Mixture of Toluene + Decane + Glycerin

Excel

Toluene

Name
Toluene
InChI
InChI=1S/C7H8/c1-7-5-3-2-4-6-7/h2-6H,1H3
InChI Key
YXFVVABEGXRONW-UHFFFAOYSA-N
Formula
C7H8
SMILES
Cc1ccccc1
Mol. Weight (g/mol)
92.14
CAS
108-88-3

Decane

Name
Decane
InChI
InChI=1S/C10H22/c1-3-5-7-9-10-8-6-4-2/h3-10H2,1-2H3
InChI Key
DIOQZVSQGTUSAI-UHFFFAOYSA-N
Formula
C10H22
SMILES
CCCCCCCCCC
Mol. Weight (g/mol)
142.28
CAS
124-18-5

Glycerin

Name
Glycerin
InChI
InChI=1S/C3H8O3/c4-1-3(6)2-5/h3-6H,1-2H2
InChI Key
PEDCQBHIVMGVHV-UHFFFAOYSA-N
Formula
C3H8O3
SMILES
OCC(O)CO
Mol. Weight (g/mol)
92.09
CAS
56-81-5
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Datasets

  1. Mass fraction (4)
  2. ρl - Mass density, kg/m3 (2)

Mass fraction of Toluene (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Fixed Measured
Temperature, K - Liquid mixture 1 Mass fraction of Decane (2) - Liquid mixture 1 Mass fraction of Toluene (1) - Liquid mixture 1
303.15 0.9972 0.0000
303.15 0.8222 0.1713
303.15 0.7332 0.2597
303.15 0.6176 0.3741
303.15 0.4869 0.4948
303.15 0.3678 0.6098
303.15 0.2407 0.7279
303.15 0.1281 0.8548
303.15 0.0039 0.0000
303.15 0.0032 0.1108
303.15 0.0071 0.0455
303.15 0.0050 0.1942
303.15 0.0058 0.2536
303.15 0.0044 0.3744
303.15 0.0000 0.9932
333.15 0.9964 0.0000
333.15 0.9529 0.0357
333.15 0.9032 0.0901
333.15 0.8597 0.1286
333.15 0.8058 0.1886
333.15 0.7472 0.2494
333.15 0.6940 0.2984
333.15 0.6362 0.3454
333.15 0.0028 0.0000
333.15 0.0034 0.0391
333.15 0.0031 0.7191
333.15 0.0047 0.4981
333.15 0.0079 0.8557
333.15 0.0054 0.3984

Temperature, K x Mass fraction [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 1 Mass fraction of Toluene (1) - Liquid mixture 2 Mass fraction of Decane (2) - Liquid mixture 2 Mass fraction of Toluene (1) - Liquid mixture 1 Mass fraction of Decane (2) - Liquid mixture 1
303.15 0.0203 0.0050 0.2553 0.7368
303.15 0.0326 0.0052 0.3292 0.6579
303.15 0.0445 0.0188 0.4126 0.5702
303.15 0.0557 0.0054 0.5199 0.4592
333.15 0.0069 0.0022 0.0277 0.9657
333.15 0.0069 0.0022 0.0681 0.9249
333.15 0.0069 0.0022 0.1266 0.8658
333.15 0.0074 0.0022 0.1920 0.7994
333.15 0.0087 0.0021 0.2612 0.7290
333.15 0.0084 0.0021 0.3689 0.6189

Mass fraction of Toluene (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Fixed Measured
Temperature, K - Liquid mixture 1 Mass fraction of Decane (2) - Liquid mixture 1 Mass fraction of Toluene (1) - Liquid mixture 1
303.15 0.9972 0.0000
303.15 0.8222 0.1713
303.15 0.7332 0.2597
303.15 0.6176 0.3741
303.15 0.4869 0.4948
303.15 0.3678 0.6098
303.15 0.2407 0.7279
303.15 0.1281 0.8548
303.15 0.0039 0.0000
303.15 0.0032 0.1108
303.15 0.0071 0.0455
303.15 0.0050 0.1942
303.15 0.0058 0.2536
303.15 0.0044 0.3744
303.15 0.0000 0.9932
333.15 0.9964 0.0000
333.15 0.9529 0.0357
333.15 0.9032 0.0901
333.15 0.8597 0.1286
333.15 0.8058 0.1886
333.15 0.7472 0.2494
333.15 0.6940 0.2984
333.15 0.6362 0.3454
333.15 0.0028 0.0000
333.15 0.0034 0.0391
333.15 0.0031 0.7191
333.15 0.0047 0.4981
333.15 0.0079 0.8557
333.15 0.0054 0.3984

