- InChI
- InChI=1S/C3H8O2/c1-5-3-2-4/h4H,2-3H2,1H3
- InChI Key
- XNWFRZJHXBZDAG-UHFFFAOYSA-N
- Formula
- C3H8O2
- SMILES
- COCCO
- Molecular Weight1
- 76.09
- CAS
- 109-86-4
- Other Names
-
- 1,2-ethanediol, methyl ether
- 1,2-ethanediol, monomethyl ether
- 1-Hydroxy-2-methoxyethane
- 2-Hydroxyethyl methyl ether
- 2-Methoxy-1-ethanol
- 2-Methoxy-aethanol
- 2-Methoxyethanol
- 2-Methoxyethyl alcohol
- 2-Metossietanolo
- 2-methoxyethan-1-ol
- 2-methoxyethanol (methyl cellosolve)
- 3-Oxa-1-butanol
- Aethylenglykol-monomethylaether
- Amsco-Solv EE
- Dowanol EM
- EGM
- EGME
- Ektasolve EM
- Ether monomethylique de l'ethylene-glycol
- Ethylene glycol methyl ether
- Ethylene glycol monomethyl ether
- Glycol ether EM
- Glycol monomethyl ether
- Glycolmethyl ether
- HOCH2CH2OCH3
- Jeffersol EM
- MECS
- Methoxyethanol
- Methoxyethylene glycol
- Methoxyhydroxyethane
- Methyl cellosolve
- Methyl ethoxol
- Methyl glycol
- Methyl icinol
- Methyl oxitol
- Methylcelosolv
- Methylglykol
- Metil cellosolve
- Metoksyetylowy alkohol
- Monoethylene glycol methyl ether
- Monomethyl ether of ethylene glycol
- Monomethyl glycol
- NSC 1258
- Poly-Solv EM
- Prist
- UN 1188
- ethylene glycol, monomethyl ether
- «beta»-Methoxyethanol
- «beta»-Methoxyethanol
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- Vm : Molar Volume (m3/mol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| PAff | 768.80 | kJ/mol | NIST |
| BasG | 729.80 | kJ/mol | NIST |
| ΔcH°liquid | -1880.00 | kJ/mol | NIST |
| η | 0.0015119 | Pa×s | Volumet... |
| ΔfG° | -267.44 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-395.90; -376.90] | kJ/mol |
|
| ΔfH°gas | -376.90 ± 8.10 | kJ/mol | NIST |
| ΔfH°gas | -395.90 | kJ/mol | NIST |
| ΔfH°liquid | [-441.00; -422.00] | kJ/mol |
|
| ΔfH°liquid | -422.00 ± 7.60 | kJ/mol | NIST |
| ΔfH°liquid | -441.00 | kJ/mol | NIST |
| ΔfusH° | 8.80 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [45.10; 45.20] | kJ/mol |
|
| ΔvapH° | 45.20 | kJ/mol | NIST |
| ΔvapH° | 45.10 | kJ/mol | NIST |
| ΔvapH° | 45.20 ± 0.20 | kJ/mol | NIST |
| IE | 10.13 | eV | NIST |
| log10WS | 0.57 | Crippen Calculated Property | |
| logPoct/wat | -0.375 | Crippen Calculated Property | |
| McVol | 64.870 | ml/mol | McGowan Calculated Property |
| Pc | [3600.00; 5285.00] | kPa |
|
| Pc | 5285.00 ± 20.00 | kPa | NIST |
| Pc | 3600.00 ± 5.00 | kPa | NIST |
| ρc | [289.16; 306.66] | kg/m3 |
|
| ρc | 289.16 ± 6.85 | kg/m3 | NIST |
| ρc | 306.66 ± 3.04 | kg/m3 | NIST |
| Inp | [588.00; 646.00] |
|
|
| Inp | 630.00 | NIST | |
| Inp | Outlier 588.00 | NIST | |
| Inp | 591.00 | NIST | |
| Inp | 595.00 | NIST | |
| Inp | 617.00 | NIST | |
| Inp | 624.00 | NIST | |
| Inp | 635.00 | NIST | |
| Inp | 629.00 | NIST | |
| Inp | 629.00 | NIST | |
| Inp | 618.00 | NIST | |
| Inp | 646.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 623.00 | NIST | |
| Inp | 616.00 | NIST | |
| Inp | 635.30 | NIST | |
| Inp | 617.00 | NIST | |
| Inp | 617.00 | NIST | |
| Inp | 616.00 | NIST | |
| Inp | 616.00 | NIST | |
| Inp | 617.00 | NIST | |
| I | [1172.00; 1225.00] |
|
|
| I | 1184.00 | NIST | |
| I | Outlier 1225.00 | NIST | |
| I | 1180.00 | NIST | |
| I | 1202.00 | NIST | |
| I | 1199.00 | NIST | |
| I | 1199.00 | NIST | |
| I | 1172.00 | NIST | |
| I | 1180.00 | NIST | |
| Tboil | [397.30; 397.70] | K |
|
| Tboil | 397.63 | K | Isobari... |
| Tboil | 397.67 | K | Isobari... |
| Tboil | 397.67 | K | Isobari... |
| Tboil | 397.58 | K | Evaluat... |
| Tboil | 397.60 ± 0.40 | K | NIST |
| Tboil | 397.50 ± 0.50 | K | NIST |
| Tboil | 397.70 | K | NIST |
| Tboil | Outlier 397.30 | K | NIST |
| Tboil | 397.65 ± 0.40 | K | NIST |
| Tboil | 397.36 ± 0.20 | K | NIST |
| Tboil | 397.65 | K | NIST |
| Tboil | 397.70 ± 0.50 | K | NIST |
