Mixture of Ethanol + Acetic acid, butyl ester

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Ethanol

Name
Ethanol
InChI
InChI=1S/C2H6O/c1-2-3/h3H,2H2,1H3
InChI Key
LFQSCWFLJHTTHZ-UHFFFAOYSA-N
Formula
C2H6O
SMILES
CCO
Mol. Weight (g/mol)
46.07
CAS
64-17-5

Acetic acid, butyl ester

Name
Acetic acid, butyl ester
InChI
InChI=1S/C6H12O2/c1-3-4-5-8-6(2)7/h3-5H2,1-2H3
InChI Key
DKPFZGUDAPQIHT-UHFFFAOYSA-N
Formula
C6H12O2
SMILES
CCCCOC(C)=O
Mol. Weight (g/mol)
116.16
CAS
123-86-4
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Datasets

  1. Mole fraction (2)
  2. η - Viscosity, Pa*s (2)
  3. ρl - Mass density, kg/m3 (4)
  4. Tboil - Boiling temperature at pressure P, K (2)
  5. Vapor Liquid Equilibrium at Constant Temperature (3)

Mole fraction of Acetic acid, butyl ester (2) [ref]

Operational condition: Pressure, kPa = 150 (Liquid)

Mole fraction of Acetic acid, butyl ester (2) - Liquid Mole fraction of Acetic acid, butyl ester (2) - Gas
0.0000 0.0000
0.0160 0.0100
0.0250 0.0150
0.0360 0.0220
0.0540 0.0290
0.0760 0.0400
0.0980 0.0490
0.1180 0.0530
0.1390 0.0620
0.1600 0.0720
0.1900 0.0790
0.2090 0.0860
0.2350 0.0900
0.2580 0.1020
0.2790 0.1080
0.3130 0.1180
0.3390 0.1260
0.3580 0.1300
0.3820 0.1360
0.4030 0.1440
0.4280 0.1510
0.4760 0.1600
0.5050 0.1680
0.5530 0.1790
0.5970 0.1960
0.6320 0.2100
0.6710 0.2360
0.6760 0.2300
0.6940 0.2360
0.7130 0.2470
0.7610 0.2800
0.7980 0.3070
0.8210 0.3310
0.8670 0.3980
0.9120 0.4970
0.9480 0.6360
0.9760 0.8010
0.9870 0.8920
1.0000 1.0000

Mole fraction of Acetic acid, butyl ester (2) [ref]

Operational condition: Pressure, kPa = 150 (Liquid)

Mole fraction of Acetic acid, butyl ester (2) - Liquid Mole fraction of Acetic acid, butyl ester (2) - Gas
0.0000 0.0000
0.0160 0.0100
0.0250 0.0150
0.0360 0.0220
0.0540 0.0290
0.0760 0.0400
0.0980 0.0490
0.1180 0.0530
0.1390 0.0620
0.1600 0.0720
0.1900 0.0790
0.2090 0.0860
0.2350 0.0900
0.2580 0.1020
0.2790 0.1080
0.3130 0.1180
0.3390 0.1260
0.3580 0.1300
0.3820 0.1360
0.4030 0.1440
0.4280 0.1510
0.4760 0.1600
0.5050 0.1680
0.5530 0.1790
0.5970 0.1960
0.6320 0.2100
0.6710 0.2360
0.6760 0.2300
0.6940 0.2360
0.7130 0.2470
0.7610 0.2800
0.7980 0.3070
0.8210 0.3310
0.8670 0.3980
0.9120 0.4970
0.9480 0.6360
0.9760 0.8010
0.9870 0.8920
1.0000 1.0000

