Mixture of Acetic acid + Ethyl Acetate

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Acetic acid

Name
Acetic acid
InChI
InChI=1S/C2H4O2/c1-2(3)4/h1H3,(H,3,4)
InChI Key
QTBSBXVTEAMEQO-UHFFFAOYSA-N
Formula
C2H4O2
SMILES
CC(=O)O
Mol. Weight (g/mol)
60.05
CAS
64-19-7

Ethyl Acetate

Name
Ethyl Acetate
InChI
InChI=1S/C4H8O2/c1-3-6-4(2)5/h3H2,1-2H3
InChI Key
XEKOWRVHYACXOJ-UHFFFAOYSA-N
Formula
C4H8O2
SMILES
CCOC(C)=O
Mol. Weight (g/mol)
88.11
CAS
141-78-6
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Datasets

  1. Mole fraction (2)
  2. η - Viscosity, Pa*s (2)
  3. Excess molar enthalpy (molar enthalpy (2)
  4. ρl - Mass density, kg/m3 (2)
  5. csound,fluid - Speed of Sound, m/s (2)
  6. Tboil - Boiling temperature at pressure P, K (6)
  7. Vapor Liquid Equilibrium at Constant Pressure
  8. Vapor Liquid Equilibrium at Constant Temperature (2)
  9. Vapor or sublimation pressure, kPa (2)

Mole fraction of Ethyl Acetate (2) [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid Mole fraction of Ethyl Acetate (2) - Gas
0.0238 0.0825
0.0366 0.1189
0.0476 0.1518
0.0776 0.2443
0.0907 0.2718
0.1170 0.3265
0.1410 0.3795
0.1657 0.4297
0.2203 0.5369
0.2661 0.6113
0.3085 0.6739
0.3924 0.7621
0.4617 0.8215
0.4924 0.8463
0.5332 0.8702
0.5559 0.8820
0.6068 0.9074
0.6568 0.9266
0.6986 0.9439
0.7426 0.9571
0.7974 0.9710
0.8415 0.9769
0.8644 0.9811
0.9197 0.9898
0.9482 0.9938
0.9809 0.9968

Mole fraction of Ethyl Acetate (2) [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid Mole fraction of Ethyl Acetate (2) - Gas
0.0238 0.0825
0.0366 0.1189
0.0476 0.1518
0.0776 0.2443
0.0907 0.2718
0.1170 0.3265
0.1410 0.3795
0.1657 0.4297
0.2203 0.5369
0.2661 0.6113
0.3085 0.6739
0.3924 0.7621
0.4617 0.8215
0.4924 0.8463
0.5332 0.8702
0.5559 0.8820
0.6068 0.9074
0.6568 0.9266
0.6986 0.9439
0.7426 0.9571
0.7974 0.9710
0.8415 0.9769
0.8644 0.9811
0.9197 0.9898
0.9482 0.9938
0.9809 0.9968

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Acetic acid (1) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0005
293.15 0.0697 0.0005
293.15 0.0988 0.0005
293.15 0.1960 0.0005
293.15 0.2944 0.0006
293.15 0.3968 0.0006
293.15 0.5007 0.0007
293.15 0.5967 0.0007
293.15 0.7000 0.0008
293.15 0.7989 0.0009
293.15 0.8993 0.0011
293.15 0.9493 0.0011
293.15 1.0000 0.0012
298.15 0.0000 0.0004
298.15 0.0697 0.0004
298.15 0.0988 0.0005
298.15 0.1960 0.0005
298.15 0.2944 0.0005
298.15 0.3968 0.0006
298.15 0.5007 0.0006
298.15 0.5967 0.0007
298.15 0.7000 0.0008
298.15 0.7989 0.0008
298.15 0.8993 0.0010
298.15 0.9493 0.0010
298.15 1.0000 0.0011
303.15 0.0000 0.0004
303.15 0.0697 0.0004
303.15 0.0988 0.0004
303.15 0.1960 0.0005
303.15 0.2944 0.0005
303.15 0.3968 0.0005
303.15 0.5007 0.0006
303.15 0.5967 0.0006
303.15 0.7000 0.0007
303.15 0.7989 0.0008
303.15 0.8993 0.0009
303.15 0.9493 0.0010
303.15 1.0000 0.0010