| Tboil | 397.60 ± 1.00 | K | NIST |
| Tc | [571.00; 597.60] | K |
|
| Tc | 597.60 ± 0.20 | K | NIST |
| Tc | 571.00 ± 2.00 | K | NIST |
| Tfus | 188.05 | K | NIST |
| Vc | 0.240 | m3/kmol | Joback Calculated Property |
| Vm | 7.93e-05 | m3/mol | Excess ... |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [120.54; 151.76] | J/mol×K | [382.64; 545.53] |
|
| Cp,gas | 120.54 | J/mol×K | 382.64 | Joback Calculated Property |
| Cp,gas | 126.06 | J/mol×K | 409.79 | Joback Calculated Property |
| Cp,gas | 131.45 | J/mol×K | 436.94 | Joback Calculated Property |
| Cp,gas | 136.72 | J/mol×K | 464.08 | Joback Calculated Property |
| Cp,gas | 141.87 | J/mol×K | 491.23 | Joback Calculated Property |
| Cp,gas | 146.88 | J/mol×K | 518.38 | Joback Calculated Property |
| Cp,gas | 151.76 | J/mol×K | 545.53 | Joback Calculated Property |
| Cp,liquid | [174.90; 176.60] | J/mol×K | [298.15; 298.15] |
|
| Cp,liquid | 175.38 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 176.60 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 174.90 | J/mol×K | 298.15 | NIST |
| η | [0.0010470; 0.0017080] | Pa×s | [293.15; 318.15] |
|
| η | 0.0017080 | Pa×s | 293.15 | Relativ... |
| η | 0.0015440 | Pa×s | 298.15 | Relativ... |
| η | 0.0015430 | Pa×s | 298.15 | Viscosi... |
| η | 0.0015920 | Pa×s | 298.15 | Densiti... |
| η | 0.0015430 | Pa×s | 298.15 | Density... |
| η | 0.0014040 | Pa×s | 303.15 | Relativ... |
| η | 0.0012420 | Pa×s | 308.15 | Densiti... |
| η | 0.0012560 | Pa×s | 308.15 | Density... |
| η | 0.0012570 | Pa×s | 308.15 | Viscosi... |
| η | 0.0010470 | Pa×s | 318.15 | Density... |
| η | 0.0010510 | Pa×s | 318.15 | Viscosi... |
| ΔvapH | [37.54; 43.00] | kJ/mol | [273.00; 397.30] |
|
| ΔvapH | 41.30 | kJ/mol | 273.00 | NIST |
| ΔvapH | 42.90 | kJ/mol | 362.50 | NIST |
| ΔvapH | 43.00 | kJ/mol | 371.50 | NIST |
| ΔvapH | 42.80 | kJ/mol | 378.00 | NIST |
| ΔvapH | 37.54 | kJ/mol | 397.30 | NIST |
| Pvap | [15.00; 176.50] | kPa | [346.40; 416.60] |
|
| Pvap | 15.00 | kPa | 346.40 | Supplem... |
| Pvap | 23.50 | kPa | 356.90 | Supplem... |
| Pvap | 28.10 | kPa | 364.15 | Vapor-l... |
| Pvap | 32.00 | kPa | 364.70 | Supplem... |
| Pvap | 34.20 | kPa | 368.84 | Vapor-l... |
| Pvap | 41.30 | kPa | 373.48 | Vapor-l... |
| Pvap | 49.00 | kPa | 376.00 | Supplem... |
| Pvap | 47.90 | kPa | 377.22 | Vapor-l... |
| Pvap | 53.70 | kPa | 380.17 | Vapor-l... |
| Pvap | 57.50 | kPa | 380.60 | Supplem... |
| Pvap | 60.50 | kPa | 383.30 | Vapor-l... |
| Pvap | 66.00 | kPa | 384.50 | Supplem... |
| Pvap | 68.60 | kPa | 386.66 | Vapor-l... |
| Pvap | 74.50 | kPa | 388.10 | Supplem... |
| Pvap | 76.40 | kPa | 389.59 | Vapor-l... |
| Pvap | 81.20 | kPa | 391.28 | Vapor-l... |
| Pvap | 83.00 | kPa | 391.30 | Supplem... |
| Pvap | 88.70 | kPa | 393.75 | Vapor-l... |
| Pvap | 91.50 | kPa | 394.40 | Supplem... |
| Pvap | 95.30 | kPa | 395.78 | Vapor-l... |
| Pvap | 100.00 | kPa | 397.20 | Supplem... |
| Pvap | 101.30 | kPa | 397.58 | Evaluat... |
| Pvap | 101.30 | kPa | 397.67 | Isobari... |
| Pvap | 108.50 | kPa | 400.10 | Supplem... |
| Pvap | 117.00 | kPa | 402.60 | Supplem... |
| Pvap | 125.50 | kPa | 404.90 | Supplem... |
| Pvap | 134.00 | kPa | 407.00 | Supplem... |
| Pvap | 142.50 | kPa | 409.10 | Supplem... |
| Pvap | 151.00 | kPa | 411.10 | Supplem... |
| Pvap | 159.50 | kPa | 412.90 | Supplem... |
| Pvap | 168.00 | kPa | 414.70 | Supplem... |
| Pvap | 176.50 | kPa | 416.60 | Supplem... |
| n0 | [1.39830; 1.40060] | [298.15; 303.15] |
|
|
| n0 | 1.40060 | 298.15 | Isobari... | |
| n0 | 1.40020 | 298.15 | Effect ... | |
| n0 | 1.40040 | 298.15 | Non-ide... | |
| n0 | 1.40040 | 298.15 | Physica... | |
| n0 | 1.40020 | 298.15 | Thermod... | |
| n0 | 1.40030 | 298.15 | Volumet... | |
| n0 | 1.39830 | 303.15 | Densiti... | |
