Mixture of Toluene + n-Butyl ether + Methyl methacrylate

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

n-Butyl ether

Name
n-Butyl ether
InChI
InChI=1S/C8H18O/c1-3-5-7-9-8-6-4-2/h3-8H2,1-2H3
InChI Key
DURPTKYDGMDSBL-UHFFFAOYSA-N
Formula
C8H18O
SMILES
CCCCOCCCC
Mol. Weight (g/mol)
130.23
CAS
142-96-1

Methyl methacrylate

Name
Methyl methacrylate
InChI
InChI=1S/C5H8O2/c1-4(2)5(6)7-3/h1H2,2-3H3
InChI Key
VVQNEPGJFQJSBK-UHFFFAOYSA-N
Formula
C5H8O2
SMILES
C=C(C)C(=O)OC
Mol. Weight (g/mol)
100.12
CAS
80-62-6
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Datasets

  1. ρl - Mass density, kg/m3 (2)
  2. csound,fluid - Speed of Sound, m/s (2)

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Mole fraction of Methyl methacrylate (3) - Liquid Mole fraction of n-Butyl ether (2) - Liquid Temperature, K - Liquid Mass density, kg/m3 - Liquid
0.0457 0.1020 298.15 850.79
0.0457 0.1020 303.15 846.18
0.0457 0.1020 308.15 841.56
0.0457 0.1020 313.15 836.93
0.0985 0.8524 298.15 777.96
0.0985 0.8524 303.15 773.58
0.0985 0.8524 308.15 769.2
0.0985 0.8524 313.15 764.77
0.1027 0.6427 298.15 795.04
0.1027 0.6427 303.15 790.59
0.1027 0.6427 308.15 786.14
0.1027 0.6427 313.15 781.65
0.1425 0.2458 298.15 838.51
0.1425 0.2458 303.15 833.93
0.1425 0.2458 308.15 829.32
0.1425 0.2458 313.15 824.7
0.1457 0.7495 298.15 787.89
0.1457 0.7495 303.15 783.48
0.1457 0.7495 308.15 779.02
0.1457 0.7495 313.15 774.51
0.1954 0.0972 298.15 862.35
0.1954 0.0972 303.15 857.69
0.1954 0.0972 308.15 852.99
0.1954 0.0972 313.15 848.3
0.2357 0.5771 298.15 807.3
0.2357 0.5771 303.15 802.79
0.2357 0.5771 308.15 798.19
0.2357 0.5771 313.15 793.53
0.3463 0.4458 298.15 826.67
0.3463 0.4458 303.15 822.02
0.3463 0.4458 308.15 817.22
0.3463 0.4458 313.15 812.42
0.3779 0.0516 298.15 882.87
0.3779 0.0516 303.15 878.97
0.3779 0.0516 308.15 873.0
0.3779 0.0516 313.15 868.13
0.4365 0.1405 298.15 872.58
0.4365 0.1405 303.15 867.63
0.4365 0.1405 308.15 862.59
0.4365 0.1405 313.15 857.66
0.5255 0.3257 298.15 851.76
0.5255 0.3257 303.15 846.75
0.5255 0.3257 308.15 841.61
0.5255 0.3257 313.15 836.63
0.6428 0.0995 298.15 893.46
0.6428 0.0995 303.15 888.07
0.6428 0.0995 308.15 882.64
0.6428 0.0995 313.15 877.49
0.7521 0.1514 298.15 892.66
0.7521 0.1514 303.15 887.02
0.7521 0.1514 308.15 881.43
0.7521 0.1514 313.15 876.22
0.8287 0.0978 298.15 907.2
0.8287 0.0978 303.15 901.39
0.8287 0.0978 308.15 895.66
0.8287 0.0978 313.15 890.37

