Mixture of Isopropyl Alcohol + 1-Butanol, 3-methyl-, acetate

Excel

Isopropyl Alcohol

Name
Isopropyl Alcohol
InChI
InChI=1S/C3H8O/c1-3(2)4/h3-4H,1-2H3
InChI Key
KFZMGEQAYNKOFK-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CC(C)O
Mol. Weight (g/mol)
60.09
CAS
67-63-0

1-Butanol, 3-methyl-, acetate

Name
1-Butanol, 3-methyl-, acetate
InChI
InChI=1S/C7H14O2/c1-6(2)4-5-9-7(3)8/h6H,4-5H2,1-3H3
InChI Key
MLFHJEHSLIIPHL-UHFFFAOYSA-N
Formula
C7H14O2
SMILES
CC(=O)OCCC(C)C
Mol. Weight (g/mol)
130.18
CAS
123-92-2
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Datasets

  1. ρl - Mass density, kg/m3 (2)
  2. Excess molar volume, m3/mol (2)

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Butanol, 3-methyl-, acetate (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0803 796.71
293.15 0.1602 806.95
293.15 0.2414 816.24
293.15 0.3152 823.84
293.15 0.4006 831.81
293.15 0.4934 839.65
293.15 0.5668 845.36
293.15 0.6524 851.53
293.15 0.7273 856.58
293.15 0.7771 859.71
293.15 0.8718 865.49
293.15 0.9413 869.53
303.15 0.0803 787.87
303.15 0.1602 797.82
303.15 0.2414 806.9
303.15 0.3152 814.34
303.15 0.4006 822.18
303.15 0.4934 829.92
303.15 0.5668 835.58
303.15 0.6524 841.7
303.15 0.7273 846.74
303.15 0.7771 849.86
303.15 0.8718 855.68
303.15 0.9413 859.73
313.15 0.0803 778.75
313.15 0.1602 788.43
313.15 0.2414 797.34
313.15 0.3152 804.63
313.15 0.4006 812.37
313.15 0.4934 820.06
313.15 0.5668 825.66
313.15 0.6524 831.76
313.15 0.7273 836.8
313.15 0.7771 839.93
313.15 0.8718 845.77
313.15 0.9413 849.86
323.15 0.0803 769.3
323.15 0.1602 778.76
323.15 0.2414 787.51
323.15 0.3152 794.7
323.15 0.4006 802.35
323.15 0.4934 810.0
323.15 0.5668 815.57
323.15 0.6524 821.68
323.15 0.7273 826.74
323.15 0.7771 829.88
323.15 0.8718 835.77
323.15 0.9413 839.91
333.15 0.0803 759.45
333.15 0.1602 768.74
333.15 0.2414 777.37
333.15 0.3152 784.5
333.15 0.4006 792.1
333.15 0.4934 799.73
333.15 0.5668 805.31
333.15 0.6524 811.43
333.15 0.7273 816.52
333.15 0.7771 819.71
333.15 0.8718 825.67
333.15 0.9413 829.86

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Butanol, 3-methyl-, acetate (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0803 796.71
293.15 0.1602 806.95
293.15 0.2414 816.24
293.15 0.3152 823.84
293.15 0.4006 831.81
293.15 0.4934 839.65
293.15 0.5668 845.36
293.15 0.6524 851.53
293.15 0.7273 856.58
293.15 0.7771 859.71
293.15 0.8718 865.49
293.15 0.9413 869.53
303.15 0.0803 787.87
303.15 0.1602 797.82
303.15 0.2414 806.9
303.15 0.3152 814.34
303.15 0.4006 822.18
303.15 0.4934 829.92
303.15 0.5668 835.58
303.15 0.6524 841.7
303.15 0.7273 846.74
303.15 0.7771 849.86
303.15 0.8718 855.68
303.15 0.9413 859.73
313.15 0.0803 778.75
313.15 0.1602 788.43
313.15 0.2414 797.34
313.15 0.3152 804.63
313.15 0.4006 812.37
313.15 0.4934 820.06
313.15 0.5668 825.66
313.15 0.6524 831.76
313.15 0.7273 836.8
313.15 0.7771 839.93
313.15 0.8718 845.77
313.15 0.9413 849.86
323.15 0.0803 769.3
323.15 0.1602 778.76
323.15 0.2414 787.51
323.15 0.3152 794.7
323.15 0.4006 802.35
323.15 0.4934 810.0
323.15 0.5668 815.57
323.15 0.6524 821.68
323.15 0.7273 826.74
323.15 0.7771 829.88
323.15 0.8718 835.77
323.15 0.9413 839.91
333.15 0.0803 759.45
333.15 0.1602 768.74
333.15 0.2414 777.37
333.15 0.3152 784.5
333.15 0.4006 792.1
333.15 0.4934 799.73
333.15 0.5668 805.31
333.15 0.6524 811.43
333.15 0.7273 816.52
333.15 0.7771 819.71
333.15 0.8718 825.67
333.15 0.9413 829.86

