Mixture of Diisopropyl ether + Acetonitrile

Excel

Diisopropyl ether

Name
Diisopropyl ether
InChI
InChI=1S/C6H14O/c1-5(2)7-6(3)4/h5-6H,1-4H3
InChI Key
ZAFNJMIOTHYJRJ-UHFFFAOYSA-N
Formula
C6H14O
SMILES
CC(C)OC(C)C
Mol. Weight (g/mol)
102.17
CAS
108-20-3

Acetonitrile

Name
Acetonitrile
InChI
InChI=1S/C2H3N/c1-2-3/h1H3
InChI Key
WEVYAHXRMPXWCK-UHFFFAOYSA-N
Formula
C2H3N
SMILES
CC#N
Mol. Weight (g/mol)
41.05
CAS
75-05-8
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Datasets

  1. ρl - Mass density, kg/m3 (2)

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diisopropyl ether (1) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0072 786.61
288.15 0.0150 785.8
288.15 0.0247 784.84
288.15 0.0308 784.29
288.15 0.0381 783.55
288.15 0.0482 782.56
288.15 0.0991 777.78
288.15 0.1496 773.32
288.15 0.2511 765.5
288.15 0.3069 761.73
288.15 0.3507 758.83
288.15 0.4104 755.28
288.15 0.4513 752.87
288.15 0.5132 749.57
288.15 0.5600 747.13
288.15 0.6429 743.32
288.15 0.6938 741.1
288.15 0.7600 738.32
288.15 0.8129 736.2
288.15 0.8449 735.0
288.15 0.9040 732.62
288.15 0.9509 730.9
288.15 0.9630 730.42
288.15 0.9685 730.2
288.15 0.9815 729.68
288.15 0.9887 729.4
288.15 0.9945 729.15
293.15 0.0072 781.29
293.15 0.0150 780.49
293.15 0.0247 779.54
293.15 0.0308 778.97
293.15 0.0381 778.25
293.15 0.0482 777.27
293.15 0.0991 772.47
293.15 0.1496 768.06
293.15 0.2511 760.24
293.15 0.3069 756.5
293.15 0.3507 753.58
293.15 0.4104 750.02
293.15 0.4513 747.67
293.15 0.5132 744.35
293.15 0.5600 741.91
293.15 0.6429 738.15
293.15 0.6938 735.9
293.15 0.7600 733.12
293.15 0.8129 731.02
293.15 0.8449 729.8
293.15 0.9040 727.46
293.15 0.9509 725.75
293.15 0.9630 725.28
293.15 0.9685 725.06
293.15 0.9815 724.52
293.15 0.9887 724.27
293.15 0.9945 724.02
298.15 0.0072 775.9
298.15 0.0150 775.1
298.15 0.0247 774.15
298.15 0.0308 773.59
298.15 0.0381 772.87
298.15 0.0482 771.89
298.15 0.0991 767.11
298.15 0.1496 762.72
298.15 0.2511 754.91
298.15 0.3069 751.18
298.15 0.3507 748.27
298.15 0.4104 744.74
298.15 0.4513 742.35
298.15 0.5132 739.06
298.15 0.5600 736.63
298.15 0.6429 732.87
298.15 0.6938 730.64
298.15 0.7600 727.83
298.15 0.8129 725.76
298.15 0.8449 724.53
298.15 0.9040 722.22
298.15 0.9509 720.52
298.15 0.9630 720.05
298.15 0.9685 719.83
298.15 0.9815 719.32
298.15 0.9887 719.05
298.15 0.9945 718.81
303.15 0.0072 770.47
303.15 0.0150 769.68
303.15 0.0247 768.74
303.15 0.0308 768.17
303.15 0.0381 767.46
303.15 0.0482 766.48
303.15 0.0991 761.72
303.15 0.1496 757.34
303.15 0.2511 749.55
303.15 0.3069 745.83
303.15 0.3507 742.93
303.15 0.4104 739.4
303.15 0.4513 737.04
303.15 0.5132 733.73
303.15 0.5600 731.3
303.15 0.6429 727.55
303.15 0.6938 725.33
303.15 0.7600 722.53
303.15 0.8129 720.46
303.15 0.8449 719.26
303.15 0.9040 716.94
303.15 0.9509 715.25
303.15 0.9630 714.78
303.15 0.9685 714.56
303.15 0.9815 714.06
303.15 0.9887 713.79
303.15 0.9945 713.55