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Mole fraction of Methyl methacrylate (3) - Liquid Mole fraction of n-Butyl ether (2) - Liquid Temperature, K - Liquid Mass density, kg/m3 - Liquid
0.0457 0.1020 298.15 850.79
0.0457 0.1020 303.15 846.18
0.0457 0.1020 308.15 841.56
0.0457 0.1020 313.15 836.93
0.0985 0.8524 298.15 777.96
0.0985 0.8524 303.15 773.58
0.0985 0.8524 308.15 769.2
0.0985 0.8524 313.15 764.77
0.1027 0.6427 298.15 795.04
0.1027 0.6427 303.15 790.59
0.1027 0.6427 308.15 786.14
0.1027 0.6427 313.15 781.65
0.1425 0.2458 298.15 838.51
0.1425 0.2458 303.15 833.93
0.1425 0.2458 308.15 829.32
0.1425 0.2458 313.15 824.7
0.1457 0.7495 298.15 787.89
0.1457 0.7495 303.15 783.48
0.1457 0.7495 308.15 779.02
0.1457 0.7495 313.15 774.51
0.1954 0.0972 298.15 862.35
0.1954 0.0972 303.15 857.69
0.1954 0.0972 308.15 852.99
0.1954 0.0972 313.15 848.3
0.2357 0.5771 298.15 807.3
0.2357 0.5771 303.15 802.79
0.2357 0.5771 308.15 798.19
0.2357 0.5771 313.15 793.53
0.3463 0.4458 298.15 826.67
0.3463 0.4458 303.15 822.02
0.3463 0.4458 308.15 817.22
0.3463 0.4458 313.15 812.42
0.3779 0.0516 298.15 882.87
0.3779 0.0516 303.15 878.97
0.3779 0.0516 308.15 873.0
0.3779 0.0516 313.15 868.13
0.4365 0.1405 298.15 872.58
0.4365 0.1405 303.15 867.63
0.4365 0.1405 308.15 862.59
0.4365 0.1405 313.15 857.66
0.5255 0.3257 298.15 851.76
0.5255 0.3257 303.15 846.75
0.5255 0.3257 308.15 841.61
0.5255 0.3257 313.15 836.63
0.6428 0.0995 298.15 893.46
0.6428 0.0995 303.15 888.07
0.6428 0.0995 308.15 882.64
0.6428 0.0995 313.15 877.49
0.7521 0.1514 298.15 892.66
0.7521 0.1514 303.15 887.02
0.7521 0.1514 308.15 881.43
0.7521 0.1514 313.15 876.22
0.8287 0.0978 298.15 907.2
0.8287 0.0978 303.15 901.39
0.8287 0.0978 308.15 895.66
0.8287 0.0978 313.15 890.37

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Mole fraction of Methyl methacrylate (3) - Liquid Mole fraction of n-Butyl ether (2) - Liquid Temperature, K - Liquid Speed of sound, m/s - Liquid
0.0457 0.1020 298.15 1287.9
0.0457 0.1020 308.15 1248.1
0.0985 0.8524 298.15 1219.3
0.0985 0.8524 308.15 1180.4
0.1027 0.6427 298.15 1229.2
0.1027 0.6427 308.15 1190.0
0.1425 0.2458 298.15 1264.5
0.1425 0.2458 308.15 1224.5
0.1457 0.7495 298.15 1219.7
0.1457 0.7495 308.15 1181.7
0.1954 0.0972 298.15 1277.1
0.1954 0.0972 308.15 1238.3
0.2357 0.5771 298.15 1221.3
0.2357 0.5771 308.15 1184.3
0.3463 0.4458 298.15 1221.0
0.3463 0.4458 308.15 1184.7
0.3779 0.0516 298.15 1260.7
0.3779 0.0516 308.15 1224.4
0.4365 0.1405 298.15 1246.4
0.4365 0.1405 308.15 1208.5
0.5255 0.3257 298.15 1211.9
0.5255 0.3257 308.15 1178.6
0.6428 0.0995 298.15 1223.8
0.6428 0.0995 308.15 1189.5
0.7521 0.1514 298.15 1203.0
0.7521 0.1514 308.15 1171.5
0.8287 0.0978 298.15 1197.9
0.8287 0.0978 308.15 1167.4

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Mole fraction of Methyl methacrylate (3) - Liquid Mole fraction of n-Butyl ether (2) - Liquid Temperature, K - Liquid Speed of sound, m/s - Liquid
0.0457 0.1020 298.15 1287.9
0.0457 0.1020 308.15 1248.1
0.0985 0.8524 298.15 1219.3
0.0985 0.8524 308.15 1180.4
0.1027 0.6427 298.15 1229.2
0.1027 0.6427 308.15 1190.0
0.1425 0.2458 298.15 1264.5
0.1425 0.2458 308.15 1224.5
0.1457 0.7495 298.15 1219.7
0.1457 0.7495 308.15 1181.7
0.1954 0.0972 298.15 1277.1
0.1954 0.0972 308.15 1238.3
0.2357 0.5771 298.15 1221.3
0.2357 0.5771 308.15 1184.3
0.3463 0.4458 298.15 1221.0
0.3463 0.4458 308.15 1184.7
0.3779 0.0516 298.15 1260.7
0.3779 0.0516 308.15 1224.4
0.4365 0.1405 298.15 1246.4
0.4365 0.1405 308.15 1208.5
0.5255 0.3257 298.15 1211.9
0.5255 0.3257 308.15 1178.6
0.6428 0.0995 298.15 1223.8
0.6428 0.0995 308.15 1189.5
0.7521 0.1514 298.15 1203.0
0.7521 0.1514 308.15 1171.5
0.8287 0.0978 298.15 1197.9
0.8287 0.0978 308.15 1167.4

Sources