Mixture of 1-Butanol + 1-Propanol, 2-methyl-

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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

1-Propanol, 2-methyl-

Name
1-Propanol, 2-methyl-
InChI
InChI=1S/C4H10O/c1-4(2)3-5/h4-5H,3H2,1-2H3
InChI Key
ZXEKIIBDNHEJCQ-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CC(C)CO
Mol. Weight (g/mol)
74.12
CAS
78-83-1
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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
303.15 0.1010 0.0034
303.15 0.2029 0.0034
303.15 0.3008 0.0034
303.15 0.4000 0.0033
303.15 0.5000 0.0032
303.15 0.5999 0.0032
303.15 0.6999 0.0031
303.15 0.7993 0.0030
303.15 0.8995 0.0030
308.15 0.1010 0.0030
308.15 0.2029 0.0030
308.15 0.3008 0.0029
308.15 0.4000 0.0029
308.15 0.5000 0.0028
308.15 0.5999 0.0028
308.15 0.6999 0.0027
308.15 0.7993 0.0027
308.15 0.8995 0.0026
313.15 0.1010 0.0026
313.15 0.2029 0.0026
313.15 0.3008 0.0026
313.15 0.4000 0.0025
313.15 0.5000 0.0025
313.15 0.5999 0.0024
313.15 0.6999 0.0024
313.15 0.7993 0.0024
313.15 0.8995 0.0023
318.15 0.1010 0.0022
318.15 0.2029 0.0022
318.15 0.3008 0.0022
318.15 0.4000 0.0022
318.15 0.5000 0.0022
318.15 0.5999 0.0021
318.15 0.6999 0.0021
318.15 0.7993 0.0021
318.15 0.8995 0.0021
323.15 0.1010 0.0020
323.15 0.2029 0.0020
323.15 0.3008 0.0020
323.15 0.4000 0.0019
323.15 0.5000 0.0019
323.15 0.5999 0.0019
323.15 0.6999 0.0019
323.15 0.7993 0.0019
323.15 0.8995 0.0018
328.15 0.1010 0.0017
328.15 0.2029 0.0017
328.15 0.3008 0.0017
328.15 0.4000 0.0017
328.15 0.5000 0.0017
328.15 0.5999 0.0017
328.15 0.6999 0.0017
328.15 0.7993 0.0017
328.15 0.8995 0.0017
333.15 0.1010 0.0015
333.15 0.2029 0.0015
333.15 0.3008 0.0015
333.15 0.4000 0.0015
333.15 0.5000 0.0015
333.15 0.5999 0.0015
333.15 0.6999 0.0015
333.15 0.7993 0.0015
333.15 0.8995 0.0015
338.15 0.1010 0.0013
338.15 0.2029 0.0014
338.15 0.3008 0.0014
338.15 0.4000 0.0014
338.15 0.5000 0.0014
338.15 0.5999 0.0013
338.15 0.6999 0.0013
338.15 0.7993 0.0013
338.15 0.8995 0.0013
343.15 0.1010 0.0012
343.15 0.2029 0.0012
343.15 0.3008 0.0012
343.15 0.4000 0.0012
343.15 0.5000 0.0012
343.15 0.5999 0.0012
343.15 0.6999 0.0012
343.15 0.7993 0.0012
343.15 0.8995 0.0012

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
303.15 0.1010 0.0034
303.15 0.2029 0.0034
303.15 0.3008 0.0034
303.15 0.4000 0.0033
303.15 0.5000 0.0032
303.15 0.5999 0.0032
303.15 0.6999 0.0031
303.15 0.7993 0.0030
303.15 0.8995 0.0030
308.15 0.1010 0.0030
308.15 0.2029 0.0030
308.15 0.3008 0.0029
308.15 0.4000 0.0029
308.15 0.5000 0.0028
308.15 0.5999 0.0028
308.15 0.6999 0.0027
308.15 0.7993 0.0027
308.15 0.8995 0.0026
313.15 0.1010 0.0026
313.15 0.2029 0.0026
313.15 0.3008 0.0026
313.15 0.4000 0.0025
313.15 0.5000 0.0025
313.15 0.5999 0.0024
313.15 0.6999 0.0024
313.15 0.7993 0.0024
313.15 0.8995 0.0023
318.15 0.1010 0.0022
318.15 0.2029 0.0022
318.15 0.3008 0.0022
318.15 0.4000 0.0022
318.15 0.5000 0.0022
318.15 0.5999 0.0021
318.15 0.6999 0.0021
318.15 0.7993 0.0021
318.15 0.8995 0.0021
323.15 0.1010 0.0020
323.15 0.2029 0.0020
323.15 0.3008 0.0020
323.15 0.4000 0.0019
323.15 0.5000 0.0019
323.15 0.5999 0.0019
323.15 0.6999 0.0019
323.15 0.7993 0.0019
323.15 0.8995 0.0018
328.15 0.1010 0.0017
328.15 0.2029 0.0017
328.15 0.3008 0.0017
328.15 0.4000 0.0017
328.15 0.5000 0.0017
328.15 0.5999 0.0017
328.15 0.6999 0.0017
328.15 0.7993 0.0017
328.15 0.8995 0.0017
333.15 0.1010 0.0015
333.15 0.2029 0.0015
333.15 0.3008 0.0015
333.15 0.4000 0.0015
333.15 0.5000 0.0015
333.15 0.5999 0.0015
333.15 0.6999 0.0015
333.15 0.7993 0.0015
333.15 0.8995 0.0015
338.15 0.1010 0.0013
338.15 0.2029 0.0014
338.15 0.3008 0.0014
338.15 0.4000 0.0014
338.15 0.5000 0.0014
338.15 0.5999 0.0013
338.15 0.6999 0.0013
338.15 0.7993 0.0013
338.15 0.8995 0.0013
343.15 0.1010 0.0012
343.15 0.2029 0.0012
343.15 0.3008 0.0012
343.15 0.4000 0.0012
343.15 0.5000 0.0012
343.15 0.5999 0.0012
343.15 0.6999 0.0012
343.15 0.7993 0.0012
343.15 0.8995 0.0012

