- 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
- 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
- Mole fraction (2)
- η - Viscosity, Pa*s (2)
- csound,fluid - Speed of Sound, m/s (2)
- γ - Surface tension liquid-gas, N/m (2)
- Tboil - Boiling temperature at pressure P, K (2)
- 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)
Mole fraction of Diisopropyl ether (1)
0
0.2
0.4
0.6
0.8
1
0
0.5
1
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)
Mole fraction of Diisopropyl ether (1)
0
0.2
0.4
0.6
0.8
1
0
0.5
1
Viscosity, Pa*s [ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| 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 |
Mole fraction of Diisopropyl ether (1)
Viscosity, Pa*s
4.00e-4
5.00e-4
6.00e-4
7.00e-4
8.00e-4
0
0.5
1
Viscosity, Pa*s [ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| 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 |
Mole fraction of Diisopropyl ether (1)
Viscosity, Pa*s
4.00e-4
5.00e-4
6.00e-4
7.00e-4
8.00e-4
0
0.5
1
Speed of sound, m/s [ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| 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 |
Mole fraction of Diisopropyl ether (1)
Speed of sound, m/s
950
1000
1050
1100
1150
1200
1250
0
0.5
1
Speed of sound, m/s [ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| 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 |
Mole fraction of Diisopropyl ether (1)
Speed of sound, m/s
950
1000
1050
1100
1150
1200
1250
0
0.5
1
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 |
Mole fraction of Diisopropyl ether (1)
Surface tension liquid-gas, N/m
0.02
0.02
0.02
0.02
0.02
0.02
0.02
0.2
0.4
0.6000000000000001
0.8
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 |
Mole fraction of Diisopropyl ether (1)
Surface tension liquid-gas, N/m
0.02
0.02
0.02
0.02
0.02
0.02
0.02
0.2
0.4
0.6000000000000001
0.8
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 |
Mole fraction of Diisopropyl ether (1)
Boiling temperature at pressure P, K
340
342
344
346
348
350
352
0
0.5
1
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 |
Mole fraction of Diisopropyl ether (1)
Boiling temperature at pressure P, K
340
342
344
346
348
350
352
0
0.5
1
Excess molar volume, m3/mol [ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| 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 |
Mole fraction of Diisopropyl ether (1)
Excess molar volume, m3/mol
3.00e-8
4.00e-8
5.00e-8
6.00e-8
7.00e-8
0.2
0.4
0.6000000000000001
0.8
Excess molar volume, m3/mol [ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| 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 |
Mole fraction of Diisopropyl ether (1)
Excess molar volume, m3/mol
3.00e-8
4.00e-8
5.00e-8
6.00e-8
7.00e-8
0.2
0.4
0.6000000000000001
0.8