- Name
- Ethanol, 2-methoxy-
- InChI
- InChI=1S/C3H8O2/c1-5-3-2-4/h4H,2-3H2,1H3
- InChI Key
- XNWFRZJHXBZDAG-UHFFFAOYSA-N
- Formula
- C3H8O2
- SMILES
- COCCO
- Mol. Weight (g/mol)
- 76.09
- CAS
- 109-86-4
- 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
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Datasets
- Activity coefficient (2)
- Mole fraction (4)
- η - Viscosity, Pa*s (2)
- ρl - Mass density, kg/m3 (2)
- csound,fluid - Speed of Sound, m/s (2)
- Tboil - Boiling temperature at pressure P, K (2)
Activity coefficient of Cyclohexane (2) [ref]
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mole fraction of Cyclohexane (2) - Liquid | Activity coefficient of Cyclohexane (2) - Liquid |
| 298.00 | 238.00 | 0.0000 | 11.4 |
Activity coefficient of Cyclohexane (2) [ref]
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mole fraction of Cyclohexane (2) - Liquid | Activity coefficient of Cyclohexane (2) - Liquid |
| 298.00 | 238.00 | 0.0000 | 11.4 |
Mole fraction of Ethanol, 2-methoxy- (1) [ref]
Operational condition: Temperature, K = 298.15 (Gas)
| Mole fraction of Ethanol, 2-methoxy- (1) - Liquid | Mole fraction of Ethanol, 2-methoxy- (1) - Gas |
|---|---|
| 0.0019 | 0.0147 |
| 0.0031 | 0.0203 |
| 0.0040 | 0.0222 |
| 0.0044 | 0.0264 |
| 0.0076 | 0.0398 |
| 0.0134 | 0.0512 |
| 0.0146 | 0.0571 |
| 0.0281 | 0.0744 |
| 0.0408 | 0.0653 |
| 0.0695 | 0.0718 |
| 0.1062 | 0.0764 |
| 0.1791 | 0.0790 |
| 0.2212 | 0.0806 |
| 0.2880 | 0.0804 |
| 0.3393 | 0.0817 |
| 0.4163 | 0.0801 |
| 0.4416 | 0.0824 |
| 0.5010 | 0.0786 |
| 0.5143 | 0.0786 |
| 0.5172 | 0.0775 |
| 0.6044 | 0.0857 |
| 0.6194 | 0.0887 |
| 0.6984 | 0.0880 |
| 0.7239 | 0.0879 |
| 0.8064 | 0.0963 |
| 0.8368 | 0.1068 |
| 0.8620 | 0.1145 |
| 0.9080 | 0.1336 |
| 0.9144 | 0.1493 |
| 0.9248 | 0.1569 |
| 0.9520 | 0.2082 |
| 0.9559 | 0.2290 |
| 0.9703 | 0.2779 |
| 0.9807 | 0.3807 |
| 0.9905 | 0.5395 |
Mole fraction of Cyclohexane (2) [ref]
Operational condition: Pressure, kPa = 100 (Gas)
| Mole fraction of Cyclohexane (2) - Liquid | Mole fraction of Cyclohexane (2) - Gas |
|---|---|
| 0.0120 | 0.1600 |
| 0.0350 | 0.3870 |
| 0.0640 | 0.5560 |
| 0.1190 | 0.7170 |
| 0.1520 | 0.7660 |
| 0.2520 | 0.8160 |
| 0.2840 | 0.8250 |
| 0.3310 | 0.8300 |
| 0.3870 | 0.8320 |
| 0.4660 | 0.8430 |
| 0.5260 | 0.8470 |
| 0.5840 | 0.8520 |
| 0.6300 | 0.8540 |
| 0.6750 | 0.8600 |
| 0.7340 | 0.8630 |
| 0.7790 | 0.8650 |
| 0.8500 | 0.8680 |
| 0.8790 | 0.8810 |
| 0.9340 | 0.9030 |
| 0.9810 | 0.9540 |
Mole fraction of Ethanol, 2-methoxy- (1) [ref]
Operational condition: Temperature, K = 298.15 (Gas)
| Mole fraction of Ethanol, 2-methoxy- (1) - Liquid | Mole fraction of Ethanol, 2-methoxy- (1) - Gas |
|---|---|
| 0.0019 | 0.0147 |
| 0.0031 | 0.0203 |
| 0.0040 | 0.0222 |
| 0.0044 | 0.0264 |
| 0.0076 | 0.0398 |
| 0.0134 | 0.0512 |
| 0.0146 | 0.0571 |