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Acetic acid, butyl ester (2) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0012
293.15 0.1135 0.0011
293.15 0.2054 0.0011
293.15 0.3078 0.0010
293.15 0.4122 0.0010
293.15 0.5191 0.0009
293.15 0.6123 0.0009
293.15 0.7008 0.0008
293.15 0.8054 0.0008
293.15 0.9127 0.0008
293.15 1.0000 0.0007
303.15 0.0000 0.0010
303.15 0.1082 0.0009
303.15 0.2006 0.0009
303.15 0.3121 0.0008
303.15 0.4018 0.0008
303.15 0.5213 0.0008
303.15 0.6015 0.0007
303.15 0.7028 0.0007
303.15 0.8043 0.0007
303.15 0.9074 0.0007
303.15 1.0000 0.0006
313.15 0.0000 0.0008
313.15 0.1051 0.0008
313.15 0.1988 0.0007
313.15 0.3047 0.0007
313.15 0.4038 0.0007
313.15 0.5088 0.0007
313.15 0.6091 0.0006
313.15 0.7053 0.0006
313.15 0.8144 0.0006
313.15 0.9058 0.0006
313.15 1.0000 0.0005

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Acetic acid, butyl ester (2) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0012
293.15 0.1135 0.0011
293.15 0.2054 0.0011
293.15 0.3078 0.0010
293.15 0.4122 0.0010
293.15 0.5191 0.0009
293.15 0.6123 0.0009
293.15 0.7008 0.0008
293.15 0.8054 0.0008
293.15 0.9127 0.0008
293.15 1.0000 0.0007
303.15 0.0000 0.0010
303.15 0.1082 0.0009
303.15 0.2006 0.0009
303.15 0.3121 0.0008
303.15 0.4018 0.0008
303.15 0.5213 0.0008
303.15 0.6015 0.0007
303.15 0.7028 0.0007
303.15 0.8043 0.0007
303.15 0.9074 0.0007
303.15 1.0000 0.0006
313.15 0.0000 0.0008
313.15 0.1051 0.0008
313.15 0.1988 0.0007
313.15 0.3047 0.0007
313.15 0.4038 0.0007
313.15 0.5088 0.0007
313.15 0.6091 0.0006
313.15 0.7053 0.0006
313.15 0.8144 0.0006
313.15 0.9058 0.0006
313.15 1.0000 0.0005

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Acetic acid, butyl ester (2) - Liquid Mass density, kg/m3 - Liquid
0.0000 785.2
0.0443 793.7
0.1461 810.2
0.2003 817.6
0.2554 824.3
0.2954 828.8
0.3487 834.3
0.4451 843.0
0.4968 847.2
0.5987 854.6
0.6505 858.0
0.7492 863.9
0.8035 866.9
0.8567 869.7
0.8978 871.7
0.9429 873.9
1.0000 876.5

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Acetic acid, butyl ester (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 788.24
293.15 0.1135 799.54
293.15 0.2054 805.63
293.15 0.3078 815.47
293.15 0.4122 829.14
293.15 0.5191 836.41
293.15 0.6123 846.01
293.15 0.7008 852.17
293.15 0.8054 863.04
293.15 0.9127 872.94
293.15 1.0000 881.04
303.15 0.0000 780.73
303.15 0.1082 791.5
303.15 0.2006 799.54
303.15 0.3121 807.54
303.15 0.4018 817.14
303.15 0.5213 827.93
303.15 0.6015 834.68
303.15 0.7028 844.62
303.15 0.8043 853.58
303.15 0.9074 862.91
303.15 1.0000 871.3
313.15 0.0000 771.98
313.15 0.1051 780.51
313.15 0.1988 787.51
313.15 0.3047 799.06
313.15 0.4038 808.27
313.15 0.5088 817.7
313.15 0.6091 829.34
313.15 0.7053 835.36
313.15 0.8144 845.16
313.15 0.9058 857.73
313.15 1.0000 861.84

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Acetic acid, butyl ester (2) - Liquid Mass density, kg/m3 - Liquid
0.0000 785.2
0.0443 793.7
0.1461 810.2
0.2003 817.6
0.2554 824.3
0.2954 828.8
0.3487 834.3
0.4451 843.0
0.4968 847.2
0.5987 854.6
0.6505 858.0
0.7492 863.9
0.8035 866.9
0.8567 869.7
0.8978 871.7
0.9429 873.9
1.0000 876.5