| ρl | [898.55; 974.70] | kg/m3 | [283.15; 363.15] |
|
| ρl | 974.70 | kg/m3 | 283.15 | Solubil... |
| ρl | 969.90 | kg/m3 | 288.15 | Solubil... |
| ρl | 966.52 | kg/m3 | 291.15 | Density... |
| ρl | 964.70 | kg/m3 | 293.15 | Density... |
| ρl | 964.86 | kg/m3 | 293.15 | Densiti... |
| ρl | 964.88 | kg/m3 | 293.15 | Volumet... |
| ρl | 965.20 | kg/m3 | 293.15 | Viscosi... |
| ρl | 964.88 | kg/m3 | 293.15 | Density... |
| ρl | 964.70 | kg/m3 | 293.15 | Solubil... |
| ρl | 964.70 | kg/m3 | 293.15 | Monoeth... |
| ρl | 960.32 | kg/m3 | 298.15 | Speeds ... |
| ρl | 960.10 | kg/m3 | 298.15 | Monoeth... |
| ρl | 960.90 | kg/m3 | 298.15 | Study o... |
| ρl | 960.31 | kg/m3 | 298.15 | Density... |
| ρl | 960.89 | kg/m3 | 298.15 | Modifie... |
| ρl | 960.29 | kg/m3 | 298.15 | Density... |
| ρl | 960.10 | kg/m3 | 298.15 | Solubil... |
| ρl | 960.29 | kg/m3 | 298.15 | Volumet... |
| ρl | 960.10 | kg/m3 | 298.15 | Isobari... |
| ρl | 960.32 | kg/m3 | 298.15 | Study o... |
| ρl | 960.29 | kg/m3 | 298.15 | FT-IR s... |
| ρl | 960.01 | kg/m3 | 298.15 | Excess ... |
| ρl | 959.73 | kg/m3 | 298.15 | Liquid ... |
| ρl | 960.20 | kg/m3 | 298.15 | Isobari... |
| ρl | 960.20 | kg/m3 | 298.15 | Density... |
| ρl | 955.76 | kg/m3 | 303.15 | Volumet... |
| ρl | 956.73 | kg/m3 | 303.15 | Surface... |
| ρl | 955.76 | kg/m3 | 303.15 | Density... |
| ρl | 955.50 | kg/m3 | 303.15 | Monoeth... |
| ρl | 955.84 | kg/m3 | 303.15 | FT-IR s... |
| ρl | 955.68 | kg/m3 | 303.15 | Densiti... |
| ρl | 955.50 | kg/m3 | 303.15 | Density... |
| ρl | 955.71 | kg/m3 | 303.15 | Density... |
| ρl | 955.50 | kg/m3 | 303.15 | Solubil... |
| ρl | 955.71 | kg/m3 | 303.15 | Study o... |
| ρl | 955.72 | kg/m3 | 303.15 | Intermo... |
| ρl | 951.11 | kg/m3 | 308.15 | Intermo... |
| ρl | 951.08 | kg/m3 | 308.15 | Study o... |
| ρl | 951.10 | kg/m3 | 308.15 | Volumet... |
| ρl | 952.09 | kg/m3 | 308.15 | Surface... |
| ρl | 951.16 | kg/m3 | 308.15 | FT-IR s... |
| ρl | 950.90 | kg/m3 | 308.15 | Solubil... |
| ρl | 950.90 | kg/m3 | 308.15 | Monoeth... |
| ρl | 951.10 | kg/m3 | 308.15 | Density... |
| ρl | 951.70 | kg/m3 | 308.15 | Study o... |
| ρl | 951.08 | kg/m3 | 308.15 | Density... |
| ρl | 950.90 | kg/m3 | 308.15 | Density... |
| ρl | 946.27 | kg/m3 | 313.15 | Intermo... |
| ρl | 946.20 | kg/m3 | 313.15 | Density... |
| ρl | 946.20 | kg/m3 | 313.15 | Monoeth... |
| ρl | 946.20 | kg/m3 | 313.15 | Solubil... |
| ρl | 946.54 | kg/m3 | 313.15 | Volumet... |
| ρl | 947.42 | kg/m3 | 313.15 | Surface... |
| ρl | 946.49 | kg/m3 | 313.15 | FT-IR s... |
| ρl | 946.41 | kg/m3 | 313.15 | Density... |
| ρl | 946.42 | kg/m3 | 313.15 | Study o... |
| ρl | 946.38 | kg/m3 | 313.15 | Densiti... |
| ρl | 941.50 | kg/m3 | 318.15 | Density... |
| ρl | 942.72 | kg/m3 | 318.15 | Surface... |
| ρl | 941.50 | kg/m3 | 318.15 | Solubil... |
| ρl | 942.70 | kg/m3 | 318.15 | Study o... |
| ρl | 941.50 | kg/m3 | 318.15 | Monoeth... |
| ρl | 941.72 | kg/m3 | 318.15 | Density... |
| ρl | 941.64 | kg/m3 | 318.15 | Intermo... |
| ρl | 941.89 | kg/m3 | 318.15 | FT-IR s... |
| ρl | 941.72 | kg/m3 | 318.15 | Study o... |
| ρl | 936.95 | kg/m3 | 323.15 | Densiti... |
| ρl | 936.88 | kg/m3 | 323.15 | Intermo... |
| ρl | 936.70 | kg/m3 | 323.15 | Monoeth... |
| ρl | 937.98 | kg/m3 | 323.15 | Surface... |
| ρl | 936.70 | kg/m3 | 323.15 | Solubil... |
| ρl | 936.89 | kg/m3 | 323.15 | Study o... |
| ρl | 936.80 | kg/m3 | 323.15 | Density... |
| ρl | 936.99 | kg/m3 | 323.15 | Density... |
| ρl | 933.40 | kg/m3 | 328.15 | Study o... |
| ρl | 932.00 | kg/m3 | 328.15 | Monoeth... |
| ρl | 932.00 | kg/m3 | 328.15 | Solubil... |
| ρl | 933.21 | kg/m3 | 328.15 | Surface... |
| ρl | 932.00 | kg/m3 | 328.15 | Density... |
| ρl | 927.20 | kg/m3 | 333.15 | Density... |