| 0.0281 | 0.0744 |
| 0.0408 | 0.0653 |
| 0.0695 | 0.0718 |
| 0.1062 | 0.0764 |
| 0.1791 | 0.0790 |
| 0.2212 | 0.0806 |
| 0.2880 | 0.0804 |
| 0.3393 | 0.0817 |
| 0.4163 | 0.0801 |
| 0.4416 | 0.0824 |
| 0.5010 | 0.0786 |
| 0.5143 | 0.0786 |
| 0.5172 | 0.0775 |
| 0.6044 | 0.0857 |
| 0.6194 | 0.0887 |
| 0.6984 | 0.0880 |
| 0.7239 | 0.0879 |
| 0.8064 | 0.0963 |
| 0.8368 | 0.1068 |
| 0.8620 | 0.1145 |
| 0.9080 | 0.1336 |
| 0.9144 | 0.1493 |
| 0.9248 | 0.1569 |
| 0.9520 | 0.2082 |
| 0.9559 | 0.2290 |
| 0.9703 | 0.2779 |
| 0.9807 | 0.3807 |
| 0.9905 | 0.5395 |
Mole fraction of Cyclohexane (2) [ref]
Operational condition: Pressure, kPa = 100 (Gas)
| Mole fraction of Cyclohexane (2) - Liquid | Mole fraction of Cyclohexane (2) - Gas |
|---|---|
| 0.0120 | 0.1600 |
| 0.0350 | 0.3870 |
| 0.0640 | 0.5560 |
| 0.1190 | 0.7170 |
| 0.1520 | 0.7660 |
| 0.2520 | 0.8160 |
| 0.2840 | 0.8250 |
| 0.3310 | 0.8300 |
| 0.3870 | 0.8320 |
| 0.4660 | 0.8430 |
| 0.5260 | 0.8470 |
| 0.5840 | 0.8520 |
| 0.6300 | 0.8540 |
| 0.6750 | 0.8600 |
| 0.7340 | 0.8630 |
| 0.7790 | 0.8650 |
| 0.8500 | 0.8680 |
| 0.8790 | 0.8810 |
| 0.9340 | 0.9030 |
| 0.9810 | 0.9540 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-methoxy- (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0540 | 0.0009 |
| 298.15 | 0.1506 | 0.0009 |
| 298.15 | 0.2513 | 0.0009 |
| 298.15 | 0.3532 | 0.0010 |
| 298.15 | 0.4508 | 0.0010 |
| 298.15 | 0.4955 | 0.0011 |
| 298.15 | 0.5513 | 0.0011 |
| 298.15 | 0.6490 | 0.0012 |
| 298.15 | 0.7493 | 0.0013 |
| 298.15 | 0.8496 | 0.0014 |
| 298.15 | 0.9529 | 0.0015 |
| 308.15 | 0.0540 | 0.0008 |
| 308.15 | 0.1506 | 0.0008 |
| 308.15 | 0.2513 | 0.0008 |
| 308.15 | 0.3532 | 0.0008 |
| 308.15 | 0.4508 | 0.0008 |
| 308.15 | 0.4955 | 0.0008 |
| 308.15 | 0.5513 | 0.0009 |
| 308.15 | 0.6490 | 0.0009 |
| 308.15 | 0.7493 | 0.0010 |
| 308.15 | 0.8496 | 0.0011 |
| 308.15 | 0.9529 | 0.0012 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-methoxy- (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0540 | 0.0009 |
| 298.15 | 0.1506 | 0.0009 |
| 298.15 | 0.2513 | 0.0009 |
| 298.15 | 0.3532 | 0.0010 |
| 298.15 | 0.4508 | 0.0010 |
| 298.15 | 0.4955 | 0.0011 |
| 298.15 | 0.5513 | 0.0011 |
| 298.15 | 0.6490 | 0.0012 |
| 298.15 | 0.7493 | 0.0013 |
| 298.15 | 0.8496 | 0.0014 |
| 298.15 | 0.9529 | 0.0015 |
| 308.15 | 0.0540 | 0.0008 |
| 308.15 | 0.1506 | 0.0008 |
| 308.15 | 0.2513 | 0.0008 |
| 308.15 | 0.3532 | 0.0008 |
| 308.15 | 0.4508 | 0.0008 |
| 308.15 | 0.4955 | 0.0008 |
| 308.15 | 0.5513 | 0.0009 |
| 308.15 | 0.6490 | 0.0009 |
| 308.15 | 0.7493 | 0.0010 |
| 308.15 | 0.8496 | 0.0011 |
| 308.15 | 0.9529 | 0.0012 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-methoxy- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0540 | 779.6 |
| 298.15 | 0.1506 | 791.26 |
| 298.15 | 0.2513 | 804.98 |
| 298.15 | 0.3532 | 820.23 |
