Mixture of Diisopropyl ether + Cyclohexane

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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

Cyclohexane

Name
Cyclohexane
InChI
InChI=1S/C6H12/c1-2-4-6-5-3-1/h1-6H2
InChI Key
XDTMQSROBMDMFD-UHFFFAOYSA-N
Formula
C6H12
SMILES
C1CCCCC1
Mol. Weight (g/mol)
84.16
CAS
110-82-7
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Datasets

  1. Mole fraction (2)
  2. η - Viscosity, Pa*s (2)
  3. csound,fluid - Speed of Sound, m/s (2)
  4. γ - Surface tension liquid-gas, N/m (2)
  5. Tboil - Boiling temperature at pressure P, K (2)
  6. Excess molar volume, m3/mol (2)

Mole fraction of Diisopropyl ether (1) [ref]

Operational condition: Pressure, kPa = 94 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid Mole fraction of Diisopropyl ether (1) - Gas
0.0000 0.0000
0.0650 0.1060
0.1190 0.1820
0.1690 0.2470
0.2230 0.3130
0.2720 0.3690
0.3210 0.4210
0.3700 0.4700
0.4190 0.5180
0.4680 0.5650
0.5180 0.6090
0.5690 0.6530
0.6160 0.6930
0.6660 0.7350
0.7110 0.7710
0.7600 0.8110
0.8130 0.8530
0.8590 0.8890
0.9070 0.9270
0.9590 0.9680
1.0000 1.0000

Mole fraction of Diisopropyl ether (1) [ref]

Operational condition: Pressure, kPa = 94 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid Mole fraction of Diisopropyl ether (1) - Gas
0.0000 0.0000
0.0650 0.1060
0.1190 0.1820
0.1690 0.2470
0.2230 0.3130
0.2720 0.3690
0.3210 0.4210
0.3700 0.4700
0.4190 0.5180
0.4680 0.5650
0.5180 0.6090
0.5690 0.6530
0.6160 0.6930
0.6660 0.7350
0.7110 0.7710
0.7600 0.8110
0.8130 0.8530
0.8590 0.8890
0.9070 0.9270
0.9590 0.9680
1.0000 1.0000

Viscosity, Pa*s [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (1) - Liquid Viscosity, Pa*s - Liquid
0.0000 0.0008
0.1180 0.0007
0.2172 0.0006
0.3570 0.0005
0.3972 0.0005
0.5029 0.0005
0.6777 0.0004
0.8199 0.0004
1.0000 0.0003

Viscosity, Pa*s [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (1) - Liquid Viscosity, Pa*s - Liquid
0.0000 0.0008
0.1180 0.0007
0.2172 0.0006
0.3570 0.0005
0.3972 0.0005
0.5029 0.0005
0.6777 0.0004
0.8199 0.0004
1.0000 0.0003

Speed of sound, m/s [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (1) - Liquid Speed of sound, m/s - Liquid
0.0000 1231.0
0.1180 1187.4
0.2172 1157.7
0.3570 1117.9
0.3972 1106.9
0.5029 1080.7
0.6777 1041.6
0.8199 1011.6
1.0000 974.9

Speed of sound, m/s [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (1) - Liquid Speed of sound, m/s - Liquid
0.0000 1231.0
0.1180 1187.4
0.2172 1157.7
0.3570 1117.9
0.3972 1106.9
0.5029 1080.7
0.6777 1041.6
0.8199 1011.6
1.0000 974.9

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

Operational condition: Temperature, K = 303.15 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid Surface tension liquid-gas, N/m - Liquid
0.0490 0.0233
0.0980 0.0227
0.1990 0.0214
0.3010 0.0207
0.4030 0.0198
0.5090 0.0190
0.6220 0.0183
0.7270 0.0178
0.8370 0.0173
0.9360 0.0169
0.9670 0.0168

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

Operational condition: Temperature, K = 303.15 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid Surface tension liquid-gas, N/m - Liquid
0.0490 0.0233
0.0980 0.0227
0.1990 0.0214
0.3010 0.0207
0.4030 0.0198
0.5090 0.0190
0.6220 0.0183
0.7270 0.0178
0.8370 0.0173
0.9360 0.0169
0.9670 0.0168

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 94 (Liquid)

Mole fraction of Diisopropyl ether (1) - Gas Boiling temperature at pressure P, K - Liquid
0.0000 351.37
0.1060 349.96
0.1820 348.93
0.2470 348.03
0.3130 347.13
0.3690 346.39
0.4210 345.70
0.4700 345.08
0.5180 344.41
0.5650 343.89
0.6090 343.24
0.6530 342.73
0.6930 342.22
0.7350 341.80
0.7710 341.39
0.8110 340.96
0.8530 340.54
0.8890 340.13
0.9270 339.76
0.9680 339.37
1.0000 339.31

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 94 (Liquid)

Mole fraction of Diisopropyl ether (1) - Gas Boiling temperature at pressure P, K - Liquid
0.0000 351.37
0.1060 349.96
0.1820 348.93
0.2470 348.03
0.3130 347.13
0.3690 346.39
0.4210 345.70
0.4700 345.08
0.5180 344.41
0.5650 343.89
0.6090 343.24
0.6530 342.73
0.6930 342.22
0.7350 341.80
0.7710 341.39
0.8110 340.96
0.8530 340.54
0.8890 340.13
0.9270 339.76
0.9680 339.37
1.0000 339.31

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (1) - Liquid Excess molar volume, m3/mol - Liquid
0.1180 3.2000e-08
0.2172 4.7000e-08
0.3570 6.3000e-08
0.3972 6.6000e-08
0.5029 6.9000e-08
0.6777 6.3000e-08
0.8199 3.9000e-08

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (1) - Liquid Excess molar volume, m3/mol - Liquid
0.1180 3.2000e-08
0.2172 4.7000e-08
0.3570 6.3000e-08
0.3972 6.6000e-08
0.5029 6.9000e-08
0.6777 6.3000e-08
0.8199 3.9000e-08

Sources