Mixture of Propane, 2-bromo- + Ethanol

Excel

Propane, 2-bromo-

Name
Propane, 2-bromo-
InChI
InChI=1S/C3H7Br/c1-3(2)4/h3H,1-2H3
InChI Key
NAMYKGVDVNBCFQ-UHFFFAOYSA-N
Formula
C3H7Br
SMILES
CC(C)Br
Mol. Weight (g/mol)
122.99
CAS
75-26-3

Ethanol

Name
Ethanol
InChI
InChI=1S/C2H6O/c1-2-3/h3H,2H2,1H3
InChI Key
LFQSCWFLJHTTHZ-UHFFFAOYSA-N
Formula
C2H6O
SMILES
CCO
Mol. Weight (g/mol)
46.07
CAS
64-17-5
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 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 2-bromo- (1) - Liquid Viscosity, Pa*s - Liquid
298.15 0.0000 0.0011
298.15 0.1000 0.0010
298.15 0.2000 0.0008
298.15 0.3000 0.0007
298.15 0.4000 0.0007
298.15 0.5000 0.0006
298.15 0.6000 0.0005
298.15 0.7000 0.0005
298.15 0.8000 0.0005
298.15 0.9000 0.0005
298.15 1.0000 0.0005
303.15 0.0000 0.0010
303.15 0.1000 0.0009
303.15 0.2000 0.0008
303.15 0.3000 0.0007
303.15 0.4000 0.0006
303.15 0.5000 0.0006
303.15 0.6000 0.0005
303.15 0.7000 0.0005
303.15 0.8000 0.0005
303.15 0.9000 0.0005
303.15 1.0000 0.0005
308.15 0.0000 0.0009
308.15 0.1000 0.0008
308.15 0.2000 0.0007
308.15 0.3000 0.0006
308.15 0.4000 0.0006
308.15 0.5000 0.0005
308.15 0.6000 0.0005
308.15 0.7000 0.0005
308.15 0.8000 0.0004
308.15 0.9000 0.0005
308.15 1.0000 0.0005
313.15 0.0000 0.0009
313.15 0.1000 0.0008
313.15 0.2000 0.0007
313.15 0.3000 0.0006
313.15 0.4000 0.0006
313.15 0.5000 0.0005
313.15 0.6000 0.0005
313.15 0.7000 0.0004
313.15 0.8000 0.0004
313.15 0.9000 0.0004
313.15 1.0000 0.0004
318.15 0.0000 0.0008
318.15 0.1000 0.0007
318.15 0.2000 0.0006
318.15 0.3000 0.0006
318.15 0.4000 0.0005
318.15 0.5000 0.0005
318.15 0.6000 0.0004
318.15 0.7000 0.0004
318.15 0.8000 0.0004
318.15 0.9000 0.0004
318.15 1.0000 0.0004

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 2-bromo- (1) - Liquid Viscosity, Pa*s - Liquid
298.15 0.0000 0.0011
298.15 0.1000 0.0010
298.15 0.2000 0.0008
298.15 0.3000 0.0007
298.15 0.4000 0.0007
298.15 0.5000 0.0006
298.15 0.6000 0.0005
298.15 0.7000 0.0005
298.15 0.8000 0.0005
298.15 0.9000 0.0005
298.15 1.0000 0.0005
303.15 0.0000 0.0010
303.15 0.1000 0.0009
303.15 0.2000 0.0008
303.15 0.3000 0.0007
303.15 0.4000 0.0006
303.15 0.5000 0.0006
303.15 0.6000 0.0005
303.15 0.7000 0.0005
303.15 0.8000 0.0005
303.15 0.9000 0.0005
303.15 1.0000 0.0005
308.15 0.0000 0.0009
308.15 0.1000 0.0008
308.15 0.2000 0.0007
308.15 0.3000 0.0006
308.15 0.4000 0.0006
308.15 0.5000 0.0005
308.15 0.6000 0.0005
308.15 0.7000 0.0005
308.15 0.8000 0.0004
308.15 0.9000 0.0005
308.15 1.0000 0.0005
313.15 0.0000 0.0009
313.15 0.1000 0.0008
313.15 0.2000 0.0007
313.15 0.3000 0.0006
313.15 0.4000 0.0006
313.15 0.5000 0.0005
313.15 0.6000 0.0005
313.15 0.7000 0.0004
313.15 0.8000 0.0004
313.15 0.9000 0.0004
313.15 1.0000 0.0004
318.15 0.0000 0.0008
318.15 0.1000 0.0007
318.15 0.2000 0.0006
318.15 0.3000 0.0006
318.15 0.4000 0.0005
318.15 0.5000 0.0005
318.15 0.6000 0.0004
318.15 0.7000 0.0004
318.15 0.8000 0.0004
318.15 0.9000 0.0004
318.15 1.0000 0.0004