| 298.15 | 0.4508 | 836.01 |
| 298.15 | 0.4955 | 843.61 |
| 298.15 | 0.5513 | 853.47 |
| 298.15 | 0.6490 | 871.88 |
| 298.15 | 0.7493 | 892.72 |
| 298.15 | 0.8496 | 916.39 |
| 298.15 | 0.9529 | 945.13 |
| 303.15 | 0.0540 | 774.21 |
| 303.15 | 0.1506 | 785.84 |
| 303.15 | 0.2513 | 799.48 |
| 303.15 | 0.3532 | 814.65 |
| 303.15 | 0.4508 | 830.4 |
| 303.15 | 0.4955 | 838.01 |
| 303.15 | 0.5513 | 847.91 |
| 303.15 | 0.6490 | 866.44 |
| 303.15 | 0.7493 | 887.49 |
| 303.15 | 0.8496 | 911.41 |
| 303.15 | 0.9529 | 940.38 |
| 308.15 | 0.0540 | 770.01 |
| 308.15 | 0.1506 | 781.46 |
| 308.15 | 0.2513 | 795.15 |
| 308.15 | 0.3532 | 810.51 |
| 308.15 | 0.4508 | 826.48 |
| 308.15 | 0.4955 | 834.21 |
| 308.15 | 0.5513 | 844.24 |
| 308.15 | 0.6490 | 862.98 |
| 308.15 | 0.7493 | 884.25 |
| 308.15 | 0.8496 | 908.47 |
| 308.15 | 0.9529 | 937.97 |
| 313.15 | 0.0540 | 764.53 |
| 313.15 | 0.1506 | 775.56 |
| 313.15 | 0.2513 | 789.09 |
| 313.15 | 0.3532 | 804.43 |
| 313.15 | 0.4508 | 820.39 |
| 313.15 | 0.4955 | 828.08 |
| 313.15 | 0.5513 | 838.04 |
| 313.15 | 0.6490 | 856.55 |
| 313.15 | 0.7493 | 877.48 |
| 313.15 | 0.8496 | 901.33 |
| 313.15 | 0.9529 | 930.66 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-methoxy- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0540 | 779.6 |
| 298.15 | 0.1506 | 791.26 |
| 298.15 | 0.2513 | 804.98 |
| 298.15 | 0.3532 | 820.23 |
| 298.15 | 0.4508 | 836.01 |
| 298.15 | 0.4955 | 843.61 |
| 298.15 | 0.5513 | 853.47 |
| 298.15 | 0.6490 | 871.88 |
| 298.15 | 0.7493 | 892.72 |
| 298.15 | 0.8496 | 916.39 |
| 298.15 | 0.9529 | 945.13 |
| 303.15 | 0.0540 | 774.21 |
| 303.15 | 0.1506 | 785.84 |
| 303.15 | 0.2513 | 799.48 |
| 303.15 | 0.3532 | 814.65 |
| 303.15 | 0.4508 | 830.4 |
| 303.15 | 0.4955 | 838.01 |
| 303.15 | 0.5513 | 847.91 |
| 303.15 | 0.6490 | 866.44 |
| 303.15 | 0.7493 | 887.49 |
| 303.15 | 0.8496 | 911.41 |
| 303.15 | 0.9529 | 940.38 |
| 308.15 | 0.0540 | 770.01 |
| 308.15 | 0.1506 | 781.46 |
| 308.15 | 0.2513 | 795.15 |
| 308.15 | 0.3532 | 810.51 |
| 308.15 | 0.4508 | 826.48 |
| 308.15 | 0.4955 | 834.21 |
| 308.15 | 0.5513 | 844.24 |
| 308.15 | 0.6490 | 862.98 |
| 308.15 | 0.7493 | 884.25 |
| 308.15 | 0.8496 | 908.47 |
| 308.15 | 0.9529 | 937.97 |
| 313.15 | 0.0540 | 764.53 |
| 313.15 | 0.1506 | 775.56 |
| 313.15 | 0.2513 | 789.09 |
| 313.15 | 0.3532 | 804.43 |
| 313.15 | 0.4508 | 820.39 |
| 313.15 | 0.4955 | 828.08 |
| 313.15 | 0.5513 | 838.04 |
| 313.15 | 0.6490 | 856.55 |
| 313.15 | 0.7493 | 877.48 |
| 313.15 | 0.8496 | 901.33 |
| 313.15 | 0.9529 | 930.66 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-methoxy- (1) - Liquid | Speed of sound, m/s - Liquid |
| 298.15 | 0.0540 | 1249.0 |
| 298.15 | 0.1506 | 1240.0 |
| 298.15 | 0.2513 | 1237.0 |
| 298.15 | 0.3532 | 1234.0 |
| 298.15 | 0.4508 | 1236.0 |
| 298.15 | 0.4955 | 1239.0 |
| 298.15 | 0.5513 | 1244.0 |