| ρl | 928.39 | kg/m3 | 333.15 | Surface... |
| ρl | 927.20 | kg/m3 | 333.15 | Monoeth... |
| ρl | 927.38 | kg/m3 | 333.15 | Densiti... |
| ρl | 927.20 | kg/m3 | 333.15 | Solubil... |
| ρl | 923.54 | kg/m3 | 338.15 | Surface... |
| ρl | 922.30 | kg/m3 | 338.15 | Monoeth... |
| ρl | 922.40 | kg/m3 | 338.15 | Density... |
| ρl | 917.40 | kg/m3 | 343.15 | Monoeth... |
| ρl | 918.64 | kg/m3 | 343.15 | Surface... |
| ρl | 917.64 | kg/m3 | 343.15 | Densiti... |
| ρl | 917.50 | kg/m3 | 343.15 | Density... |
| ρl | 912.40 | kg/m3 | 348.15 | Monoeth... |
| ρl | 912.50 | kg/m3 | 348.15 | Density... |
| ρl | 913.69 | kg/m3 | 348.15 | Surface... |
| ρl | 908.70 | kg/m3 | 353.15 | Surface... |
| ρl | 907.50 | kg/m3 | 353.15 | Density... |
| ρl | 907.40 | kg/m3 | 353.15 | Monoeth... |
| ρl | 903.65 | kg/m3 | 358.15 | Surface... |
| ρl | 898.55 | kg/m3 | 363.15 | Surface... |
| csound,fluid | [1260.70; 1380.00] | m/s | [288.15; 323.15] |
|
| csound,fluid | 1376.47 | m/s | 288.15 | Densiti... |
| csound,fluid | 1380.00 | m/s | 288.15 | Volumet... |
| csound,fluid | 1359.04 | m/s | 293.15 | Densiti... |
| csound,fluid | 1367.00 | m/s | 293.15 | Volumet... |
| csound,fluid | 1351.00 | m/s | 298.15 | Volumet... |
| csound,fluid | 1341.72 | m/s | 298.15 | Densiti... |
| csound,fluid | 1324.47 | m/s | 303.15 | Densiti... |
| csound,fluid | 1337.00 | m/s | 303.15 | Volumet... |
| csound,fluid | 1324.20 | m/s | 303.15 | Acousti... |
| csound,fluid | 1324.50 | m/s | 303.15 | Densiti... |
| csound,fluid | 1312.60 | m/s | 308.15 | Densiti... |
| csound,fluid | 1321.00 | m/s | 308.15 | Volumet... |
| csound,fluid | 1307.14 | m/s | 308.15 | Densiti... |
| csound,fluid | 1289.95 | m/s | 313.15 | Densiti... |
| csound,fluid | 1304.00 | m/s | 313.15 | Volumet... |
| csound,fluid | 1293.90 | m/s | 313.15 | Acousti... |
| csound,fluid | 1299.60 | m/s | 313.15 | Densiti... |
| csound,fluid | 1272.81 | m/s | 318.15 | Densiti... |
| csound,fluid | 1287.20 | m/s | 318.15 | Densiti... |
| csound,fluid | 1287.00 | m/s | 318.15 | Volumet... |
| csound,fluid | 1260.70 | m/s | 323.15 | Acousti... |
| γ | [0.03; 0.03] | N/m | [298.15; 318.15] |
|
| γ | 0.03 | N/m | 298.15 | Experim... |
| γ | 0.03 | N/m | 298.15 | Excess ... |
| γ | 0.03 | N/m | 308.15 | Experim... |
| γ | 0.03 | N/m | 313.15 | Excess ... |
| γ | 0.03 | N/m | 318.15 | Experim... |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 20000.00 | 0.0019 |
| 293.15 | 40000.00 | 0.0022 |
| 293.15 | 60000.00 | 0.0024 |
| 293.15 | 80000.00 | 0.0027 |
| 293.15 | 100000.00 | 0.0029 |
| 303.15 | 20000.00 | 0.0016 |
| 303.15 | 40000.00 | 0.0018 |
| 303.15 | 60000.00 | 0.0020 |
| 303.15 | 80000.00 | 0.0022 |
| 303.15 | 100000.00 | 0.0024 |
| 313.15 | 20000.00 | 0.0013 |
| 313.15 | 40000.00 | 0.0015 |
| 313.15 | 60000.00 | 0.0016 |
| 313.15 | 80000.00 | 0.0018 |
| 313.15 | 100000.00 | 0.0020 |
| 323.15 | 20000.00 | 0.0011 |
| 323.15 | 40000.00 | 0.0013 |
| 323.15 | 60000.00 | 0.0014 |
| 323.15 | 80000.00 | 0.0015 |
| 323.15 | 100000.00 | 0.0017 |
| 333.15 | 20000.00 | 0.0010 |
| 333.15 | 40000.00 | 0.0011 |
| 333.15 | 60000.00 | 0.0012 |
| 333.15 | 80000.00 | 0.0013 |
| 333.15 | 100000.00 | 0.0015 |
| 343.15 | 20000.00 | 0.0009 |
| 343.15 | 40000.00 | 0.0010 |
| 343.15 | 60000.00 | 0.0011 |
| 343.15 | 80000.00 | 0.0011 |
| 343.15 | 100000.00 | 0.0012 |
| 353.15 | 20000.00 | 0.0007 |
| 353.15 | 40000.00 | 0.0008 |
| 353.15 | 60000.00 | 0.0009 |
| 353.15 | 80000.00 | 0.0010 |
| 353.15 | 100000.00 | 0.0011 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
| 101.00 | 303.15 | 0.0014 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 100.00 | 964.5 |
| 293.15 | 5000.00 | 967.5 |
| 293.15 | 10000.00 | 970.7 |
| 293.15 | 15000.00 | 973.8 |
| 293.15 | 20000.00 | 976.6 |
