquid)

Fixed		Measured
Mole fraction of Water (3) - Liquid	Mole fraction of Acetic acid, butyl ester (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
0.0000	0.1000	0.0216
0.0000	0.2000	0.0217
0.0000	0.3000	0.0218
0.0000	0.4000	0.0220
0.0000	0.5000	0.0221
0.0000	0.6000	0.0221
0.0000	0.7000	0.0222
0.0000	0.8000	0.0222
0.0000	0.9000	0.0222
0.0100	0.9000	0.0221
0.0200	0.8000	0.0221
0.0200	0.9800	0.0221
0.0300	0.9000	0.0223
0.0400	0.6000	0.0221
0.0400	0.9600	0.0222
0.0500	0.0000	0.0215
0.0500	0.9000	0.0224
0.0600	0.4000	0.0220
0.0600	0.7000	0.0222
0.0600	0.8000	0.0223
0.0600	0.9400	0.0222
0.0800	0.2000	0.0219
0.0800	0.9200	0.0222
0.0900	0.1000	0.0218
0.1000	0.0000	0.0217
0.1000	0.5000	0.0222
0.1000	0.8000	0.0225
0.1200	0.6000	0.0223
0.1200	0.7000	0.0224
0.1400	0.3000	0.0222
0.1800	0.1000	0.0221
0.1800	0.4000	0.0224
0.2000	0.0000	0.0219
0.2000	0.5000	0.0226
0.2000	0.6000	0.0225
0.2400	0.2000	0.0224
0.2800	0.3000	0.0226
0.3000	0.0000	0.0223
0.3000	0.4000	0.0227
0.3600	0.1000	0.0227
0.4000	0.0000	0.0227
0.4000	0.2000	0.0228
0.4500	0.1000	0.0230
0.5000	0.0000	0.0231
0.5100	0.1500	0.0230
0.5700	0.0500	0.0231
0.6000	0.0000	0.0234
0.6650	0.0500	0.0231
0.7000	0.0000	0.0237
0.7800	0.0250	0.0235
0.8000	0.0000	0.0241
0.9000	0.0000	0.0253
0.9200	0.0000	0.0264
0.9500	0.0000	0.0296
0.9800	0.0000	0.0444

Sources

• Liquid-Liquid Equilibria, Density, Viscosity, and Surface and Interfacial Tension of the System Water + n-Butyl Acetate + 1-Propanol at 323.15 K and Atmospheric Pressure