Mixture of 2-Propanol, 2-methyl- + Butane, 2-methoxy-2-methyl-

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2-Propanol, 2-methyl-

Name
2-Propanol, 2-methyl-
InChI
InChI=1S/C4H10O/c1-4(2,3)5/h5H,1-3H3
InChI Key
DKGAVHZHDRPRBM-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CC(C)(C)O
Mol. Weight (g/mol)
74.12
CAS
75-65-0

Butane, 2-methoxy-2-methyl-

Name
Butane, 2-methoxy-2-methyl-
InChI
InChI=1S/C6H14O/c1-5-6(2,3)7-4/h5H2,1-4H3
InChI Key
HVZJRWJGKQPSFL-UHFFFAOYSA-N
Formula
C6H14O
SMILES
CCC(C)(C)OC
Mol. Weight (g/mol)
102.17
CAS
994-05-8
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Datasets

  1. Azeotropic composition: mole fraction (6)
  2. Vapor or sublimation pressure, kPa (2)

Azeotropic composition: mole fraction of Butane, 2-methoxy-2-methyl- (2) [ref]

Temperature, K - Liquid Azeotropic composition: mole fraction of Butane, 2-methoxy-2-methyl- (2) - Liquid
318.13 0.7386
328.20 0.6549
338.28 0.5770

Azeotropic composition: mole fraction of Butane, 2-methoxy-2-methyl- (2) [ref]

Pressure, kPa - Liquid Azeotropic composition: mole fraction of Butane, 2-methoxy-2-methyl- (2) - Liquid
26.20 0.7386
39.98 0.6549
59.52 0.5770

Mole fraction of Butane, 2-methoxy-2-methyl- (2) [ref]

Fixed Measured
Mole fraction of Butane, 2-methoxy-2-methyl- (2) - Liquid Temperature, K - Liquid Mole fraction of Butane, 2-methoxy-2-methyl- (2) - Gas
0.0000 318.13 0.0000
0.0000 328.20 0.0000
0.0000 338.28 0.0000
0.1459 318.13 0.2653
0.1524 328.20 0.2461
0.1586 338.28 0.2269
0.1977 318.13 0.3304
0.1998 328.20 0.3058
0.2089 338.28 0.2833
0.2475 318.13 0.3871
0.2559 328.20 0.3610
0.2642 338.28 0.3397
0.3132 318.13 0.4495
0.3223 328.20 0.4222
0.3300 338.28 0.3984
0.3817 318.13 0.5060
0.3893 328.20 0.4761
0.3970 338.28 0.4501
0.4566 318.13 0.5595
0.4655 328.20 0.5312
0.4735 338.28 0.5062
0.4966 318.13 0.5855
0.5050 328.20 0.5577
0.5126 338.28 0.5330
0.5665 318.13 0.6288
0.5727 328.20 0.6022
0.5788 338.28 0.5781
0.6213 318.13 0.6629
0.6285 328.20 0.6387
0.6350 338.28 0.6168
0.6893 318.13 0.7044
0.6961 328.20 0.6829
0.7018 338.28 0.6639
0.7664 318.13 0.7527
0.7710 328.20 0.7354
0.8548 328.20 0.8042
0.8562 318.13 0.8214
0.8574 338.28 0.7957
0.9458 318.13 0.9161
0.9481 328.20 0.9142
0.9481 338.28 0.9105
0.9812 328.20 0.9670
0.9816 318.13 0.9685
0.9821 338.28 0.9648
1.0000 318.13 1.0000
1.0000 328.20 1.0000
1.0000 338.28 1.0000

Azeotropic composition: mole fraction of Butane, 2-methoxy-2-methyl- (2) [ref]

Temperature, K - Liquid Azeotropic composition: mole fraction of Butane, 2-methoxy-2-methyl- (2) - Liquid
318.13 0.7386
328.20 0.6549
338.28 0.5770

Azeotropic composition: mole fraction of Butane, 2-methoxy-2-methyl- (2) [ref]

Pressure, kPa - Liquid Azeotropic composition: mole fraction of Butane, 2-methoxy-2-methyl- (2) - Liquid
26.20 0.7386
39.98 0.6549
59.52 0.5770

Mole fraction of Butane, 2-methoxy-2-methyl- (2) [ref]