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Acetic acid, butyl ester (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 788.24
293.15 0.1135 799.54
293.15 0.2054 805.63
293.15 0.3078 815.47
293.15 0.4122 829.14
293.15 0.5191 836.41
293.15 0.6123 846.01
293.15 0.7008 852.17
293.15 0.8054 863.04
293.15 0.9127 872.94
293.15 1.0000 881.04
303.15 0.0000 780.73
303.15 0.1082 791.5
303.15 0.2006 799.54
303.15 0.3121 807.54
303.15 0.4018 817.14
303.15 0.5213 827.93
303.15 0.6015 834.68
303.15 0.7028 844.62
303.15 0.8043 853.58
303.15 0.9074 862.91
303.15 1.0000 871.3
313.15 0.0000 771.98
313.15 0.1051 780.51
313.15 0.1988 787.51
313.15 0.3047 799.06
313.15 0.4038 808.27
313.15 0.5088 817.7
313.15 0.6091 829.34
313.15 0.7053 835.36
313.15 0.8144 845.16
313.15 0.9058 857.73
313.15 1.0000 861.84

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 150 (Liquid)

Mole fraction of Acetic acid, butyl ester (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 361.98
0.0160 362.29
0.0250 362.33
0.0360 362.42
0.0540 362.74
0.0760 362.99
0.0980 363.35
0.1180 363.61
0.1390 363.90
0.1600 364.16
0.1900 364.54
0.2090 364.82
0.2350 365.20
0.2580 365.66
0.2790 366.06
0.3130 366.59
0.3390 367.02
0.3580 367.38
0.3820 367.73
0.4030 368.19
0.4280 368.60
0.4760 369.34
0.5050 369.98
0.5530 370.84
0.5970 372.07
0.6320 373.29
0.6710 375.12
0.6760 374.98
0.6940 375.43
0.7130 376.21
0.7610 378.61
0.7980 380.96
0.8210 382.83
0.8670 387.28
0.9120 393.43
0.9480 399.96
0.9760 406.25
0.9870 409.34
1.0000 413.30

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 150 (Liquid)

Mole fraction of Acetic acid, butyl ester (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 361.98
0.0160 362.29
0.0250 362.33
0.0360 362.42
0.0540 362.74
0.0760 362.99
0.0980 363.35
0.1180 363.61
0.1390 363.90
0.1600 364.16
0.1900 364.54
0.2090 364.82
0.2350 365.20
0.2580 365.66
0.2790 366.06
0.3130 366.59
0.3390 367.02
0.3580 367.38
0.3820 367.73
0.4030 368.19
0.4280 368.60
0.4760 369.34
0.5050 369.98
0.5530 370.84
0.5970 372.07
0.6320 373.29
0.6710 375.12
0.6760 374.98
0.6940 375.43
0.7130 376.21
0.7610 378.61
0.7980 380.96
0.8210 382.83
0.8670 387.28
0.9120 393.43
0.9480 399.96
0.9760 406.25
0.9870 409.34
1.0000 413.30

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 323.15 (VLE)

P [kPa] - VLE x1[mol/mol] of Ethanol (1) - Liquid
6.27 0.0000
9.07 0.0500
11.7 0.1000
16.3 0.2000
19.5 0.3000
22.0 0.4000
23.899 0.5000
26.001 0.6000
26.9 0.7000
28.0 0.8000
28.7 0.9000
29.1 0.9500
29.3 1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 333.15 (VLE)

P [kPa] - VLE x1[mol/mol] of Ethanol (1) - Liquid
9.801 0.0000
14.7 0.0500
18.7 0.1000
24.901 0.2000
29.7 0.3000
33.6 0.4000
36.9 0.5000
39.699 0.6000
42.001 0.7000
44.1 0.8000
45.9 0.9000
46.4 0.9500
47.0 1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 343.15 (VLE)

P [kPa] - VLE x1[mol/mol] of Ethanol (1) - Liquid
14.9 0.0000
22.299 0.0500
28.0 0.1000
37.3 0.2000
44.9 0.3000
51.2 0.4000
56.399 0.5000
60.7 0.6000
64.4 0.7000
68.0 0.8000
70.7 0.9000
71.499 0.9500
72.099 1.0000

Sources