Mixture of Diisopropyl ether + o-Xylene

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

o-Xylene

Name
o-Xylene
InChI
InChI=1S/C8H10/c1-7-5-3-4-6-8(7)2/h3-6H,1-2H3
InChI Key
CTQNGGLPUBDAKN-UHFFFAOYSA-N
Formula
C8H10
SMILES
Cc1ccccc1C
Mol. Weight (g/mol)
106.17
CAS
95-47-6
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Datasets

  1. γ - Surface tension liquid-gas, N/m (2)
  2. Excess molar volume, m3/mol (2)

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 298.15 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid Surface tension liquid-gas, N/m - Liquid
0.1022 0.0272
0.2010 0.0255
0.3018 0.0242
0.4037 0.0230
0.4997 0.0220
0.5998 0.0210
0.7013 0.0200
0.7987 0.0192
0.8987 0.0181

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 298.15 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid Surface tension liquid-gas, N/m - Liquid
0.1022 0.0272
0.2010 0.0255
0.3018 0.0242
0.4037 0.0230
0.4997 0.0220
0.5998 0.0210
0.7013 0.0200
0.7987 0.0192
0.8987 0.0181

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (1) - Liquid Excess molar volume, m3/mol - Liquid
0.0506 -1.7700e-07
0.0997 -3.1500e-07
0.1501 -4.4900e-07
0.2003 -5.7400e-07
0.2503 -6.9100e-07
0.3003 -7.8200e-07
0.3500 -8.3900e-07
0.4004 -8.8300e-07
0.4497 -9.2200e-07
0.5050 -9.3600e-07
0.5505 -9.4800e-07
0.6001 -9.1000e-07
0.6509 -8.8200e-07
0.7000 -8.1100e-07
0.7502 -7.4700e-07
0.7999 -6.3100e-07
0.8502 -5.1100e-07
0.8997 -3.6900e-07
0.9493 -2.1000e-07

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (1) - Liquid Excess molar volume, m3/mol - Liquid
0.0506 -1.7700e-07
0.0997 -3.1500e-07
0.1501 -4.4900e-07
0.2003 -5.7400e-07
0.2503 -6.9100e-07
0.3003 -7.8200e-07
0.3500 -8.3900e-07
0.4004 -8.8300e-07
0.4497 -9.2200e-07
0.5050 -9.3600e-07
0.5505 -9.4800e-07
0.6001 -9.1000e-07
0.6509 -8.8200e-07
0.7000 -8.1100e-07
0.7502 -7.4700e-07
0.7999 -6.3100e-07
0.8502 -5.1100e-07
0.8997 -3.6900e-07
0.9493 -2.1000e-07

Sources