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Acetic acid (1) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0005
293.15 0.0697 0.0005
293.15 0.0988 0.0005
293.15 0.1960 0.0005
293.15 0.2944 0.0006
293.15 0.3968 0.0006
293.15 0.5007 0.0007
293.15 0.5967 0.0007
293.15 0.7000 0.0008
293.15 0.7989 0.0009
293.15 0.8993 0.0011
293.15 0.9493 0.0011
293.15 1.0000 0.0012
298.15 0.0000 0.0004
298.15 0.0697 0.0004
298.15 0.0988 0.0005
298.15 0.1960 0.0005
298.15 0.2944 0.0005
298.15 0.3968 0.0006
298.15 0.5007 0.0006
298.15 0.5967 0.0007
298.15 0.7000 0.0008
298.15 0.7989 0.0008
298.15 0.8993 0.0010
298.15 0.9493 0.0010
298.15 1.0000 0.0011
303.15 0.0000 0.0004
303.15 0.0697 0.0004
303.15 0.0988 0.0004
303.15 0.1960 0.0005
303.15 0.2944 0.0005
303.15 0.3968 0.0005
303.15 0.5007 0.0006
303.15 0.5967 0.0006
303.15 0.7000 0.0007
303.15 0.7989 0.0008
303.15 0.8993 0.0009
303.15 0.9493 0.0010
303.15 1.0000 0.0010

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

Operational conditions:

Mole fraction of Ethyl Acetate (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0148 -0.0074
0.0300 -0.0148
0.0613 -0.0266
0.1108 -0.0387
0.1637 -0.0437
0.2403 -0.0394
0.3246 -0.0264
0.4179 -0.0055
0.5217 0.0219
0.6379 0.0539
0.7347 0.0730
0.8409 0.0786
0.9178 0.0638
0.9582 0.0440

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

Operational conditions:

Mole fraction of Ethyl Acetate (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0148 -0.0074
0.0300 -0.0148
0.0613 -0.0266
0.1108 -0.0387
0.1637 -0.0437
0.2403 -0.0394
0.3246 -0.0264
0.4179 -0.0055
0.5217 0.0219
0.6379 0.0539
0.7347 0.0730
0.8409 0.0786
0.9178 0.0638
0.9582 0.0440

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Acetic acid (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 900.52
293.15 0.0697 907.35
293.15 0.0988 910.56
293.15 0.1960 920.61
293.15 0.2944 931.46
293.15 0.3968 943.68
293.15 0.5007 957.31
293.15 0.5967 971.28
293.15 0.7000 987.79
293.15 0.7989 1005.47
293.15 0.8993 1025.8
293.15 0.9493 1037.09
293.15 1.0000 1049.3
298.15 0.0000 894.43
298.15 0.0697 901.3
298.15 0.0988 904.53
298.15 0.1960 914.62
298.15 0.2944 925.5
298.15 0.3968 937.74
298.15 0.5007 951.4
298.15 0.5967 965.4
298.15 0.7000 981.94
298.15 0.7989 999.66
298.15 0.8993 1020.06
298.15 0.9493 1031.4
298.15 1.0000 1043.65
303.15 0.0000 888.3
303.15 0.0697 895.2
303.15 0.0988 898.44
303.15 0.1960 908.59
303.15 0.2944 919.49
303.15 0.3968 931.77
303.15 0.5007 945.46
303.15 0.5967 959.5
303.15 0.7000 976.09
303.15 0.7989 993.85
303.15 0.8993 1014.32
303.15 0.9493 1025.69
303.15 1.0000 1038.0

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Acetic acid (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 900.52
293.15 0.0697 907.35
293.15 0.0988 910.56
293.15 0.1960 920.61
293.15 0.2944 931.46
293.15 0.3968 943.68
293.15 0.5007 957.31
293.15 0.5967 971.28
293.15 0.7000 987.79
293.15 0.7989 1005.47
293.15 0.8993 1025.8
293.15 0.9493 1037.09
293.15 1.0000 1049.3
298.15 0.0000 894.43
298.15 0.0697 901.3
298.15 0.0988 904.53
298.15 0.1960 914.62
298.15 0.2944 925.5
298.15 0.3968 937.74
298.15 0.5007 951.4
298.15 0.5967 965.4
298.15 0.7000 981.94
298.15 0.7989 999.66
298.15 0.8993 1020.06
298.15 0.9493 1031.4
298.15 1.0000 1043.65
303.15 0.0000 888.3
303.15 0.0697 895.2
303.15 0.0988 898.44
303.15 0.1960 908.59
303.15 0.2944 919.49
303.15 0.3968 931.77
303.15 0.5007 945.46
303.15 0.5967 959.5
303.15 0.7000 976.09
303.15 0.7989 993.85
303.15 0.8993 1014.32
303.15 0.9493 1025.69
303.15 1.0000 1038.0