| 293.15 | 25000.00 | 979.5 |
| 293.15 | 30000.00 | 982.3 |
| 293.15 | 35000.00 | 985.1 |
| 293.15 | 40000.00 | 987.7 |
| 293.15 | 45000.00 | 990.3 |
| 293.15 | 50000.00 | 992.9 |
| 293.15 | 55000.00 | 995.3 |
| 293.15 | 60000.00 | 997.7 |
| 303.15 | 100.00 | 955.4 |
| 303.15 | 5000.00 | 958.4 |
| 303.15 | 10000.00 | 961.8 |
| 303.15 | 15000.00 | 965.1 |
| 303.15 | 20000.00 | 968.0 |
| 303.15 | 25000.00 | 971.1 |
| 303.15 | 30000.00 | 974.0 |
| 303.15 | 35000.00 | 976.9 |
| 303.15 | 40000.00 | 979.6 |
| 303.15 | 45000.00 | 982.3 |
| 303.15 | 50000.00 | 984.8 |
| 303.15 | 55000.00 | 987.5 |
| 303.15 | 60000.00 | 989.9 |
| 313.15 | 100.00 | 945.9 |
| 313.15 | 5000.00 | 949.3 |
| 313.15 | 10000.00 | 952.7 |
| 313.15 | 15000.00 | 956.3 |
| 313.15 | 20000.00 | 959.5 |
| 313.15 | 25000.00 | 962.5 |
| 313.15 | 30000.00 | 965.6 |
| 313.15 | 35000.00 | 968.5 |
| 313.15 | 40000.00 | 971.5 |
| 313.15 | 45000.00 | 974.4 |
| 313.15 | 50000.00 | 977.0 |
| 313.15 | 55000.00 | 979.5 |
| 313.15 | 60000.00 | 982.2 |
| 323.15 | 100.00 | 936.3 |
| 323.15 | 5000.00 | 940.2 |
| 323.15 | 10000.00 | 943.9 |
| 323.15 | 15000.00 | 947.4 |
| 323.15 | 20000.00 | 950.8 |
| 323.15 | 25000.00 | 954.0 |
| 323.15 | 30000.00 | 957.2 |
| 323.15 | 35000.00 | 960.5 |
| 323.15 | 40000.00 | 963.3 |
| 323.15 | 45000.00 | 966.3 |
| 323.15 | 50000.00 | 969.1 |
| 323.15 | 55000.00 | 971.9 |
| 323.15 | 60000.00 | 974.6 |
| 333.15 | 100.00 | 926.7 |
| 333.15 | 5000.00 | 930.9 |
| 333.15 | 10000.00 | 934.6 |
| 333.15 | 15000.00 | 938.4 |
| 333.15 | 20000.00 | 941.9 |
| 333.15 | 25000.00 | 945.3 |
| 333.15 | 30000.00 | 948.8 |
| 333.15 | 35000.00 | 952.0 |
| 333.15 | 40000.00 | 955.0 |
| 333.15 | 45000.00 | 958.0 |
| 333.15 | 50000.00 | 961.0 |
| 333.15 | 55000.00 | 963.9 |
| 333.15 | 60000.00 | 966.8 |
| 343.15 | 100.00 | 917.1 |
| 343.15 | 5000.00 | 921.2 |
| 343.15 | 10000.00 | 925.3 |
| 343.15 | 15000.00 | 929.3 |
| 343.15 | 20000.00 | 932.9 |
| 343.15 | 25000.00 | 936.9 |
| 343.15 | 30000.00 | 940.2 |
| 343.15 | 35000.00 | 943.6 |
| 343.15 | 40000.00 | 946.8 |
| 343.15 | 45000.00 | 950.0 |
| 343.15 | 50000.00 | 953.1 |
| 343.15 | 55000.00 | 956.2 |
| 343.15 | 60000.00 | 959.0 |
| 353.15 | 100.00 | 907.1 |
| 353.15 | 5000.00 | 911.7 |
| 353.15 | 10000.00 | 916.1 |
| 353.15 | 15000.00 | 920.1 |
| 353.15 | 20000.00 | 924.0 |
| 353.15 | 25000.00 | 927.9 |
| 353.15 | 30000.00 | 931.5 |
| 353.15 | 35000.00 | 934.9 |
| 353.15 | 40000.00 | 938.7 |
| 353.15 | 45000.00 | 941.8 |
| 353.15 | 50000.00 | 945.1 |
| 353.15 | 55000.00 | 948.2 |
| 353.15 | 60000.00 | 951.2 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [300.92; 419.45] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.75122e+01 | |||
| Coefficient B | -4.95806e+03 | |||
| Coefficient C | -1.30710e+01 | |||
| Temperature range, min. | 300.92 | |||
| Temperature range, max. | 419.45 | |||
| Pvap | 1.33 | kPa | 300.92 | Calculated Property |
| Pvap | 2.83 | kPa | 314.09 | Calculated Property |
| Pvap | 5.65 | kPa | 327.26 | Calculated Property |
| Pvap | 10.66 | kPa | 340.43 | Calculated Property |
| Pvap | 19.15 | kPa | 353.60 | Calculated Property |
| Pvap | 32.93 | kPa | 366.77 | Calculated Property |
| Pvap | 54.47 | kPa | 379.94 | Calculated Property |
| Pvap | 87.01 | kPa | 393.11 | Calculated Property |
| Pvap | 134.69 | kPa | 406.28 | Calculated Property |
| Pvap | 202.67 | kPa | 419.45 | Calculated Property |
Similar Compounds
![2-[2-[2-[2-[2-[2-(2-Methoxyethoxy)ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethanol.](data:image/png;base64,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)