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
303.15 0.1010 794.896
303.15 0.2029 795.74
303.15 0.3008 796.558
303.15 0.4000 797.382
303.15 0.5000 798.209
303.15 0.5999 799.026
303.15 0.6999 799.838
303.15 0.7993 800.635
303.15 0.8995 801.426
308.15 0.1010 790.969
308.15 0.2029 791.819
308.15 0.3008 792.643
308.15 0.4000 793.476
308.15 0.5000 794.307
308.15 0.5999 795.132
308.15 0.6999 795.953
308.15 0.7993 796.757
308.15 0.8995 797.554
313.15 0.1010 786.977
313.15 0.2029 787.84
313.15 0.3008 788.67
313.15 0.4000 789.511
313.15 0.5000 790.349
313.15 0.5999 791.184
313.15 0.6999 792.012
313.15 0.7993 792.829
313.15 0.8995 793.633
318.15 0.1010 782.93
318.15 0.2029 783.806
318.15 0.3008 784.646
318.15 0.4000 785.496
318.15 0.5000 786.344
318.15 0.5999 787.188
318.15 0.6999 788.027
318.15 0.7993 788.855
318.15 0.8995 789.67
323.15 0.1010 778.816
323.15 0.2029 779.704
323.15 0.3008 780.558
323.15 0.4000 781.419
323.15 0.5000 782.279
323.15 0.5999 783.136
323.15 0.6999 783.985
323.15 0.7993 784.825
323.15 0.8995 785.654
328.15 0.1010 774.633
328.15 0.2029 775.537
328.15 0.3008 776.405
328.15 0.4000 777.281
328.15 0.5000 778.156
328.15 0.5999 779.026
328.15 0.6999 779.893
328.15 0.7993 780.744
328.15 0.8995 781.588
333.15 0.1010 770.368
333.15 0.2029 771.292
333.15 0.3008 772.177
333.15 0.4000 773.068
333.15 0.5000 773.961
333.15 0.5999 774.846
333.15 0.6999 775.732
333.15 0.7993 776.596
333.15 0.8995 777.457
338.15 0.1010 766.021
338.15 0.2029 766.966
338.15 0.3008 767.871
338.15 0.4000 768.778
338.15 0.5000 769.689
338.15 0.5999 770.594
338.15 0.6999 771.495
338.15 0.7993 772.378
338.15 0.8995 773.258
343.15 0.1010 761.578
343.15 0.2029 762.548
343.15 0.3008 763.474
343.15 0.4000 764.4
343.15 0.5000 765.333
343.15 0.5999 766.26
343.15 0.6999 767.182
343.15 0.7993 768.085
343.15 0.8995 768.986

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
303.15 0.1010 794.896
303.15 0.2029 795.74
303.15 0.3008 796.558
303.15 0.4000 797.382
303.15 0.5000 798.209
303.15 0.5999 799.026
303.15 0.6999 799.838
303.15 0.7993 800.635
303.15 0.8995 801.426
308.15 0.1010 790.969
308.15 0.2029 791.819
308.15 0.3008 792.643
308.15 0.4000 793.476
308.15 0.5000 794.307
308.15 0.5999 795.132
308.15 0.6999 795.953
308.15 0.7993 796.757
308.15 0.8995 797.554
313.15 0.1010 786.977
313.15 0.2029 787.84
313.15 0.3008 788.67
313.15 0.4000 789.511
313.15 0.5000 790.349
313.15 0.5999 791.184
313.15 0.6999 792.012
313.15 0.7993 792.829
313.15 0.8995 793.633
318.15 0.1010 782.93
318.15 0.2029 783.806
318.15 0.3008 784.646
318.15 0.4000 785.496
318.15 0.5000 786.344
318.15 0.5999 787.188
318.15 0.6999 788.027
318.15 0.7993 788.855
318.15 0.8995 789.67
323.15 0.1010 778.816
323.15 0.2029 779.704
323.15 0.3008 780.558
323.15 0.4000 781.419
323.15 0.5000 782.279
323.15 0.5999 783.136
323.15 0.6999 783.985
323.15 0.7993 784.825
323.15 0.8995 785.654
328.15 0.1010 774.633
328.15 0.2029 775.537
328.15 0.3008 776.405
328.15 0.4000 777.281
328.15 0.5000 778.156
328.15 0.5999 779.026
328.15 0.6999 779.893
328.15 0.7993 780.744
328.15 0.8995 781.588
333.15 0.1010 770.368
333.15 0.2029 771.292
333.15 0.3008 772.177
333.15 0.4000 773.068
333.15 0.5000 773.961
333.15 0.5999 774.846
333.15 0.6999 775.732
333.15 0.7993 776.596
333.15 0.8995 777.457
338.15 0.1010 766.021
338.15 0.2029 766.966
338.15 0.3008 767.871
338.15 0.4000 768.778
338.15 0.5000 769.689
338.15 0.5999 770.594
338.15 0.6999 771.495
338.15 0.7993 772.378
338.15 0.8995 773.258
343.15 0.1010 761.578
343.15 0.2029 762.548
343.15 0.3008 763.474
343.15 0.4000 764.4
343.15 0.5000 765.333
343.15 0.5999 766.26
343.15 0.6999 767.182
343.15 0.7993 768.085
343.15 0.8995 768.986

Sources