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Acetic acid (1) - Liquid Speed of sound, m/s - Liquid
293.15 0.0000 1163.0
293.15 0.0697 1165.0
293.15 0.0988 1166.0
293.15 0.1960 1166.0
293.15 0.2944 1165.0
293.15 0.3968 1165.0
293.15 0.5007 1163.0
293.15 0.5967 1162.0
293.15 0.7000 1159.0
293.15 0.7989 1157.0
293.15 0.8993 1153.0
293.15 0.9493 1152.0
293.15 1.0000 1149.0
298.15 0.0000 1140.0
298.15 0.0697 1143.0
298.15 0.0988 1144.0
298.15 0.1960 1144.0
298.15 0.2944 1144.0
298.15 0.3968 1143.0
298.15 0.5007 1142.0
298.15 0.5967 1141.0
298.15 0.7000 1140.0
298.15 0.7989 1137.0
298.15 0.8993 1135.0
298.15 0.9493 1134.0
298.15 1.0000 1132.0
303.15 0.0000 1118.0
303.15 0.0697 1121.0
303.15 0.0988 1122.0
303.15 0.1960 1123.0
303.15 0.2944 1123.0
303.15 0.3968 1123.0
303.15 0.5007 1122.0
303.15 0.5967 1121.0
303.15 0.7000 1120.0
303.15 0.7989 1119.0
303.15 0.8993 1117.0
303.15 0.9493 1116.0
303.15 1.0000 1115.0

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Acetic acid (1) - Liquid Speed of sound, m/s - Liquid
293.15 0.0000 1163.0
293.15 0.0697 1165.0
293.15 0.0988 1166.0
293.15 0.1960 1166.0
293.15 0.2944 1165.0
293.15 0.3968 1165.0
293.15 0.5007 1163.0
293.15 0.5967 1162.0
293.15 0.7000 1159.0
293.15 0.7989 1157.0
293.15 0.8993 1153.0
293.15 0.9493 1152.0
293.15 1.0000 1149.0
298.15 0.0000 1140.0
298.15 0.0697 1143.0
298.15 0.0988 1144.0
298.15 0.1960 1144.0
298.15 0.2944 1144.0
298.15 0.3968 1143.0
298.15 0.5007 1142.0
298.15 0.5967 1141.0
298.15 0.7000 1140.0
298.15 0.7989 1137.0
298.15 0.8993 1135.0
298.15 0.9493 1134.0
298.15 1.0000 1132.0
303.15 0.0000 1118.0
303.15 0.0697 1121.0
303.15 0.0988 1122.0
303.15 0.1960 1123.0
303.15 0.2944 1123.0
303.15 0.3968 1123.0
303.15 0.5007 1122.0
303.15 0.5967 1121.0
303.15 0.7000 1120.0
303.15 0.7989 1119.0
303.15 0.8993 1117.0
303.15 0.9493 1116.0
303.15 1.0000 1115.0

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0238 388.86
0.0366 387.91
0.0476 386.97
0.0776 385.03
0.0907 384.03
0.1170 382.21
0.1410 380.57
0.1657 379.12
0.2203 376.35
0.2661 373.77
0.3085 371.67
0.3924 367.87
0.4617 365.00
0.4924 364.00
0.5332 362.65
0.5559 361.91
0.6068 360.21
0.6568 358.94
0.6986 357.82
0.7426 356.57
0.7974 355.20
0.8415 354.21
0.8644 353.55
0.9197 352.20
0.9482 351.45
0.9809 350.61

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 77.3 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.1030 375.25
0.2220 368.85
0.3770 360.75
0.5460 352.95
0.7090 347.75

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 77.3 (Gas)

Mole fraction of Ethyl Acetate (2) - Gas Boiling temperature at pressure P, K - Liquid
0.2790 375.25
0.4520 368.85
0.6830 360.75
0.8290 352.95
0.9010 347.75