Temperature, K x Mass fraction [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 1 Mass fraction of Toluene (1) - Liquid mixture 2 Mass fraction of Decane (2) - Liquid mixture 2 Mass fraction of Toluene (1) - Liquid mixture 1 Mass fraction of Decane (2) - Liquid mixture 1
303.15 0.0203 0.0050 0.2553 0.7368
303.15 0.0326 0.0052 0.3292 0.6579
303.15 0.0445 0.0188 0.4126 0.5702
303.15 0.0557 0.0054 0.5199 0.4592
333.15 0.0069 0.0022 0.0277 0.9657
333.15 0.0069 0.0022 0.0681 0.9249
333.15 0.0069 0.0022 0.1266 0.8658
333.15 0.0074 0.0022 0.1920 0.7994
333.15 0.0087 0.0021 0.2612 0.7290
333.15 0.0084 0.0021 0.3689 0.6189

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mass fraction of Decane (2) - Liquid Mass fraction of Toluene (1) - Liquid Mass density, kg/m3 - Liquid
303.15 0.9972 0.0000 726.585
303.15 0.8222 0.1713 741.591
303.15 0.7332 0.2597 752.03
303.15 0.6176 0.3741 766.628
303.15 0.4869 0.4948 782.641
303.15 0.3678 0.6098 799.365
303.15 0.2407 0.7279 817.695
303.15 0.1281 0.8548 835.904
303.15 0.0039 0.0000 1254.174
303.15 0.0032 0.1108 1251.089
303.15 0.0071 0.0455 1242.805
303.15 0.0050 0.1942 1241.536
303.15 0.0058 0.2536 1227.39
303.15 0.0044 0.3744 1155.622
303.15 0.0000 0.9932 857.606
333.15 0.9964 0.0000 700.1
333.15 0.9529 0.0357 703.7
333.15 0.9032 0.0901 708.7
333.15 0.8597 0.1286 712.8
333.15 0.8058 0.1886 719.3
333.15 0.7472 0.2494 725.8
333.15 0.6940 0.2984 731.2
333.15 0.6362 0.3454 737.7
333.15 0.0028 0.0000 1230.46
333.15 0.0034 0.0391 1225.24
333.15 0.0031 0.7191 828.62
333.15 0.0047 0.4981 828.08
333.15 0.0079 0.8557 827.94
333.15 0.0054 0.3984 827.71

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mass fraction of Decane (2) - Liquid Mass fraction of Toluene (1) - Liquid Mass density, kg/m3 - Liquid
303.15 0.9972 0.0000 726.585
303.15 0.8222 0.1713 741.591
303.15 0.7332 0.2597 752.03
303.15 0.6176 0.3741 766.628
303.15 0.4869 0.4948 782.641
303.15 0.3678 0.6098 799.365
303.15 0.2407 0.7279 817.695
303.15 0.1281 0.8548 835.904
303.15 0.0039 0.0000 1254.174
303.15 0.0032 0.1108 1251.089
303.15 0.0071 0.0455 1242.805
303.15 0.0050 0.1942 1241.536
303.15 0.0058 0.2536 1227.39
303.15 0.0044 0.3744 1155.622
303.15 0.0000 0.9932 857.606
333.15 0.9964 0.0000 700.1
333.15 0.9529 0.0357 703.7
333.15 0.9032 0.0901 708.7
333.15 0.8597 0.1286 712.8
333.15 0.8058 0.1886 719.3
333.15 0.7472 0.2494 725.8
333.15 0.6940 0.2984 731.2
333.15 0.6362 0.3454 737.7
333.15 0.0028 0.0000 1230.46
333.15 0.0034 0.0391 1225.24
333.15 0.0031 0.7191 828.62
333.15 0.0047 0.4981 828.08
333.15 0.0079 0.8557 827.94
333.15 0.0054 0.3984 827.71

Sources