![Ethanol, 2-[2-(2-methoxyethoxy)ethoxy]-.](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAPoAAAD6CAIAAAAHjs1qAAAMU0lEQVR4nO3cf0xV9R/H8fflh6KQXBnaZApJooWCFAKWNcls1cZam7JVA5fT0UzFyibNXHcLdS5/7P7hypv7LrH+EefmbtvXDFJMTZzfqSXDyQwzfhimXn8MkMu99/X949wABeEC91y++75fj7+6l8s9n3vv85zz+ZyLWQAIkQ5hIz0AotBh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qSImbm3tcmHH0p2tmRmypIl0txs4raoHwcPyksvSWam5ObKwYMjPZqRFGHic69bJz6fnDwpERGyc6fk58uJE2KxmLhF6u3XX+Xjj+XQIUlJkbo6ee01SUqSZ54Z6WGNDAsAU57Y45Hx4+XaNYmJ8d8za5Z8951kZJiyuUdra2v77bffkpOTJ06cGOJNd6mtrfV6vWlpaSOw7fffl9RUWbXKf3PnTqmpkV27Qj+Qmpoai8Uyc+bM0G+6i2mTmcZGiY/vbl1EZsyQK1fM2twjVFZWTpgw4bnnnktNTf366699Pl+IB3Dr1q01a9ZkZWWlp6dnZ2dfvXo1xAOQK1ckJaX75vTpof8UmpubFyxYkJaWlpOTs2TJkpaWlhAPoBtMcucOxo9/4J4FC3DsmFmb6+XixYuvv/668RrDw8ON/8jJyamurg7NANxu944dO6xWqzEAi8UiItHR0Rs3bmxvbw/NGADgnXewb1/3zX378PbbIdt4e3v7pk2bYmJiRMRisRgfRGxs7Pbt291ud8iG0cWE3I8cwdq1AJCZicpK/52NjUhIwJ07sNtRVgafL/jb/YfL5SopKRk9erSIWK3WzZs33717t7y8PDEx0XjT8/Pzr169at4AAFRUVHSdtRcuXHjhwoXLly8XFhYa0U+ePLmsrMxn5puA69exYgUuX8bu3cjP775/8WLs3o36eqxYgZYWEwcAOJ3O5ORk403Iy8urra2tq6vLz8837klJSSkvLzd1AL0FNff6eixaBBGIoKICp04hMRFr12LDBkybhr170dCAMWMggpwcmHCU9Xq9ZWVlxhw9LCyssLDwr7/+6vppa2urzWaLiooSkbFjx9psNjOOsv1/olVVVbNnzzZ+On/+/HPnzgV9AHC7sWMHrFaIYNEidHZi4ULk5WHjRuTl4ZVX0NmJ/HyIwGrF9u0w4ShbW1v76quvGi/zqaeeOnToUM+fVlRUzJo1q+exIOgDeJQg5d7aCpsNUVEQwdixsNlglHT7Nioq4HSiuRkAfD6UlyMxESKwWJCfjz/+CM4AgKNHjwZSUn19/aJFi4yHTZ069eCBA8EawF2X66OPPoqMjOz/fG3sk48//nif++RwVVRg5kz/EWfhQhgl+Xw4exb79+PsWf95ta7OX7wIUlIQvKPszZs3i4uLjUlLXFyc3W7v7Ozs/bCeM73IyMgPPvjgrssVrDH0Y9i59y54wHnCo/aNoWpoaBjsPKFr3/j3/PnIzcX588MZALxelJW1JiUlJiQEWPBDM64tW7bcv39/WGOoq0Ne3uAKrqjArFkP7xtD1dnZ6XA44uPjRSQiIqKoqOjvv//u/1e69o30iRO9iYmw2+HxDGcMAxpe7mfO4Pnn/e/XnDk4cWIQv/vnnygs9P/u5MlDm9D3np+0tbUF+Lsej+dfDof3iScggvBwvPcerl8f7AAAoKoKGRnGC/nx3XcHNT+5dOlSXl7ecOeyLhdKSjB6NEQQEwObDYHvOW43HA7Ex0MEkZEoKsJAjfap5/zk5ZdfHtT85Pz583VLl/pLmD0bR48OYQABGmLujY2NX6xahYgIiCAhAXv3DnH1eeQI0tONl7pt2bLzAR9lfT7fQ6vPP4Y2L+rZitWKLVsG0UpDAwoLYbEMZ49Fr3VtTU1NgL/o8XgcDsetF1/077FFRUPcY69fR1ERwsMhcuqFF3bt2uUJ+CgbtNWn04nkZH/0eXn4/fchPk+/Bp17R0eH3W5/7LHHROTCggVYvx737g1rCB4PvvrqP/PmhYWFGTOBloGuGJw5c2bevHnGW5yZmXliUGeVPl269MBM4PvvB3h87/lYwGeVPrndbrvd3jWXDWQmUFVVlZGRISLvzJjhy83F8Fe95855c3OzUlNF5Omnn/7hhx/6f/i9e/dsNpsxH4uJibHZbMOdj3V0wG7HuHEQwahRKC7GnTvDesJeBpf7Q5eWfg/eLhjgXLa5ubmoqCgsLExEJk2a5HA4vF5vsMbw8DrPOMq2t+PYMRw4gIsXgX/WKklJZqy2e6/z+jzKDmGtErhAPmJzV9tNTSgqQlgYRDBpEhwOGB/xxYs4cADHjnWv9H78EV2f/rVrgSzAAs2956WlQHb9oek5l50+ffr3PY6yxlll3LhxIjJq1Kji4uI7wd71AcDtht3uv4r35ZdobERKCpYvR2kpsrKwejW8XsyZAxFkZuL48eAPoN+32lirjBkzZghrlcD1PIH3fqurq6tzcnJM/9ruzBnMmwcRZGTA48Hq1cjORmkpli/HtGloaACAuDi0tvofv38/CgoGfNaBcw/wkBNEveey3377rUlnlb61tOCzz9DZiWXLsH27/063G6mpqK7GyZPYs8fUb8oAOJ3OqVOndr3k06dPl5eXJyUlDXetErCmpqauE2lCQoLD4Th79mxIvynz+VBWhhMncPo0UlPRdUFz61YsXQqYkHtHR8eUKVOMCeWaNWtu3bo1jOEPQkdHx7Zt22JjY43TpfGpp6en//TTT6EZgN+TTz4wVykpwRdfhGzjbW1tpaWl0dHR0kNWVtYvv/wSsjGcOnUqOzu75wCio6M///xzM84qj7R1Kz75pPtmfT2SkwEgLg5OJw4fxuHD2LAhOEf3zZs3D/bSUrDcuHFj1apV0dHR4eHh69at6/MLC3NNmPDAhblNm/DppyEeQlNT07PPPmucWoO8VgmMcRHMuKCekpJi9lmlDxs2oLS0++aNG4iPB4C4OKxdi5ISlJTgzTeDk3vo39+H3L59O6THkp7mzn3gy4SCAuzZMyIDcblcIf3Dsl7a29tdIfnisw/ffPNAysePY+5cYCiTmYH/ALhrLjFSYmNjjcXZCFi5Utavl5s3RUQqK+X4cfnnDxBCzGq1Gt+mjZSoqCjjOukIWLxYfv5ZKitFRG7elPXrZeXKoT2Tmf+a6f9AQYG4XPLGG3L/vkyZIk7nA3/BT6EREyNOp9hsUlIiUVHy1ltSUCAikpYmXcdiq1WSkgZ8JtP+NRPR/x7+nwhIEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOijB3UoS5kyLMnRRh7qQIcydFmDspwtxJEeZOivwXOGiJ/kNK0vYAAAAASUVORK5CYII=)
