Mixture of Benzene + Ethanol, 2-butoxy-

Excel

Benzene

Name
Benzene
InChI
InChI=1S/C6H6/c1-2-4-6-5-3-1/h1-6H
InChI Key
UHOVQNZJYSORNB-UHFFFAOYSA-N
Formula
C6H6
SMILES
c1ccccc1
Mol. Weight (g/mol)
78.11
CAS
71-43-2

Ethanol, 2-butoxy-

Name
Ethanol, 2-butoxy-
InChI
InChI=1S/C6H14O2/c1-2-3-5-8-6-4-7/h7H,2-6H2,1H3
InChI Key
POAOYUHQDCAZBD-UHFFFAOYSA-N
Formula
C6H14O2
SMILES
CCCCOCCO
Mol. Weight (g/mol)
118.17
CAS
111-76-2
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

  1. η - Viscosity, Pa*s (2)
  2. Excess molar enthalpy (molar enthalpy (2)
  3. ρl - Mass density, kg/m3 (2)
  4. csound,fluid - Speed of Sound, m/s (2)
  5. Tfus - Solid-liquid equilibrium temperature, K (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-butoxy- (2) - Liquid Viscosity, Pa*s - Liquid
298.15 0.0553 0.0006
298.15 0.1496 0.0007
298.15 0.2488 0.0008
298.15 0.3504 0.0010
298.15 0.4555 0.0011
298.15 0.4995 0.0012
298.15 0.5504 0.0013
298.15 0.6482 0.0015
298.15 0.7535 0.0018
298.15 0.8483 0.0021
298.15 0.9556 0.0026
308.15 0.0553 0.0006
308.15 0.1496 0.0006
308.15 0.2488 0.0007
308.15 0.3504 0.0008
308.15 0.4555 0.0009
308.15 0.4995 0.0010
308.15 0.5504 0.0011
308.15 0.6482 0.0013
308.15 0.7535 0.0015
308.15 0.8483 0.0017
308.15 0.9556 0.0020

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-butoxy- (2) - Liquid Viscosity, Pa*s - Liquid
298.15 0.0553 0.0006
298.15 0.1496 0.0007
298.15 0.2488 0.0008
298.15 0.3504 0.0010
298.15 0.4555 0.0011
298.15 0.4995 0.0012
298.15 0.5504 0.0013
298.15 0.6482 0.0015
298.15 0.7535 0.0018
298.15 0.8483 0.0021
298.15 0.9556 0.0026
308.15 0.0553 0.0006
308.15 0.1496 0.0006
308.15 0.2488 0.0007
308.15 0.3504 0.0008
308.15 0.4555 0.0009
308.15 0.4995 0.0010
308.15 0.5504 0.0011
308.15 0.6482 0.0013
308.15 0.7535 0.0015
308.15 0.8483 0.0017
308.15 0.9556 0.0020

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

Operational conditions:

Mole fraction of Benzene (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0343 0.2560
0.0698 0.4198
0.1064 0.5278
0.1444 0.6084
0.1836 0.6522
0.2243 0.6769
0.2665 0.6895
0.3103 0.6820
0.3557 0.6662
0.4029 0.6392
0.4520 0.6017
0.5030 0.5563
0.5562 0.4993
0.6116 0.4409
0.6694 0.3726
0.7297 0.3037
0.7927 0.2275
0.8586 0.1504
0.9277 0.0731

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

Operational conditions:

Mole fraction of Benzene (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0343 0.2560
0.0698 0.4198
0.1064 0.5278
0.1444 0.6084
0.1836 0.6522
0.2243 0.6769
0.2665 0.6895
0.3103 0.6820
0.3557 0.6662
0.4029 0.6392
0.4520 0.6017
0.5030 0.5563
0.5562 0.4993
0.6116 0.4409
0.6694 0.3726
0.7297 0.3037
0.7927 0.2275
0.8586 0.1504
0.9277 0.0731

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-butoxy- (2) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0553 874.3
298.15 0.1496 876.28
298.15 0.2488 879.0
298.15 0.3504 882.07
298.15 0.4555 885.22
298.15 0.4995 886.47
298.15 0.5504 887.85
298.15 0.6482 890.26
298.15 0.7535 892.46
298.15 0.8483 894.11
298.15 0.9556 895.67
303.15 0.0553 869.03
303.15 0.1496 871.1
303.15 0.2488 873.93
303.15 0.3504 877.1
303.15 0.4555 880.36
303.15 0.4995 881.67
303.15 0.5504 883.11
303.15 0.6482 885.63
303.15 0.7535 887.96
303.15 0.8483 889.72
303.15 0.9556 891.4
308.15 0.0553 863.89
308.15 0.1496 866.19
308.15 0.2488 869.18
308.15 0.3504 872.51
308.15 0.4555 875.95
308.15 0.4995 877.34
308.15 0.5504 878.89
308.15 0.6482 881.65
308.15 0.7535 884.26
308.15 0.8483 886.27
308.15 0.9556 888.2
313.15 0.0553 858.82
313.15 0.1496 860.98
313.15 0.2488 863.87
313.15 0.3504 867.12
313.15 0.4555 870.52
313.15 0.4995 871.9
313.15 0.5504 873.44
313.15 0.6482 876.19
313.15 0.7535 878.79
313.15 0.8483 880.8
313.15 0.9556 882.71

