Mixture of 1-Tert-butoxybutane + Methyl Alcohol

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1-Tert-butoxybutane

Name
1-Tert-butoxybutane
InChI
InChI=1S/C8H18O/c1-5-6-7-9-8(2,3)4/h5-7H2,1-4H3
InChI Key
JJNQHLLBFBGKEL-UHFFFAOYSA-N
Formula
C8H18O
SMILES
CCCCOC(C)(C)C
Mol. Weight (g/mol)
130.23
CAS
1000-63-1

Methyl Alcohol

Name
Methyl Alcohol
InChI
InChI=1S/CH4O/c1-2/h2H,1H3
InChI Key
OKKJLVBELUTLKV-UHFFFAOYSA-N
Formula
CH4O
SMILES
CO
Mol. Weight (g/mol)
32.04
CAS
67-56-1
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Datasets

  1. Mole fraction (2)
  2. n0 - Refractive index (Na D-line) (2)
  3. ρl - Mass density, kg/m3 (2)
  4. csound,fluid - Speed of Sound, m/s (2)
  5. Tboil - Boiling temperature at pressure P, K (2)

Mole fraction of Methyl Alcohol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Methyl Alcohol (2) - Liquid Mole fraction of Methyl Alcohol (2) - Gas
0.0096 0.1751
0.0291 0.4577
0.0479 0.5887
0.0832 0.6940
0.1519 0.7749
0.2116 0.8141
0.2904 0.8421
0.3449 0.8545
0.3805 0.8609
0.4168 0.8666
0.4807 0.8751
0.5198 0.8798
0.5587 0.8842
0.5834 0.8870
0.6542 0.8949
0.6982 0.9001
0.7344 0.9047
0.7693 0.9096
0.8035 0.9150
0.8284 0.9195
0.8739 0.9295
0.9101 0.9401
0.9372 0.9510
0.9485 0.9566
0.9569 0.9614
0.9640 0.9660
0.9704 0.9705
0.9829 0.9810
0.9909 0.9891

Mole fraction of Methyl Alcohol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Methyl Alcohol (2) - Liquid Mole fraction of Methyl Alcohol (2) - Gas
0.0096 0.1751
0.0291 0.4577
0.0479 0.5887
0.0832 0.6940
0.1519 0.7749
0.2116 0.8141
0.2904 0.8421
0.3449 0.8545
0.3805 0.8609
0.4168 0.8666
0.4807 0.8751
0.5198 0.8798
0.5587 0.8842
0.5834 0.8870
0.6542 0.8949
0.6982 0.9001
0.7344 0.9047
0.7693 0.9096
0.8035 0.9150
0.8284 0.9195
0.8739 0.9295
0.9101 0.9401
0.9372 0.9510
0.9485 0.9566
0.9569 0.9614
0.9640 0.9660
0.9704 0.9705
0.9829 0.9810
0.9909 0.9891

Refractive index (Na D-line) [ref]

Operational conditions:

Mole fraction of 1-Tert-butoxybutane (1) - Liquid Refractive index (Na D-line) - Liquid
0.0406 1.3367
0.0518 1.3392
0.0974 1.3477
0.0984 1.3479
0.1493 1.3555
0.1980 1.3613
0.2051 1.362
0.2448 1.3658
0.2974 1.37
0.3373 1.3728
0.3581 1.3741
0.3783 1.3753
0.3922 1.376
0.4633 1.3795
0.4954 1.3809
0.5003 1.3811
0.5598 1.3833
0.5955 1.3845
0.6138 1.385
0.6463 1.3859
0.6737 1.3866
0.6923 1.3871
0.7210 1.3877
0.7904 1.3891
0.7934 1.3892
0.8479 1.3901
0.8631 1.3903
0.8964 1.3907
0.9255 1.3911

Refractive index (Na D-line) [ref]

Operational conditions:

Mole fraction of 1-Tert-butoxybutane (1) - Liquid Refractive index (Na D-line) - Liquid
0.0406 1.3367
0.0518 1.3392
0.0974 1.3477
0.0984 1.3479
0.1493 1.3555
0.1980 1.3613
0.2051 1.362
0.2448 1.3658
0.2974 1.37
0.3373 1.3728
0.3581 1.3741
0.3783 1.3753
0.3922 1.376
0.4633 1.3795
0.4954 1.3809
0.5003 1.3811
0.5598 1.3833
0.5955 1.3845
0.6138 1.385
0.6463 1.3859
0.6737 1.3866
0.6923 1.3871
0.7210 1.3877
0.7904 1.3891
0.7934 1.3892
0.8479 1.3901
0.8631 1.3903
0.8964 1.3907
0.9255 1.3911

