Mixture of Butane, 1-bromo- + 1-Decanol

Excel

Butane, 1-bromo-

Name
Butane, 1-bromo-
InChI
InChI=1S/C4H9Br/c1-2-3-4-5/h2-4H2,1H3
InChI Key
MPPPKRYCTPRNTB-UHFFFAOYSA-N
Formula
C4H9Br
SMILES
CCCCBr
Mol. Weight (g/mol)
137.02
CAS
109-65-9

1-Decanol

Name
1-Decanol
InChI
InChI=1S/C10H22O/c1-2-3-4-5-6-7-8-9-10-11/h11H,2-10H2,1H3
InChI Key
MWKFXSUHUHTGQN-UHFFFAOYSA-N
Formula
C10H22O
SMILES
CCCCCCCCCCO
Mol. Weight (g/mol)
158.28
CAS
112-30-1
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. Pvap - Vapor or sublimation pressure, kPa (2)

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Decanol (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
283.15 0.0997 2.39
283.15 0.1937 2.30
283.15 0.3007 2.17
283.15 0.4342 1.91
283.15 0.4912 1.83
283.15 0.5656 1.70
283.15 0.6516 1.47
283.15 0.7095 1.26
283.15 0.7113 1.23
283.15 0.7801 0.98
283.15 0.7906 0.94
283.15 0.9006 0.51
288.15 0.0998 3.13
288.15 0.1937 3.02
288.15 0.3007 2.84
288.15 0.4343 2.55
288.15 0.4913 2.39
288.15 0.5657 2.17
288.15 0.6517 1.86
288.15 0.7096 1.60
288.15 0.7114 1.59
288.15 0.7802 1.28
288.15 0.7907 1.24
288.15 0.9007 0.64
293.15 0.0998 4.07
293.15 0.1938 3.92
293.15 0.3008 3.68
293.15 0.4344 3.27
293.15 0.4914 3.08
293.15 0.5658 2.80
293.15 0.6518 2.40
293.15 0.7097 2.09
293.15 0.7116 2.08
293.15 0.7803 1.67
293.15 0.7908 1.59
293.15 0.9007 0.82
298.15 0.0998 5.23
298.15 0.1938 5.02
298.15 0.3009 4.71
298.15 0.4345 4.21
298.15 0.4916 3.94
298.15 0.5660 3.56
298.15 0.6519 3.06
298.15 0.7098 2.66
298.15 0.7117 2.65
298.15 0.7805 2.12
298.15 0.7909 2.02
298.15 0.9008 1.03
303.15 0.0998 6.69
303.15 0.1939 6.33
303.15 0.3010 5.99
303.15 0.4347 5.34
303.15 0.4918 4.98
303.15 0.5661 4.50
303.15 0.6521 3.86
303.15 0.7100 3.34
303.15 0.7120 3.35
303.15 0.7806 2.67
303.15 0.7910 2.56
303.15 0.9008 1.32
308.15 0.0999 8.42
308.15 0.1940 8.04
308.15 0.3011 7.52
308.15 0.4350 6.67
308.15 0.4920 6.24
308.15 0.5664 5.63
308.15 0.6524 4.80
308.15 0.7102 4.15
308.15 0.7122 4.16
308.15 0.7809 3.31
308.15 0.7912 3.18
308.15 0.9009 1.64
313.15 0.1000 10.52
313.15 0.1942 10.08
313.15 0.3014 9.34
313.15 0.4354 8.29
313.15 0.4924 7.74
313.15 0.5667 6.97
313.15 0.6527 5.92
313.15 0.7104 5.12
313.15 0.7126 5.14
313.15 0.7812 4.08
313.15 0.7914 3.93
313.15 0.9010 2.03
318.15 0.1000 13.05
318.15 0.1944 12.41
318.15 0.3016 11.53
318.15 0.4358 10.20
318.15 0.4928 9.51
318.15 0.5670 8.57
318.15 0.6531 7.27
318.15 0.7116 6.29
318.15 0.7130 6.29
318.15 0.7816 4.98
318.15 0.7916 4.80
318.15 0.9012 2.50
323.15 0.1002 16.04
323.15 0.1946 15.21
323.15 0.3020 14.10
323.15 0.4364 12.44
323.15 0.4934 11.59
323.15 0.5675 10.42
323.15 0.6536 8.81
323.15 0.7112 7.62
323.15 0.7135 7.61
323.15 0.7820 6.03
323.15 0.7919 5.82
323.15 0.9013 3.04