Fixed Measured
Mole fraction of Butane, 2-methoxy-2-methyl- (2) - Liquid Temperature, K - Liquid Mole fraction of Butane, 2-methoxy-2-methyl- (2) - Gas
0.0000 318.13 0.0000
0.0000 328.20 0.0000
0.0000 338.28 0.0000
0.1459 318.13 0.2653
0.1524 328.20 0.2461
0.1586 338.28 0.2269
0.1977 318.13 0.3304
0.1998 328.20 0.3058
0.2089 338.28 0.2833
0.2475 318.13 0.3871
0.2559 328.20 0.3610
0.2642 338.28 0.3397
0.3132 318.13 0.4495
0.3223 328.20 0.4222
0.3300 338.28 0.3984
0.3817 318.13 0.5060
0.3893 328.20 0.4761
0.3970 338.28 0.4501
0.4566 318.13 0.5595
0.4655 328.20 0.5312
0.4735 338.28 0.5062
0.4966 318.13 0.5855
0.5050 328.20 0.5577
0.5126 338.28 0.5330
0.5665 318.13 0.6288
0.5727 328.20 0.6022
0.5788 338.28 0.5781
0.6213 318.13 0.6629
0.6285 328.20 0.6387
0.6350 338.28 0.6168
0.6893 318.13 0.7044
0.6961 328.20 0.6829
0.7018 338.28 0.6639
0.7664 318.13 0.7527
0.7710 328.20 0.7354
0.8548 328.20 0.8042
0.8562 318.13 0.8214
0.8574 338.28 0.7957
0.9458 318.13 0.9161
0.9481 328.20 0.9142
0.9481 338.28 0.9105
0.9812 328.20 0.9670
0.9816 318.13 0.9685
0.9821 338.28 0.9648
1.0000 318.13 1.0000
1.0000 328.20 1.0000
1.0000 338.28 1.0000

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Mole fraction of Butane, 2-methoxy-2-methyl- (2) - Liquid Temperature, K - Liquid Vapor or sublimation pressure, kPa - Gas
0.0000 318.13 17.95
0.0000 328.20 30.35
0.0000 338.28 48.93
0.1459 318.13 21.34
0.1524 328.20 34.66
0.1586 338.28 54.33
0.1977 318.13 22.23
0.1998 328.20 35.68
0.2089 338.28 55.53
0.2475 318.13 23.02
0.2559 328.20 36.74
0.2642 338.28 56.70
0.3132 318.13 23.86
0.3223 328.20 37.74
0.3300 338.28 57.78
0.3817 318.13 24.56
0.3893 328.20 38.52
0.3970 338.28 58.61
0.4566 318.13 25.22
0.4655 328.20 39.28
0.4735 338.28 59.29
0.4966 318.13 25.52
0.5050 328.20 39.52
0.5126 338.28 59.43
0.5665 318.13 25.87
0.5727 328.20 39.78
0.5788 338.28 59.52
0.6213 318.13 26.09
0.6285 328.20 39.95
0.6350 338.28 59.47
0.6893 318.13 26.16
0.6961 328.20 39.94
0.7018 338.28 59.10
0.7664 318.13 26.19
0.7710 328.20 39.60
0.8548 328.20 38.95
0.8562 318.13 25.90
0.8574 338.28 56.82
0.9458 318.13 25.07
0.9481 328.20 37.30
0.9481 338.28 53.85
0.9812 328.20 36.22
0.9816 318.13 24.48
0.9821 338.28 52.11
1.0000 318.13 23.96
1.0000 328.20 35.45
1.0000 338.28 51.05

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Mole fraction of Butane, 2-methoxy-2-methyl- (2) - Liquid Temperature, K - Liquid Vapor or sublimation pressure, kPa - Gas
0.0000 318.13 17.95
0.0000 328.20 30.35
0.0000 338.28 48.93
0.1459 318.13 21.34
0.1524 328.20 34.66
0.1586 338.28 54.33
0.1977 318.13 22.23
0.1998 328.20 35.68
0.2089 338.28 55.53
0.2475 318.13 23.02
0.2559 328.20 36.74
0.2642 338.28 56.70
0.3132 318.13 23.86
0.3223 328.20 37.74
0.3300 338.28 57.78
0.3817 318.13 24.56
0.3893 328.20 38.52
0.3970 338.28 58.61
0.4566 318.13 25.22
0.4655 328.20 39.28
0.4735 338.28 59.29
0.4966 318.13 25.52
0.5050 328.20 39.52
0.5126 338.28 59.43
0.5665 318.13 25.87
0.5727 328.20 39.78
0.5788 338.28 59.52
0.6213 318.13 26.09
0.6285 328.20 39.95
0.6350 338.28 59.47
0.6893 318.13 26.16
0.6961 328.20 39.94
0.7018 338.28 59.10
0.7664 318.13 26.19
0.7710 328.20 39.60
0.8548 328.20 38.95
0.8562 318.13 25.90
0.8574 338.28 56.82
0.9458 318.13 25.07
0.9481 328.20 37.30
0.9481 338.28 53.85
0.9812 328.20 36.22
0.9816 318.13 24.48
0.9821 338.28 52.11
1.0000 318.13 23.96
1.0000 328.20 35.45
1.0000 338.28 51.05

Sources