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 2-bromo- (1) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 792.4
298.15 0.1000 868.6
298.15 0.2000 936.3
298.15 0.3000 997.3
298.15 0.4000 1053.1
298.15 0.5000 1104.8
298.15 0.6000 1152.3
298.15 0.7000 1196.1
298.15 0.8000 1236.9
298.15 0.9000 1274.6
298.15 1.0000 1309.9
303.15 0.0000 789.3
303.15 0.1000 864.2
303.15 0.2000 931.2
303.15 0.3000 991.9
303.15 0.4000 1047.6
303.15 0.5000 1098.8
303.15 0.6000 1145.9
303.15 0.7000 1189.6
303.15 0.8000 1230.4
303.15 0.9000 1268.2
303.15 1.0000 1303.6
308.15 0.0000 783.6
308.15 0.1000 857.7
308.15 0.2000 923.6
308.15 0.3000 983.9
308.15 0.4000 1039.0
308.15 0.5000 1089.9
308.15 0.6000 1136.9
308.15 0.7000 1180.3
308.15 0.8000 1220.9
308.15 0.9000 1258.6
308.15 1.0000 1293.9
313.15 0.0000 779.9
313.15 0.1000 853.0
313.15 0.2000 917.8
313.15 0.3000 977.2
313.15 0.4000 1031.8
313.15 0.5000 1082.3
313.15 0.6000 1128.8
313.15 0.7000 1171.9
313.15 0.8000 1212.8
313.15 0.9000 1250.1
313.15 1.0000 1285.4
318.15 0.0000 775.0
318.15 0.1000 846.6
318.15 0.2000 911.1
318.15 0.3000 969.7
318.15 0.4000 1023.6
318.15 0.5000 1073.5
318.15 0.6000 1119.7
318.15 0.7000 1162.7
318.15 0.8000 1202.8
318.15 0.9000 1240.2
318.15 1.0000 1275.4

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 2-bromo- (1) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 792.4
298.15 0.1000 868.6
298.15 0.2000 936.3
298.15 0.3000 997.3
298.15 0.4000 1053.1
298.15 0.5000 1104.8
298.15 0.6000 1152.3
298.15 0.7000 1196.1
298.15 0.8000 1236.9
298.15 0.9000 1274.6
298.15 1.0000 1309.9
303.15 0.0000 789.3
303.15 0.1000 864.2
303.15 0.2000 931.2
303.15 0.3000 991.9
303.15 0.4000 1047.6
303.15 0.5000 1098.8
303.15 0.6000 1145.9
303.15 0.7000 1189.6
303.15 0.8000 1230.4
303.15 0.9000 1268.2
303.15 1.0000 1303.6
308.15 0.0000 783.6
308.15 0.1000 857.7
308.15 0.2000 923.6
308.15 0.3000 983.9
308.15 0.4000 1039.0
308.15 0.5000 1089.9
308.15 0.6000 1136.9
308.15 0.7000 1180.3
308.15 0.8000 1220.9
308.15 0.9000 1258.6
308.15 1.0000 1293.9
313.15 0.0000 779.9
313.15 0.1000 853.0
313.15 0.2000 917.8
313.15 0.3000 977.2
313.15 0.4000 1031.8
313.15 0.5000 1082.3
313.15 0.6000 1128.8
313.15 0.7000 1171.9
313.15 0.8000 1212.8
313.15 0.9000 1250.1
313.15 1.0000 1285.4
318.15 0.0000 775.0
318.15 0.1000 846.6
318.15 0.2000 911.1
318.15 0.3000 969.7
318.15 0.4000 1023.6
318.15 0.5000 1073.5
318.15 0.6000 1119.7
318.15 0.7000 1162.7
318.15 0.8000 1202.8
318.15 0.9000 1240.2
318.15 1.0000 1275.4

Sources