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Butanol, 3-methyl-, acetate (2) - Liquid Excess molar volume, m3/mol - Liquid
293.15 0.0803 1.2500e-07
293.15 0.1602 2.1700e-07
293.15 0.2414 2.8900e-07
293.15 0.3152 3.3900e-07
293.15 0.4006 3.7900e-07
293.15 0.4934 3.9900e-07
293.15 0.5668 3.9400e-07
293.15 0.6524 3.6900e-07
293.15 0.7273 3.2800e-07
293.15 0.7771 3.0000e-07
293.15 0.8718 2.0400e-07
293.15 0.9413 1.1000e-07
303.15 0.0803 1.4700e-07
303.15 0.1602 2.5700e-07
303.15 0.2414 3.4000e-07
303.15 0.3152 3.9900e-07
303.15 0.4006 4.4300e-07
303.15 0.4934 4.6400e-07
303.15 0.5668 4.5600e-07
303.15 0.6524 4.2800e-07
303.15 0.7273 3.7800e-07
303.15 0.7771 3.4500e-07
303.15 0.8718 2.2900e-07
303.15 0.9413 1.2300e-07
313.15 0.0803 1.7000e-07
313.15 0.1602 2.9900e-07
313.15 0.2414 3.9200e-07
313.15 0.3152 4.6200e-07
313.15 0.4006 5.1100e-07
313.15 0.4934 5.2900e-07
313.15 0.5668 5.2200e-07
313.15 0.6524 4.8800e-07
313.15 0.7273 4.2900e-07
313.15 0.7771 3.9000e-07
313.15 0.8718 2.5900e-07
313.15 0.9413 1.3700e-07
323.15 0.0803 1.9300e-07
323.15 0.1602 3.4100e-07
323.15 0.2414 4.4700e-07
323.15 0.3152 5.2500e-07
323.15 0.4006 5.8000e-07
323.15 0.4934 5.9800e-07
323.15 0.5668 5.9100e-07
323.15 0.6524 5.4900e-07
323.15 0.7273 4.8100e-07
323.15 0.7771 4.3600e-07
323.15 0.8718 2.8800e-07
323.15 0.9413 1.4900e-07
333.15 0.0803 2.1500e-07
333.15 0.1602 3.8300e-07
333.15 0.2414 5.0300e-07
333.15 0.3152 5.8800e-07
333.15 0.4006 6.5000e-07
333.15 0.4934 6.6900e-07
333.15 0.5668 6.5900e-07
333.15 0.6524 6.1400e-07
333.15 0.7273 5.3800e-07
333.15 0.7771 4.8300e-07
333.15 0.8718 3.1600e-07
333.15 0.9413 1.6400e-07

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Butanol, 3-methyl-, acetate (2) - Liquid Excess molar volume, m3/mol - Liquid
293.15 0.0803 1.2500e-07
293.15 0.1602 2.1700e-07
293.15 0.2414 2.8900e-07
293.15 0.3152 3.3900e-07
293.15 0.4006 3.7900e-07
293.15 0.4934 3.9900e-07
293.15 0.5668 3.9400e-07
293.15 0.6524 3.6900e-07
293.15 0.7273 3.2800e-07
293.15 0.7771 3.0000e-07
293.15 0.8718 2.0400e-07
293.15 0.9413 1.1000e-07
303.15 0.0803 1.4700e-07
303.15 0.1602 2.5700e-07
303.15 0.2414 3.4000e-07
303.15 0.3152 3.9900e-07
303.15 0.4006 4.4300e-07
303.15 0.4934 4.6400e-07
303.15 0.5668 4.5600e-07
303.15 0.6524 4.2800e-07
303.15 0.7273 3.7800e-07
303.15 0.7771 3.4500e-07
303.15 0.8718 2.2900e-07
303.15 0.9413 1.2300e-07
313.15 0.0803 1.7000e-07
313.15 0.1602 2.9900e-07
313.15 0.2414 3.9200e-07
313.15 0.3152 4.6200e-07
313.15 0.4006 5.1100e-07
313.15 0.4934 5.2900e-07
313.15 0.5668 5.2200e-07
313.15 0.6524 4.8800e-07
313.15 0.7273 4.2900e-07
313.15 0.7771 3.9000e-07
313.15 0.8718 2.5900e-07
313.15 0.9413 1.3700e-07
323.15 0.0803 1.9300e-07
323.15 0.1602 3.4100e-07
323.15 0.2414 4.4700e-07
323.15 0.3152 5.2500e-07
323.15 0.4006 5.8000e-07
323.15 0.4934 5.9800e-07
323.15 0.5668 5.9100e-07
323.15 0.6524 5.4900e-07
323.15 0.7273 4.8100e-07
323.15 0.7771 4.3600e-07
323.15 0.8718 2.8800e-07
323.15 0.9413 1.4900e-07
333.15 0.0803 2.1500e-07
333.15 0.1602 3.8300e-07
333.15 0.2414 5.0300e-07
333.15 0.3152 5.8800e-07
333.15 0.4006 6.5000e-07
333.15 0.4934 6.6900e-07
333.15 0.5668 6.5900e-07
333.15 0.6524 6.1400e-07
333.15 0.7273 5.3800e-07
333.15 0.7771 4.8300e-07
333.15 0.8718 3.1600e-07
333.15 0.9413 1.6400e-07

Sources