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

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-Butanol

Name
1-Butanol
InChI
InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3
InChI Key
LRHPLDYGYMQRHN-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CCCCO
Mol. Weight (g/mol)
74.12
CAS
71-36-3
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. η - Viscosity, Pa*s (2)
  2. ρl - Mass density, kg/m3 (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Butanol (2) - Liquid Viscosity, Pa*s - Liquid
288.15 0.1114 0.0007
288.15 0.2168 0.0008
288.15 0.3241 0.0009
288.15 0.4255 0.0010
288.15 0.5172 0.0012
288.15 0.6158 0.0014
288.15 0.7127 0.0018
288.15 0.7911 0.0021
288.15 0.8968 0.0026
298.15 0.1114 0.0006
298.15 0.2168 0.0007
298.15 0.3241 0.0008
298.15 0.4255 0.0009
298.15 0.5172 0.0010
298.15 0.6158 0.0012
298.15 0.7127 0.0014
298.15 0.7911 0.0016
298.15 0.8968 0.0020
308.15 0.1114 0.0006
308.15 0.2168 0.0006
308.15 0.3241 0.0006
308.15 0.4255 0.0007
308.15 0.5172 0.0008
308.15 0.6158 0.0009
308.15 0.7127 0.0011
308.15 0.7911 0.0013
308.15 0.8968 0.0016
318.15 0.1114 0.0005
318.15 0.2168 0.0005
318.15 0.3241 0.0006
318.15 0.4255 0.0006
318.15 0.5172 0.0007
318.15 0.6158 0.0008
318.15 0.7127 0.0009
318.15 0.7911 0.0010
318.15 0.8968 0.0013

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Butanol (2) - Liquid Viscosity, Pa*s - Liquid
288.15 0.1114 0.0007
288.15 0.2168 0.0008
288.15 0.3241 0.0009
288.15 0.4255 0.0010
288.15 0.5172 0.0012
288.15 0.6158 0.0014
288.15 0.7127 0.0018
288.15 0.7911 0.0021
288.15 0.8968 0.0026
298.15 0.1114 0.0006
298.15 0.2168 0.0007
298.15 0.3241 0.0008
298.15 0.4255 0.0009
298.15 0.5172 0.0010
298.15 0.6158 0.0012
298.15 0.7127 0.0014
298.15 0.7911 0.0016
298.15 0.8968 0.0020
308.15 0.1114 0.0006
308.15 0.2168 0.0006
308.15 0.3241 0.0006
308.15 0.4255 0.0007
308.15 0.5172 0.0008
308.15 0.6158 0.0009
308.15 0.7127 0.0011
308.15 0.7911 0.0013
308.15 0.8968 0.0016
318.15 0.1114 0.0005
318.15 0.2168 0.0005
318.15 0.3241 0.0006
318.15 0.4255 0.0006
318.15 0.5172 0.0007
318.15 0.6158 0.0008
318.15 0.7127 0.0009
318.15 0.7911 0.0010
318.15 0.8968 0.0013

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Butanol (2) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0651 1254.36
288.15 0.0908 1243.72
288.15 0.1711 1210.18
288.15 0.2243 1187.62
288.15 0.3496 1133.18
288.15 0.4142 1104.35
288.15 0.4554 1085.66
288.15 0.5543 1039.78
288.15 0.6421 997.92
288.15 0.7017 968.75
288.15 0.7817 928.75
288.15 0.8097 914.45
288.15 0.8665 885.03
288.15 0.9373 847.42
288.15 0.8665 885.03
308.15 0.1003 1211.63
308.15 0.1981 1171.51
308.15 0.2872 1134.22
308.15 0.3997 1086.06
308.15 0.5004 1041.57
308.15 0.6152 989.22
308.15 0.7005 948.99
308.15 0.7972 901.96
308.15 0.8995 850.58
318.15 0.0985 1197.92
318.15 0.1984 1157.54
318.15 0.2858 1121.53
318.15 0.3937 1075.99
318.15 0.4965 1031.33
318.15 0.5958 986.93
318.15 0.6965 940.53
318.15 0.7954 893.34
318.15 0.8967 843.28
318.15 0.9519 815.23

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Butanol (2) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0651 1254.36
288.15 0.0908 1243.72
288.15 0.1711 1210.18
288.15 0.2243 1187.62
288.15 0.3496 1133.18
288.15 0.4142 1104.35
288.15 0.4554 1085.66
288.15 0.5543 1039.78
288.15 0.6421 997.92
288.15 0.7017 968.75
288.15 0.7817 928.75
288.15 0.8097 914.45
288.15 0.8665 885.03
288.15 0.9373 847.42
288.15 0.8665 885.03
308.15 0.1003 1211.63
308.15 0.1981 1171.51
308.15 0.2872 1134.22
308.15 0.3997 1086.06
308.15 0.5004 1041.57
308.15 0.6152 989.22
308.15 0.7005 948.99
308.15 0.7972 901.96
308.15 0.8995 850.58
318.15 0.0985 1197.92
318.15 0.1984 1157.54
318.15 0.2858 1121.53
318.15 0.3937 1075.99
318.15 0.4965 1031.33
318.15 0.5958 986.93
318.15 0.6965 940.53
318.15 0.7954 893.34
318.15 0.8967 843.28
318.15 0.9519 815.23

Sources