Mixture of 1-Butanol + 4,7-Methano-1H-indene, octahydro-

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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

4,7-Methano-1H-indene, octahydro-

Name
4,7-Methano-1H-indene, octahydro-
InChI
InChI=1S/C10H16/c1-2-9-7-4-5-8(6-7)10(9)3-1/h7-10H,1-6H2
InChI Key
LPSXSORODABQKT-UHFFFAOYSA-N
Formula
C10H16
SMILES
C1CC2C3CCC(C3)C2C1
Mol. Weight (g/mol)
136.23
CAS
6004-38-2
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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 1-Butanol (1) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0031
293.15 0.1697 0.0028
293.15 0.3148 0.0027
293.15 0.4378 0.0026
293.15 0.5481 0.0027
293.15 0.6472 0.0027
293.15 0.7336 0.0027
293.15 0.8102 0.0028
293.15 0.8799 0.0029
293.15 0.9439 0.0029
293.15 1.0000 0.0029
298.15 0.0000 0.0028
298.15 0.1697 0.0025
298.15 0.3148 0.0024
298.15 0.4378 0.0024
298.15 0.5481 0.0024
298.15 0.6472 0.0024
298.15 0.7336 0.0024
298.15 0.8102 0.0025
298.15 0.8799 0.0025
298.15 0.9439 0.0025
298.15 1.0000 0.0026
303.15 0.0000 0.0025
303.15 0.1697 0.0023
303.15 0.3148 0.0022
303.15 0.4378 0.0021
303.15 0.5481 0.0021
303.15 0.6472 0.0021
303.15 0.7336 0.0022
303.15 0.8102 0.0022
303.15 0.8799 0.0022
303.15 0.9439 0.0023
303.15 1.0000 0.0023
313.15 0.0000 0.0021
313.15 0.1697 0.0019
313.15 0.3148 0.0018
313.15 0.4378 0.0017
313.15 0.5481 0.0017
313.15 0.6472 0.0017
313.15 0.7336 0.0017
313.15 0.8102 0.0017
313.15 0.8799 0.0017
313.15 0.9439 0.0018
313.15 1.0000 0.0018

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Butanol (1) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0031
293.15 0.1697 0.0028
293.15 0.3148 0.0027
293.15 0.4378 0.0026
293.15 0.5481 0.0027
293.15 0.6472 0.0027
293.15 0.7336 0.0027
293.15 0.8102 0.0028
293.15 0.8799 0.0029
293.15 0.9439 0.0029
293.15 1.0000 0.0029
298.15 0.0000 0.0028
298.15 0.1697 0.0025
298.15 0.3148 0.0024
298.15 0.4378 0.0024
298.15 0.5481 0.0024
298.15 0.6472 0.0024
298.15 0.7336 0.0024
298.15 0.8102 0.0025
298.15 0.8799 0.0025
298.15 0.9439 0.0025
298.15 1.0000 0.0026
303.15 0.0000 0.0025
303.15 0.1697 0.0023
303.15 0.3148 0.0022
303.15 0.4378 0.0021
303.15 0.5481 0.0021
303.15 0.6472 0.0021
303.15 0.7336 0.0022
303.15 0.8102 0.0022
303.15 0.8799 0.0022
303.15 0.9439 0.0023
303.15 1.0000 0.0023
313.15 0.0000 0.0021
313.15 0.1697 0.0019
313.15 0.3148 0.0018
313.15 0.4378 0.0017
313.15 0.5481 0.0017
313.15 0.6472 0.0017
313.15 0.7336 0.0017
313.15 0.8102 0.0017
313.15 0.8799 0.0017
313.15 0.9439 0.0018
313.15 1.0000 0.0018

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Butanol (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 935.6
293.15 0.1697 920.1
293.15 0.3148 905.3
293.15 0.4378 891.5
293.15 0.5481 877.9
293.15 0.6472 864.7
293.15 0.7336 852.3
293.15 0.8102 840.7
293.15 0.8799 829.5
293.15 0.9439 819.1
293.15 1.0000 809.1
298.15 0.0000 931.2
298.15 0.1697 916.1
298.15 0.3148 901.4
298.15 0.4378 887.7
298.15 0.5481 874.3
298.15 0.6472 861.2
298.15 0.7336 849.0
298.15 0.8102 837.4
298.15 0.8799 826.4
298.15 0.9439 815.6
298.15 1.0000 805.6
303.15 0.0000 927.6
303.15 0.1697 912.6
303.15 0.3148 898.1
303.15 0.4378 884.5
303.15 0.5481 871.0
303.15 0.6472 857.9
303.15 0.7336 845.7
303.15 0.8102 834.1
303.15 0.8799 823.1
303.15 0.9439 812.3
303.15 1.0000 802.0
313.15 0.0000 919.3
313.15 0.1697 904.5
313.15 0.3148 890.0
313.15 0.4378 876.4
313.15 0.5481 862.9
313.15 0.6472 849.8
313.15 0.7336 837.4
313.15 0.8102 825.8
313.15 0.8799 814.7
313.15 0.9439 803.9
313.15 1.0000 793.4

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Butanol (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 935.6
293.15 0.1697 920.1
293.15 0.3148 905.3
293.15 0.4378 891.5
293.15 0.5481 877.9
293.15 0.6472 864.7
293.15 0.7336 852.3
293.15 0.8102 840.7
293.15 0.8799 829.5
293.15 0.9439 819.1
293.15 1.0000 809.1
298.15 0.0000 931.2
298.15 0.1697 916.1
298.15 0.3148 901.4
298.15 0.4378 887.7
298.15 0.5481 874.3
298.15 0.6472 861.2
298.15 0.7336 849.0
298.15 0.8102 837.4
298.15 0.8799 826.4
298.15 0.9439 815.6
298.15 1.0000 805.6
303.15 0.0000 927.6
303.15 0.1697 912.6
303.15 0.3148 898.1
303.15 0.4378 884.5
303.15 0.5481 871.0
303.15 0.6472 857.9
303.15 0.7336 845.7
303.15 0.8102 834.1
303.15 0.8799 823.1
303.15 0.9439 812.3
303.15 1.0000 802.0
313.15 0.0000 919.3
313.15 0.1697 904.5
313.15 0.3148 890.0
313.15 0.4378 876.4
313.15 0.5481 862.9
313.15 0.6472 849.8
313.15 0.7336 837.4
313.15 0.8102 825.8
313.15 0.8799 814.7
313.15 0.9439 803.9
313.15 1.0000 793.4

Sources