![2-[2-[2-[2-[2-[2-[2-[2-(2-Methoxyethoxy)ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethanol.](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAPoAAAD6CAIAAAAHjs1qAAAMhElEQVR4nO3ae0zV9R/H8TcKiKKIgDIOt2xolrV5yaPmBVNcGoflUKRWB2c6KBQsBZmhnuOchmXbYas5ysmONicYJIFpRf0qB15+2s/wmoqZCKnIRQ8XOXh4//74Ho8HPRwOzaLt/Xr8xdz7fM77i0/O+crRjZkJQIY+vb0AwD8HuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRDkDoIgdxAEuYMgyB0EQe4gCHIHQZA7CILcQRD3v/Kg4mKqrKR58+iJJx7zOn8BMxUV0R9/UGwshYb29jZEzFRQQDU1tGABqVS9vQ1RRwft3Us3b9LChRQY2NvbEFkslJdH9fUUH09Dh/7DT97zV/fcXDKbackS0uuppcWVR5hMpubmZmZ28RlMJlNTU5Or89u2kYcHLV5MmZnU1vb4z+/pvMFAvr6UkEAZGXTvnuvnu7iMMm8ymVyd/uADUqno9dcpLY06Oh7/+T2d37SJIiLo1Vdp1aq/5Xynep770aM0fz4NGkRTptD5885n29vbs7Ozw8LC4uLi1Gp1WVmZ83mz2ZydnR0eHr5w4UK1Wl1eXt79PhUVFB1NPj70/PNUWel8trW1dcuWLWFhYbGxsRMnTjx8+LCL8/PmzZs0adKRI0e63+fCBYqKIl9fevZZqqpyPtvS0qLX60NDQ2NiYmbMmHHy5EkX5zUazYsvvvjrr792v8+VKzRtGvn5UUQE3bjhfLa5uVmv14eHh0dHR8+aNauioqJH86dOnep+n5oaUqspIIBUKmpsdD7b1NSk1+uHDx8+e/bs2bNnnzlzpvvznWPX7dvHWi1nZvKffzIzr13LBw7wG2/wtWsOxwsLC5988knlWXx8fIjIzc2tJD2dq6sdzt8rLBz99NPK/KBBg4ioT58+ixYtqqmpcbzP3r385pucns63bjEzr17N+/fz4sXcxXxeXl54ePhD55e+9x5fv+5guqOjLS9vRESEsvbAgQOV+aVLl17vYp537+akJH73Xb59m5l5xQouLubERL5xw9F4x+effx4SEqKc7+3tTUR9+/b9ed06vnnT4fktu3c/ER7+0Pzbb79dW1vreB+jkVNSOCWFm5qYmZOTuaiIk5Ot367OLBZLbm5uUFCQcpnK+e7u7kc2bOC6OgfnWyx3jMbg4GBlfsCAAcp8ampqfX29w3n+7DNetYqTk/nuXWbmxET+4gtesYIdzVsslk8//XTYsGH253t4ePxv0yZuaHBwvmtcyr3hzBmOimIiJuKdO3n1at6wgXNyeNYsJmJv7+b3329pabHNnzt3bs6cOUpYo0aN+vrrr5ubm3U63fCAAEtgIA8YwDodt7Y+eIKzZ3nOHCbSRUaOGjXqwIEDTU1NOp3Oy8uLiLy9vXU6XavdfENFBUdGWvfZs4dXr2a9nnNzecoUJuJBg5o++uiu8j1lZuZffvll+vTpyj5jxoz56aeflPNHBQZa/PzY2/vhfU6c4GnTmCgjMnLs2LG2+X79+tn2sT+/4cQJ61MTcUGBdZ9du3jcOCbiwYPvZGe3tbXZ5o8fPz516lRln3Hjxh06dKihoSEjI2OMStXh48O+vpyVxXbn8/HjyvkrIiPHjx9vm/f09CQiX1/frKws+/Mbjx1jtdq6T1ERp6ezTsd79vDo0UzEfn63t21rb2+3zR87dmzy5MnKPhMmTCgrK6uvr09NTZ0YEsLe3jxkCGdlsd35fOwYT57MRInTpk2YMKG8vLyuri41NdXd3Z2IhgwZYjAY7M9vLC+3fivc3Hj/fk5L4/XruaCAIyKYiAMCGrdvv3fvnm3+yJEjEydOVPZRq9WHDx9Wzp8RHs5eXuznxwYD2827rpvclcsOGDiwPTTUwWVXVbFWy25ua2bMCAkJMRqNt27dsl22n5/fQ5fdcvkyz5/fKVP7H5uAgLs5OfaXffXqVa1Wq1x2aGio0WhULnvYwIHtKpWDy750iePimOidyEhlXtmnb9++ROTv728wGOzPb7l4kWNiHmSans56Pe/YwS+8wEQcGNi6Y4fFYrHNX7hwIS4uTtknIiIiPz+/trY2NTU1ZPBgy7Bh7O//8D4XLij7vDV9+ogRI/Lz82tqahITE5V9goKCcjpfb8v588qPPbu5Pch0504eP56JOCioddcu+31+++236OhoZZ+RI0cWFxdXV1cnJiaO8Pfv8PNjlYpzcthuns+f55dfZqJFU6c+9dRTJSUl1dXVWq3Wzc2NiFQqVU5Ojv35LadPW/9q+vTh4mJOS+v0YxMS0rJnT0dHh23+3Llzc+fOtX+Zu3btmlarHT10aIePDwcHs9HIdvO2l7n4yZOVl7mqqirbPkpR9ue3njxpfZlzd7f+2Kxbx4WFvHmzdcL2RRec5W4ymZR3E3d39690OsdvasyWH3+cpFYrF2l7U0tJSanrYp5/+IHfeYczMlh5F16zhr//vqs3NWYuLS197rnnlPP79++vvKkd3Lixqzc183ffjR0zRplX3h88PT1XrlzZ2NjoeJ9vvuH0dF65kpWBVau4tJTT0qz3JI84ePDg0/dvupTXe09Pz/9kZXU1f/fgwdHPPGM/369fv4yMjDt37jjep6SEMzMf3ISkpPC33/KaNWwyORwvLi4eOXKk/fleXl5lH35offgjmkpKbPPK+0P//v3Xrl3b1MU8f/kl63S8bJn1DTApiQ8c4PXrubnZ4bj9TayHh4dSxX8Nhq7mG/fte3R+w4YN9vcLneTn86ZNnJTEZjMz89KlnJzMZjObzbx8ueOH3NfNq/vy5ctnzpxZUVHhfMxisRiNRpVKFR8fr/wTx/k8M/Nbb1m/+OQTdu384ODgBQsWREVFnT592sX52NhYV+aZmZOSrF9s3coXLzqfbW9vz8nJCQ0NfeWVV6Kios6ePevifExMjEajuXTpUg/22biRq6qcz5rNZoPBEBQUNHfuXI1GU1lZ6cp8cHDwSy+9pNFoLl++3P0+tr+vzEyHd/+Pnh8SEjJz5kyNRvP77787n29razMYDGFhYcr8lStXut/H9v1ZuZKXLOEtW3jLFtZqnT+om9zt7wi71dbW1oP57du5oIBv3+aEhE73qY/r/J7Of/wx79/PDQ2ckMB2N2C9ts/WrVxaynV1nJDQ6Yakt/bZvJkPHeLaWk5I+FvO7+m8TsdHj/L167x4MS9bZv3D7l7d3djlXz8/fiUlVFn5L/p4qKiIrl79t3w8xEyFhVRT82/5eEj5uOrWLYqPp4CA3t7m/sdVjY302mt06hQpv4r4+We6/zsJh3o1d4B/Fv7PDAiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIMj/AeC7THTwfpuPAAAAAElFTkSuQmCC)
![2-[2-[2-[2-[2-[2-[2-[2-[2-[2-(2-Methoxyethoxy)ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethanol.](data:image/png;base64,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![2-[2-[2-[2-[2-[2-[2-(2-Methoxyethoxy)ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethanol.](data:image/png;base64,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)
![2-[2-[2-[2-[2-[2-[2-[2-[2-(2-Methoxyethoxy)ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethanol.](data:image/png;base64,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)
Find more compounds similar to Ethanol, 2-methoxy-.
