Mixture of 1-(isobutoxy)butane + Acetonitrile

1-(isobutoxy)butane

Name
1-(isobutoxy)butane
InChI
InChI=1S/C8H18O/c1-4-5-6-9-7-8(2)3/h8H,4-7H2,1-3H3
InChI Key
VDHBXQMYKGNZRP-UHFFFAOYSA-N
Formula
C8H18O
SMILES
CCCCOCC(C)C
Mol. Weight (g/mol)
130.23
CAS
17071-47-5

Acetonitrile

Name
Acetonitrile
InChI
InChI=1S/C2H3N/c1-2-3/h1H3
InChI Key
WEVYAHXRMPXWCK-UHFFFAOYSA-N
Formula
C2H3N
SMILES
CC#N
Mol. Weight (g/mol)
41.05
CAS
75-05-8
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Datasets

  1. Excess molar enthalpy (molar enthalpy (2)
  2. Liquid-liquid equilibrium temperature, K (2)

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

Operational conditions:

Mole fraction of Acetonitrile (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0314 0.1901
0.0610 0.3509
0.0887 0.4851
0.1149 0.5997
0.1396 0.6968
0.1851 0.8539
0.2261 0.9755
0.2631 1.0682
0.2967 1.1416
0.3275 1.1967
0.3815 1.2616
0.4274 1.2976
0.4671 1.3192
0.5097 1.3253
0.5459 1.3206
0.5772 1.3005
0.6045 1.2894
0.6329 1.2613
0.6575 1.2346
0.6789 1.2092
0.7009 1.1795
0.7183 1.1524
0.7200 1.1504
0.7368 1.121
0.7392 1.1155
0.7517 1.091
0.7613 1.0699
0.7650 1.0627
0.7847 1.0146
0.8097 0.9474
0.8362 0.8656
0.8530 0.8071
0.8705 0.7403
0.8887 0.6624
0.9077 0.5726
0.9275 0.4689
0.9411 0.3912
0.9552 0.3054
0.9697 0.2105
0.9846 0.1057

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

Operational conditions:

Mole fraction of Acetonitrile (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0314 0.1901
0.0610 0.3509
0.0887 0.4851
0.1149 0.5997
0.1396 0.6968
0.1851 0.8539
0.2261 0.9755
0.2631 1.0682
0.2967 1.1416
0.3275 1.1967
0.3815 1.2616
0.4274 1.2976
0.4671 1.3192
0.5097 1.3253
0.5459 1.3206
0.5772 1.3005
0.6045 1.2894
0.6329 1.2613
0.6575 1.2346
0.6789 1.2092
0.7009 1.1795
0.7183 1.1524
0.7200 1.1504
0.7368 1.121
0.7392 1.1155
0.7517 1.091
0.7613 1.0699
0.7650 1.0627
0.7847 1.0146
0.8097 0.9474
0.8362 0.8656
0.8530 0.8071
0.8705 0.7403
0.8887 0.6624
0.9077 0.5726
0.9275 0.4689
0.9411 0.3912
0.9552 0.3054
0.9697 0.2105
0.9846 0.1057

Liquid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 1)

Mole fraction of Acetonitrile (2) - Liquid mixture 1 Liquid-liquid equilibrium temperature, K - Liquid mixture 1
0.2674 261.60
0.2953 265.44
0.3178 268.18
0.3368 270.26
0.3672 273.21
0.3974 275.68
0.4265 277.72
0.4642 279.82
0.4981 281.24
0.5270 282.43
0.5481 283.37
0.5896 284.14
0.6255 284.49
0.6615 284.62
0.6985 284.68
0.7337 284.61
0.7682 284.13
0.7980 283.10
0.8232 281.34
0.8440 279.29
0.8639 276.36
0.8782 273.52
0.8919 270.26
0.9048 266.23
0.9177 261.46

Liquid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 1)

Mole fraction of Acetonitrile (2) - Liquid mixture 1 Liquid-liquid equilibrium temperature, K - Liquid mixture 1
0.2674 261.60
0.2953 265.44
0.3178 268.18
0.3368 270.26
0.3672 273.21
0.3974 275.68
0.4265 277.72
0.4642 279.82
0.4981 281.24
0.5270 282.43
0.5481 283.37
0.5896 284.14
0.6255 284.49
0.6615 284.62
0.6985 284.68
0.7337 284.61
0.7682 284.13
0.7980 283.10
0.8232 281.34
0.8440 279.29
0.8639 276.36
0.8782 273.52
0.8919 270.26
0.9048 266.23
0.9177 261.46

Sources

Note: These property values are available through the Cheméo API. A free account gives you an access key.