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-butoxy- (2) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0553 874.3
298.15 0.1496 876.28
298.15 0.2488 879.0
298.15 0.3504 882.07
298.15 0.4555 885.22
298.15 0.4995 886.47
298.15 0.5504 887.85
298.15 0.6482 890.26
298.15 0.7535 892.46
298.15 0.8483 894.11
298.15 0.9556 895.67
303.15 0.0553 869.03
303.15 0.1496 871.1
303.15 0.2488 873.93
303.15 0.3504 877.1
303.15 0.4555 880.36
303.15 0.4995 881.67
303.15 0.5504 883.11
303.15 0.6482 885.63
303.15 0.7535 887.96
303.15 0.8483 889.72
303.15 0.9556 891.4
308.15 0.0553 863.89
308.15 0.1496 866.19
308.15 0.2488 869.18
308.15 0.3504 872.51
308.15 0.4555 875.95
308.15 0.4995 877.34
308.15 0.5504 878.89
308.15 0.6482 881.65
308.15 0.7535 884.26
308.15 0.8483 886.27
308.15 0.9556 888.2
313.15 0.0553 858.82
313.15 0.1496 860.98
313.15 0.2488 863.87
313.15 0.3504 867.12
313.15 0.4555 870.52
313.15 0.4995 871.9
313.15 0.5504 873.44
313.15 0.6482 876.19
313.15 0.7535 878.79
313.15 0.8483 880.8
313.15 0.9556 882.71

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-butoxy- (2) - Liquid Speed of sound, m/s - Liquid
298.15 0.0553 1291.0
298.15 0.1496 1283.0
298.15 0.2488 1281.0
298.15 0.3504 1282.0
298.15 0.4555 1286.0
298.15 0.4995 1288.0
298.15 0.5504 1291.0
298.15 0.6482 1295.0
298.15 0.7535 1299.0
298.15 0.8483 1302.0
298.15 0.9556 1304.0
308.15 0.0553 1255.0
308.15 0.1496 1250.0
308.15 0.2488 1249.0
308.15 0.3504 1250.0
308.15 0.4555 1254.0
308.15 0.4995 1256.0
308.15 0.5504 1258.0
308.15 0.6482 1262.0
308.15 0.7535 1268.0
308.15 0.8483 1273.0
308.15 0.9556 1281.0

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol, 2-butoxy- (2) - Liquid Speed of sound, m/s - Liquid
298.15 0.0553 1291.0
298.15 0.1496 1283.0
298.15 0.2488 1281.0
298.15 0.3504 1282.0
298.15 0.4555 1286.0
298.15 0.4995 1288.0
298.15 0.5504 1291.0
298.15 0.6482 1295.0
298.15 0.7535 1299.0
298.15 0.8483 1302.0
298.15 0.9556 1304.0
308.15 0.0553 1255.0
308.15 0.1496 1250.0
308.15 0.2488 1249.0
308.15 0.3504 1250.0
308.15 0.4555 1254.0
308.15 0.4995 1256.0
308.15 0.5504 1258.0
308.15 0.6482 1262.0
308.15 0.7535 1268.0
308.15 0.8483 1273.0
308.15 0.9556 1281.0

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of Ethanol, 2-butoxy- (2) - Liquid Solid-liquid equilibrium temperature, K - Liquid
0.0000 278.95
0.0504 276.85
0.1007 275.22
0.1496 273.50
0.2010 271.60
0.2508 269.84
0.2991 267.93
0.3509 265.51
0.4007 262.36
0.4499 259.60
0.4994 255.88
0.5504 251.55
0.6003 246.49
0.6486 242.02
0.6996 235.59
0.7501 228.12
0.8001 220.43

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of Ethanol, 2-butoxy- (2) - Liquid Solid-liquid equilibrium temperature, K - Liquid
0.0000 278.95
0.0504 276.85
0.1007 275.22
0.1496 273.50
0.2010 271.60
0.2508 269.84
0.2991 267.93
0.3509 265.51
0.4007 262.36
0.4499 259.60
0.4994 255.88
0.5504 251.55
0.6003 246.49
0.6486 242.02
0.6996 235.59
0.7501 228.12
0.8001 220.43

Sources