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diisopropyl ether (1) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0072 786.61
288.15 0.0150 785.8
288.15 0.0247 784.84
288.15 0.0308 784.29
288.15 0.0381 783.55
288.15 0.0482 782.56
288.15 0.0991 777.78
288.15 0.1496 773.32
288.15 0.2511 765.5
288.15 0.3069 761.73
288.15 0.3507 758.83
288.15 0.4104 755.28
288.15 0.4513 752.87
288.15 0.5132 749.57
288.15 0.5600 747.13
288.15 0.6429 743.32
288.15 0.6938 741.1
288.15 0.7600 738.32
288.15 0.8129 736.2
288.15 0.8449 735.0
288.15 0.9040 732.62
288.15 0.9509 730.9
288.15 0.9630 730.42
288.15 0.9685 730.2
288.15 0.9815 729.68
288.15 0.9887 729.4
288.15 0.9945 729.15
293.15 0.0072 781.29
293.15 0.0150 780.49
293.15 0.0247 779.54
293.15 0.0308 778.97
293.15 0.0381 778.25
293.15 0.0482 777.27
293.15 0.0991 772.47
293.15 0.1496 768.06
293.15 0.2511 760.24
293.15 0.3069 756.5
293.15 0.3507 753.58
293.15 0.4104 750.02
293.15 0.4513 747.67
293.15 0.5132 744.35
293.15 0.5600 741.91
293.15 0.6429 738.15
293.15 0.6938 735.9
293.15 0.7600 733.12
293.15 0.8129 731.02
293.15 0.8449 729.8
293.15 0.9040 727.46
293.15 0.9509 725.75
293.15 0.9630 725.28
293.15 0.9685 725.06
293.15 0.9815 724.52
293.15 0.9887 724.27
293.15 0.9945 724.02
298.15 0.0072 775.9
298.15 0.0150 775.1
298.15 0.0247 774.15
298.15 0.0308 773.59
298.15 0.0381 772.87
298.15 0.0482 771.89
298.15 0.0991 767.11
298.15 0.1496 762.72
298.15 0.2511 754.91
298.15 0.3069 751.18
298.15 0.3507 748.27
298.15 0.4104 744.74
298.15 0.4513 742.35
298.15 0.5132 739.06
298.15 0.5600 736.63
298.15 0.6429 732.87
298.15 0.6938 730.64
298.15 0.7600 727.83
298.15 0.8129 725.76
298.15 0.8449 724.53
298.15 0.9040 722.22
298.15 0.9509 720.52
298.15 0.9630 720.05
298.15 0.9685 719.83
298.15 0.9815 719.32
298.15 0.9887 719.05
298.15 0.9945 718.81
303.15 0.0072 770.47
303.15 0.0150 769.68
303.15 0.0247 768.74
303.15 0.0308 768.17
303.15 0.0381 767.46
303.15 0.0482 766.48
303.15 0.0991 761.72
303.15 0.1496 757.34
303.15 0.2511 749.55
303.15 0.3069 745.83
303.15 0.3507 742.93
303.15 0.4104 739.4
303.15 0.4513 737.04
303.15 0.5132 733.73
303.15 0.5600 731.3
303.15 0.6429 727.55
303.15 0.6938 725.33
303.15 0.7600 722.53
303.15 0.8129 720.46
303.15 0.8449 719.26
303.15 0.9040 716.94
303.15 0.9509 715.25
303.15 0.9630 714.78
303.15 0.9685 714.56
303.15 0.9815 714.06
303.15 0.9887 713.79
303.15 0.9945 713.55

Sources