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0238 388.86
0.0366 387.91
0.0476 386.97
0.0776 385.03
0.0907 384.03
0.1170 382.21
0.1410 380.57
0.1657 379.12
0.2203 376.35
0.2661 373.77
0.3085 371.67
0.3924 367.87
0.4617 365.00
0.4924 364.00
0.5332 362.65
0.5559 361.91
0.6068 360.21
0.6568 358.94
0.6986 357.82
0.7426 356.57
0.7974 355.20
0.8415 354.21
0.8644 353.55
0.9197 352.20
0.9482 351.45
0.9809 350.61

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 77.3 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.1030 375.25
0.2220 368.85
0.3770 360.75
0.5460 352.95
0.7090 347.75

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 77.3 (Gas)

Mole fraction of Ethyl Acetate (2) - Gas Boiling temperature at pressure P, K - Liquid
0.2790 375.25
0.4520 368.85
0.6830 360.75
0.8290 352.95
0.9010 347.75

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Ethyl Acetate (2) - Liquid y1[mol/mol] of Ethyl Acetate (2) - Vapour
381.25 0.1380 0.3270
378.25 0.1820 0.4220
372.85 0.2860 0.5890
366.75 0.4200 0.7320
361.45 0.5610 0.8540
352.65 0.8720 0.9780

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 333.11 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Ethyl Acetate (2) - Liquid y1[mol/mol] of Ethyl Acetate (2) - Vapour
17.025 0.1098 0.3055
23.585 0.2425 0.5516
29.998 0.3725 0.7158
31.064 0.3930 0.7332
31.197 0.3986 0.7379
35.33 0.4939 0.8160
44.596 0.7311 0.9390
53.382 0.9033 0.9785
53.489 0.9410 0.9892

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 315.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Ethyl Acetate (2) - Liquid y1[mol/mol] of Ethyl Acetate (2) - Vapour
5.133 0.0000 0.0000
9.133 0.1632 0.4725
12.772 0.3168 0.6892
18.932 0.5796 0.8934
21.865 0.7312 0.9488
25.078 0.9033 0.9787
25.878 0.9295 0.9866

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 323.15 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid Vapor or sublimation pressure, kPa - Gas
0.0000 7.61
0.0012 7.65
0.0022 7.69
0.0035 7.73
0.0057 7.80
0.0082 7.88
0.0125 8.03
0.0184 8.23
0.0272 8.52
0.0384 8.90
0.0526 9.38
0.0699 9.97
0.0904 10.67
0.1163 11.56
0.1455 12.55
0.1781 13.66
0.2133 14.85
0.2505 16.10
0.2895 17.39
0.3287 18.65
0.3298 18.70
0.3677 19.89
0.3702 20.00
0.4104 21.21
0.4109 21.28
0.4572 22.64
0.5073 24.13
0.5601 25.66
0.6150 27.21
0.6710 28.76
0.7260 30.25
0.7793 31.67
0.8243 32.87
0.8647 33.96
0.8993 34.88
0.9275 35.67
0.9502 36.31
0.9654 36.76
0.9760 37.08
0.9842 37.33
0.9897 37.50
0.9952 37.68
0.9976 37.76
1.0000 37.85

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 323.15 (Liquid)

Mole fraction of Ethyl Acetate (2) - Liquid Vapor or sublimation pressure, kPa - Gas
0.0000 7.61
0.0012 7.65
0.0022 7.69
0.0035 7.73
0.0057 7.80
0.0082 7.88
0.0125 8.03
0.0184 8.23
0.0272 8.52
0.0384 8.90
0.0526 9.38
0.0699 9.97
0.0904 10.67
0.1163 11.56
0.1455 12.55
0.1781 13.66
0.2133 14.85
0.2505 16.10
0.2895 17.39
0.3287 18.65
0.3298 18.70
0.3677 19.89
0.3702 20.00
0.4104 21.21
0.4109 21.28
0.4572 22.64
0.5073 24.13
0.5601 25.66
0.6150 27.21
0.6710 28.76
0.7260 30.25
0.7793 31.67
0.8243 32.87
0.8647 33.96
0.8993 34.88
0.9275 35.67
0.9502 36.31
0.9654 36.76
0.9760 37.08
0.9842 37.33
0.9897 37.50
0.9952 37.68
0.9976 37.76
1.0000 37.85

Sources