Mixture of n-Hexane + 1-Propanol + Propane, 2-methoxy-2-methyl-

Excel

n-Hexane

Name
n-Hexane
InChI
InChI=1S/C6H14/c1-3-5-6-4-2/h3-6H2,1-2H3
InChI Key
VLKZOEOYAKHREP-UHFFFAOYSA-N
Formula
C6H14
SMILES
CCCCCC
Mol. Weight (g/mol)
86.18
CAS
110-54-3

1-Propanol

Name
1-Propanol
InChI
InChI=1S/C3H8O/c1-2-3-4/h4H,2-3H2,1H3
InChI Key
BDERNNFJNOPAEC-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CCCO
Mol. Weight (g/mol)
60.09
CAS
71-23-8

Propane, 2-methoxy-2-methyl-

Name
Propane, 2-methoxy-2-methyl-
InChI
InChI=1S/C5H12O/c1-5(2,3)6-4/h1-4H3
InChI Key
BZLVMXJERCGZMT-UHFFFAOYSA-N
Formula
C5H12O
SMILES
COC(C)(C)C
Mol. Weight (g/mol)
88.15
CAS
1634-04-4
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Datasets

  1. Pvap - Vapor or sublimation pressure, kPa (2)

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Fixed Measured
Mole fraction of Propane, 2-methoxy-2-methyl- (3) - Liquid Mole fraction of 1-Propanol (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 0.0000 37.30
0.0000 0.3016 39.42
0.0000 0.7012 34.77
0.0000 1.0000 7.01
0.0001 0.0000 37.25
0.0001 1.0000 7.00
0.0311 0.2923 40.00
0.0332 0.6778 35.40
0.0497 0.2867 40.35
0.0575 0.6608 35.91
0.1028 0.2706 41.38
0.1075 0.6257 37.03
0.1475 0.5001 39.89
0.1531 0.5936 38.10
0.1535 0.2553 42.38
0.1549 0.3489 41.80
0.1620 0.4508 40.75
0.1696 0.3820 41.72
0.1766 0.4013 41.52
0.1852 0.4173 41.57
0.1915 0.3508 42.25
0.2009 0.4528 41.31
0.2016 0.5596 39.24
0.2046 0.2399 43.39
0.2074 0.2970 42.98
0.2149 0.4845 40.98
0.2213 0.2498 43.59
0.2309 0.5209 40.43
0.2354 0.2019 44.20
0.2467 0.5570 39.64
0.2502 0.1516 44.84
0.2510 0.5248 40.42
0.2523 0.2255 44.33
0.2616 0.5908 38.61
0.2652 0.1004 45.49
0.2777 0.6275 37.03
0.2798 0.0508 46.11
0.2878 0.0235 46.38
0.2905 0.6567 35.31
0.2947 0.0000 46.48
0.2971 0.6717 34.24
0.3034 0.4881 41.69
0.3034 0.2100 45.36
0.3066 0.6934 32.36
0.3459 0.1535 46.61
0.3488 0.4998 41.68
0.3508 0.4548 42.79
0.3816 0.1693 47.09
0.3816 0.4528 43.09
0.4022 0.4188 44.01
0.4027 0.1800 47.36
0.4141 0.1838 47.49
0.4177 0.4010 44.52
0.4406 0.1686 48.13
0.4482 0.1990 47.89
0.4486 0.3862 45.11
0.4524 0.3512 45.83
0.4742 0.1585 48.81
0.4834 0.2147 48.24
0.4874 0.3010 47.09
0.4998 0.3503 46.33
0.5185 0.2303 48.55
0.5197 0.2546 48.23
0.5511 0.2448 48.77
0.5554 0.2034 49.49
0.5857 0.2603 48.95
0.5907 0.1528 50.75
0.6223 0.1074 51.97
0.6227 0.2768 49.04
0.6554 0.2915 49.03
0.6591 0.0546 53.52
0.6719 0.2988 48.98
0.6754 0.0312 54.26
0.6922 0.3078 48.89
0.6971 0.0000 55.28
1.0000 0.0000 59.91
1.0000 0.0000 59.91

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Fixed Measured
Mole fraction of Propane, 2-methoxy-2-methyl- (3) - Liquid Mole fraction of 1-Propanol (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 0.0000 37.30
0.0000 0.3016 39.42
0.0000 0.7012 34.77
0.0000 1.0000 7.01
0.0001 0.0000 37.25
0.0001 1.0000 7.00
0.0311 0.2923 40.00
0.0332 0.6778 35.40
0.0497 0.2867 40.35
0.0575 0.6608 35.91
0.1028 0.2706 41.38
0.1075 0.6257 37.03
0.1475 0.5001 39.89
0.1531 0.5936 38.10
0.1535 0.2553 42.38
0.1549 0.3489 41.80
0.1620 0.4508 40.75
0.1696 0.3820 41.72
0.1766 0.4013 41.52
0.1852 0.4173 41.57
0.1915 0.3508 42.25
0.2009 0.4528 41.31
0.2016 0.5596 39.24
0.2046 0.2399 43.39
0.2074 0.2970 42.98
0.2149 0.4845 40.98
0.2213 0.2498 43.59
0.2309 0.5209 40.43
0.2354 0.2019 44.20
0.2467 0.5570 39.64
0.2502 0.1516 44.84
0.2510 0.5248 40.42
0.2523 0.2255 44.33
0.2616 0.5908 38.61
0.2652 0.1004 45.49
0.2777 0.6275 37.03
0.2798 0.0508 46.11
0.2878 0.0235 46.38
0.2905 0.6567 35.31
0.2947 0.0000 46.48
0.2971 0.6717 34.24
0.3034 0.4881 41.69
0.3034 0.2100 45.36
0.3066 0.6934 32.36
0.3459 0.1535 46.61
0.3488 0.4998 41.68
0.3508 0.4548 42.79
0.3816 0.1693 47.09
0.3816 0.4528 43.09
0.4022 0.4188 44.01
0.4027 0.1800 47.36
0.4141 0.1838 47.49
0.4177 0.4010 44.52
0.4406 0.1686 48.13
0.4482 0.1990 47.89
0.4486 0.3862 45.11
0.4524 0.3512 45.83
0.4742 0.1585 48.81
0.4834 0.2147 48.24
0.4874 0.3010 47.09
0.4998 0.3503 46.33
0.5185 0.2303 48.55
0.5197 0.2546 48.23
0.5511 0.2448 48.77
0.5554 0.2034 49.49
0.5857 0.2603 48.95
0.5907 0.1528 50.75
0.6223 0.1074 51.97
0.6227 0.2768 49.04
0.6554 0.2915 49.03
0.6591 0.0546 53.52
0.6719 0.2988 48.98
0.6754 0.0312 54.26
0.6922 0.3078 48.89
0.6971 0.0000 55.28
1.0000 0.0000 59.91
1.0000 0.0000 59.91

Sources