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of 1-Tert-butoxybutane (1) - Liquid Mass density, kg/m3 - Liquid
0.0406 783.42
0.0518 782.76
0.0974 780.08
0.0984 779.91
0.1493 777.55
0.1980 775.42
0.2051 775.26
0.2448 773.83
0.2974 772.2
0.3373 770.98
0.3581 770.41
0.3783 769.88
0.3922 769.7
0.4633 767.85
0.4954 767.15
0.5003 767.05
0.5598 765.86
0.5955 765.21
0.6138 764.85
0.6463 764.27
0.6737 763.79
0.6923 763.48
0.7210 762.99
0.7904 761.8
0.7934 761.75
0.8479 760.78
0.8631 760.5
0.8964 759.86
0.9255 759.26

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of 1-Tert-butoxybutane (1) - Liquid Mass density, kg/m3 - Liquid
0.0406 783.42
0.0518 782.76
0.0974 780.08
0.0984 779.91
0.1493 777.55
0.1980 775.42
0.2051 775.26
0.2448 773.83
0.2974 772.2
0.3373 770.98
0.3581 770.41
0.3783 769.88
0.3922 769.7
0.4633 767.85
0.4954 767.15
0.5003 767.05
0.5598 765.86
0.5955 765.21
0.6138 764.85
0.6463 764.27
0.6737 763.79
0.6923 763.48
0.7210 762.99
0.7904 761.8
0.7934 761.75
0.8479 760.78
0.8631 760.5
0.8964 759.86
0.9255 759.26

Speed of sound, m/s [ref]

Operational conditions:

Mole fraction of 1-Tert-butoxybutane (1) - Liquid Speed of sound, m/s - Liquid
0.0406 1103.0
0.0518 1104.0
0.0974 1103.0
0.0984 1104.0
0.1493 1105.0
0.1980 1107.0
0.2051 1107.0
0.2448 1108.0
0.2974 1109.0
0.3373 1109.0
0.3581 1109.0
0.3783 1109.0
0.3922 1111.0
0.4633 1111.0
0.4954 1113.0
0.5003 1111.0
0.5598 1112.0
0.5955 1114.0
0.6138 1113.0
0.6463 1113.0
0.6737 1114.0
0.6923 1114.0
0.7210 1114.0
0.7904 1114.0
0.7934 1114.0
0.8479 1114.0
0.8631 1114.0
0.8964 1115.0
0.9255 1114.0

Speed of sound, m/s [ref]

Operational conditions:

Mole fraction of 1-Tert-butoxybutane (1) - Liquid Speed of sound, m/s - Liquid
0.0406 1103.0
0.0518 1104.0
0.0974 1103.0
0.0984 1104.0
0.1493 1105.0
0.1980 1107.0
0.2051 1107.0
0.2448 1108.0
0.2974 1109.0
0.3373 1109.0
0.3581 1109.0
0.3783 1109.0
0.3922 1111.0
0.4633 1111.0
0.4954 1113.0
0.5003 1111.0
0.5598 1112.0
0.5955 1114.0
0.6138 1113.0
0.6463 1113.0
0.6737 1114.0
0.6923 1114.0
0.7210 1114.0
0.7904 1114.0
0.7934 1114.0
0.8479 1114.0
0.8631 1114.0
0.8964 1115.0
0.9255 1114.0

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Methyl Alcohol (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0096 388.87
0.0291 377.92
0.0479 371.36
0.0832 362.06
0.1519 352.75
0.2116 347.64
0.2904 344.54
0.3449 343.17
0.3805 342.47
0.4168 341.88
0.4807 341.03
0.5198 340.60
0.5587 340.22
0.5834 340.00
0.6542 339.42
0.6982 339.09
0.7344 338.84
0.7693 338.61
0.8035 338.39
0.8284 338.23
0.8739 337.97
0.9101 337.78
0.9372 337.67
0.9485 337.63
0.9569 337.61
0.9640 337.60
0.9704 337.60
0.9829 337.61
0.9909 337.64

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Methyl Alcohol (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0096 388.87
0.0291 377.92
0.0479 371.36
0.0832 362.06
0.1519 352.75
0.2116 347.64
0.2904 344.54
0.3449 343.17
0.3805 342.47
0.4168 341.88
0.4807 341.03
0.5198 340.60
0.5587 340.22
0.5834 340.00
0.6542 339.42
0.6982 339.09
0.7344 338.84
0.7693 338.61
0.8035 338.39
0.8284 338.23
0.8739 337.97
0.9101 337.78
0.9372 337.67
0.9485 337.63
0.9569 337.61
0.9640 337.60
0.9704 337.60
0.9829 337.61
0.9909 337.64

Sources