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Decanol (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
283.15 0.0997 2.39
283.15 0.1937 2.30
283.15 0.3007 2.17
283.15 0.4342 1.91
283.15 0.4912 1.83
283.15 0.5656 1.70
283.15 0.6516 1.47
283.15 0.7095 1.26
283.15 0.7113 1.23
283.15 0.7801 0.98
283.15 0.7906 0.94
283.15 0.9006 0.51
288.15 0.0998 3.13
288.15 0.1937 3.02
288.15 0.3007 2.84
288.15 0.4343 2.55
288.15 0.4913 2.39
288.15 0.5657 2.17
288.15 0.6517 1.86
288.15 0.7096 1.60
288.15 0.7114 1.59
288.15 0.7802 1.28
288.15 0.7907 1.24
288.15 0.9007 0.64
293.15 0.0998 4.07
293.15 0.1938 3.92
293.15 0.3008 3.68
293.15 0.4344 3.27
293.15 0.4914 3.08
293.15 0.5658 2.80
293.15 0.6518 2.40
293.15 0.7097 2.09
293.15 0.7116 2.08
293.15 0.7803 1.67
293.15 0.7908 1.59
293.15 0.9007 0.82
298.15 0.0998 5.23
298.15 0.1938 5.02
298.15 0.3009 4.71
298.15 0.4345 4.21
298.15 0.4916 3.94
298.15 0.5660 3.56
298.15 0.6519 3.06
298.15 0.7098 2.66
298.15 0.7117 2.65
298.15 0.7805 2.12
298.15 0.7909 2.02
298.15 0.9008 1.03
303.15 0.0998 6.69
303.15 0.1939 6.33
303.15 0.3010 5.99
303.15 0.4347 5.34
303.15 0.4918 4.98
303.15 0.5661 4.50
303.15 0.6521 3.86
303.15 0.7100 3.34
303.15 0.7120 3.35
303.15 0.7806 2.67
303.15 0.7910 2.56
303.15 0.9008 1.32
308.15 0.0999 8.42
308.15 0.1940 8.04
308.15 0.3011 7.52
308.15 0.4350 6.67
308.15 0.4920 6.24
308.15 0.5664 5.63
308.15 0.6524 4.80
308.15 0.7102 4.15
308.15 0.7122 4.16
308.15 0.7809 3.31
308.15 0.7912 3.18
308.15 0.9009 1.64
313.15 0.1000 10.52
313.15 0.1942 10.08
313.15 0.3014 9.34
313.15 0.4354 8.29
313.15 0.4924 7.74
313.15 0.5667 6.97
313.15 0.6527 5.92
313.15 0.7104 5.12
313.15 0.7126 5.14
313.15 0.7812 4.08
313.15 0.7914 3.93
313.15 0.9010 2.03
318.15 0.1000 13.05
318.15 0.1944 12.41
318.15 0.3016 11.53
318.15 0.4358 10.20
318.15 0.4928 9.51
318.15 0.5670 8.57
318.15 0.6531 7.27
318.15 0.7116 6.29
318.15 0.7130 6.29
318.15 0.7816 4.98
318.15 0.7916 4.80
318.15 0.9012 2.50
323.15 0.1002 16.04
323.15 0.1946 15.21
323.15 0.3020 14.10
323.15 0.4364 12.44
323.15 0.4934 11.59
323.15 0.5675 10.42
323.15 0.6536 8.81
323.15 0.7112 7.62
323.15 0.7135 7.61
323.15 0.7820 6.03
323.15 0.7919 5.82
323.15 0.9013 3.04

Sources