| 298.15 | 0.6490 | 1256.0 |
| 298.15 | 0.7493 | 1274.0 |
| 298.15 | 0.8496 | 1295.0 |
| 298.15 | 0.9529 | 1325.0 |
| 308.15 | 0.0540 | 1205.0 |
| 308.15 | 0.1506 | 1194.0 |
| 308.15 | 0.2513 | 1195.0 |
| 308.15 | 0.3532 | 1196.0 |
| 308.15 | 0.4508 | 1200.0 |
| 308.15 | 0.4955 | 1203.0 |
| 308.15 | 0.5513 | 1207.0 |
| 308.15 | 0.6490 | 1218.0 |
| 308.15 | 0.7493 | 1236.0 |
| 308.15 | 0.8496 | 1250.0 |
| 308.15 | 0.9529 | 1303.0 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-methoxy- (1) - Liquid | Speed of sound, m/s - Liquid |
| 298.15 | 0.0540 | 1249.0 |
| 298.15 | 0.1506 | 1240.0 |
| 298.15 | 0.2513 | 1237.0 |
| 298.15 | 0.3532 | 1234.0 |
| 298.15 | 0.4508 | 1236.0 |
| 298.15 | 0.4955 | 1239.0 |
| 298.15 | 0.5513 | 1244.0 |
| 298.15 | 0.6490 | 1256.0 |
| 298.15 | 0.7493 | 1274.0 |
| 298.15 | 0.8496 | 1295.0 |
| 298.15 | 0.9529 | 1325.0 |
| 308.15 | 0.0540 | 1205.0 |
| 308.15 | 0.1506 | 1194.0 |
| 308.15 | 0.2513 | 1195.0 |
| 308.15 | 0.3532 | 1196.0 |
| 308.15 | 0.4508 | 1200.0 |
| 308.15 | 0.4955 | 1203.0 |
| 308.15 | 0.5513 | 1207.0 |
| 308.15 | 0.6490 | 1218.0 |
| 308.15 | 0.7493 | 1236.0 |
| 308.15 | 0.8496 | 1250.0 |
| 308.15 | 0.9529 | 1303.0 |
Boiling temperature at pressure P, K [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Mole fraction of Cyclohexane (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0120 | 391.80 |
| 0.0350 | 382.99 |
| 0.0640 | 375.57 |
| 0.1190 | 363.75 |
| 0.1520 | 361.04 |
| 0.2520 | 355.47 |
| 0.2840 | 354.52 |
| 0.3310 | 353.54 |
| 0.3870 | 352.80 |
| 0.4660 | 352.21 |
| 0.5260 | 351.85 |
| 0.5840 | 351.55 |
| 0.6300 | 351.48 |
| 0.6750 | 351.36 |
| 0.7340 | 351.17 |
| 0.7790 | 351.10 |
| 0.8500 | 351.03 |
| 0.8790 | 350.99 |
| 0.9340 | 351.18 |
| 0.9810 | 352.34 |
Boiling temperature at pressure P, K [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Mole fraction of Cyclohexane (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0120 | 391.80 |
| 0.0350 | 382.99 |
| 0.0640 | 375.57 |
| 0.1190 | 363.75 |
| 0.1520 | 361.04 |
| 0.2520 | 355.47 |
| 0.2840 | 354.52 |
| 0.3310 | 353.54 |
| 0.3870 | 352.80 |
| 0.4660 | 352.21 |
| 0.5260 | 351.85 |
| 0.5840 | 351.55 |
| 0.6300 | 351.48 |
| 0.6750 | 351.36 |
| 0.7340 | 351.17 |
| 0.7790 | 351.10 |
| 0.8500 | 351.03 |
| 0.8790 | 350.99 |
| 0.9340 | 351.18 |
| 0.9810 | 352.34 |
Sources
- Thermodynamics of solvation in propylene glycol and methyl cellosolve
- Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for CmH2m+1(OCH2CH2)nOH (m ) 1 or 2 or 4 andn ) 1) + Benzene, + Toluene, + (o-, m-, and p-) Xylenes, + Ethylbenzene, and + Cyclohexane
- Excess Gibbs Energies of the Ternary System 2-Methoxyethanol + Tetrahydrofuran + Cyclohexane and Other Relevant Binaries at 298.15 K
- Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures with Cyclohexane, Cyclohexene, and 2-Methoxyethanol at 100 kPa