Mixtures
- Propylamine + Ethanol, 2-methoxy-
- Ethanol, 2-methoxy- + 1-Butanol, 3-methyl-
- Diisopropyl ether + Ethanol, 2-methoxy-
- Isopropyl Alcohol + Ethanol, 2-methoxy-
- Diisopropyl ether + Isopropyl Alcohol + Ethanol, 2-methoxy-
- Ethanol, 2-methoxy- + 2-Pyrrolidinone, 1-methyl-
- Toluene + Ethanol, 2-methoxy-
- Ethanol, 2-methoxy- + Dimethyl Sulfoxide
- Toluene + Ethanol, 2-methoxy- + Dimethyl Sulfoxide
- Ethanol, 2-methoxy- + Cyclohexane, methyl-
- Benzene + Hexadecane + Ethanol, 2-methoxy-
- Toluene + Hexadecane + Ethanol, 2-methoxy-
- p-Xylene + Hexadecane + Ethanol, 2-methoxy-
- Benzene + Ethanol, 2-methoxy-
- p-Xylene + Ethanol, 2-methoxy-
- Ethanol, 2-methoxy- + Water
- Ethanol, 2-methoxy- + Propane, 2-ethoxy-2-methyl-
- 1-Propanol + Ethanol, 2-methoxy-
- Propylene Glycol + Ethanol, 2-methoxy-
- Ethanol, 2-methoxy- + Formamide
Find more mixtures with Ethanol, 2-methoxy-.
Sources
- Crippen Method
- Crippen Method
- Speeds of Sound and Isentropic Compressibilities of n-Alkoxyethanols and Polyethers with Propylamine at 298.15K
- Densities, Viscosities, Sound Speeds, Refractive Indices, and Excess Properties of Binary Mixtures of Isoamyl Alcohol with Some Alkoxyethanols
- Influence of the molecular structure on the viscosity of some alkoxyethanols
- Effect of pressure and the capability of 2-methoxyethanol as a solvent in the behaviour of a diisopropyl ether isopropyl alcohol azeotropic mixture
- Densities, speeds of sound and 1H NMR spectroscopic studies for binary mixtures of 1-hexyl-3-methylimidazolium based ionic liquids with ethylene glycol monomethyl ether at temperature from T = (288.15 318.15) K
- Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
- Isobaric vapor-liquid equilibrium for binary and ternary systems with toluene, 2-methoxyethanol and dimethyl sulfoxide at 101.3 kPa
- Isobaric vapor-liquid equilibrium data for methylcyclohexane + 2-methoxyethanol and methylcyclohexane + 2-ethoxyethanol at 50.00 and 101.33 kPa
- Liquid liquid equilibria in the ternary systems {hexadecane + BTX aromatics + 2-methoxyethanol or acetonitrile} at 298.15 K
- Surface tension of four oxygenated fuels: experiment and correlation
- Viscosity of aqueous solutions of 2-methoxyethanol, 2-ethoxyethanol, and ethanolamine
- Volumetric properties of binary mixtures of alkoxyethanols with ethyl tert-butyl ether at various temperatures
- Excess molar enthalpies and volumes of binary mixtures of nonafluorobutylmethylether with ethylene glycol ethers at T = 298.15 K
- Densities and derived thermodynamic properties of (2-methoxyethanol + 1-propanol, or 2-propanol, or 1,2-propandiol) at temperatures from T = (293.15 to 343.15) K
- Non-ideal behaviour of a room temperature ionic liquid in an alkoxyethanol or poly ethers at T = (298.15 to 318.15) K
- Physical and excess properties of a room temperature ionic liquid (1-methyl-3-octylimidazolium tetrafluoroborate) with n-alkoxyethanols (C1Em, m = 1 to 3) at T = (298.15 to 318.15) K
- Thermodynamic and optical studies of some ethylene glycol ethers in aqueous solutions at T = 298.15 K
- Investigation of sodium 4-nitrotoluene-2-sulfonate solubility in aqueous organic solutions
- Volumes, heat capacities, and compressibilities of the mixtures of acetonitrile and 2-methoxyethanol
- Volumetric and viscometric study of aqueous binary mixtures of some glycol ethers at T = (275.15 and 283.15) K
- Acoustic, volumetric, and spectroscopic studies of formamide with 2-alkoxyethanols at different temperatures
- Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
- Thermophysical properties of ionic liquid {1-butyl-3-methylimidazolium bromide [bmim][Br] in alkoxyalkanols + water} mixtures at different temperatures
- Thermodynamics of solvation in propylene glycol and methyl cellosolve
- Isobaric (vapor + liquid) equilibria for the binary systems (1-methoxy-2- propanol + 2-methoxyethanol), (2-butanone + 2-methoxyethanol) and (water + 2-methoxyethanol) at pressures of (74.5, 101.3, and 134.0) kPa
- FT-IR spectroscopic study of excess thermodynamic properties of liquid mixtures containing benzylalcohol with alkoxyalkanols
- Study of molecular interactions of binary mixtures DEC with alkoxyalkanols at various temperatures
- Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
- Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
- Intermolecular interactions in Formamide +2-Alkoxyethanols: Viscometric study
- Densities, speed of sound, and IR studies of Ethyl lactate with 2-alkoxyethanols at different temperatures
- Study of molecular interactions in binary liquid mixtures of [Emim][BF4] with 2-methoxyethanol using thermo acoustic, volumetric and optical properties
- Modified Method for Measuring the Solubility of Pharmaceutical Compounds in Organic Solvents by Visual Camera
- Isobaric Vapor Liquid Equilibrium for the Binary Systems of sec-Butyl Acetate + Methyl Ethyl Ketone, 2-Methoxyethanol, or 1,2-Dimethoxyethane at 101.3 kPa
- Isobaric Vapor Liquid Equilibria for (Water + 1-Methoxy-2-propanol), (Water + 2-Methoxy-1-propanol), and (1-Methoxy-2-propanol + 2-Methoxy-1-propanol) at 101.3 kPa
- Solubilities of 4',5,7-Triacetoxyflavanone in Fourteen Organic Solvents at Different Temperatures
- Measurements and Thermodynamic Models for the Separation of 2-Methoxyethanol and Water Azeotropic Mixtures via Different Solvents
- Density and Speed of Sound of the Binary Mixture of 1-Butyl-3-Methylimidazolium Bis(trifluoromethylsulfonyl)imide + 2-Methoxyethanol from T = (298.15 to 323.15) K at Atmospheric Pressure
- Isobaric Vapor-Liquid Equilibrium for Binary and Ternary Systems of 2-Methoxyethanol, Ethylbenzene, and Dimethyl Sulfoxide at 100.00 kPa
- Solid-Liquid Equilibrium of Rebaudioside A in Pure and Binary Mixed Solvents at T = (288.15 to 328.15) K
- Solubility of 4-Chloro-2,5-dimethoxynitrobenzene, 4-Chloro-2,5-dimethoxyaniline, and 2,5-Dimethoxyaniline in Binary and Pure Solvents: Determination and Modeling
- Solid-Liquid Equilibrium Solubility, Thermodynamic Properties, and Molecular Simulation of Phenylphosphonic Acid in 15 Pure Solvents at Different Temperatures
- Density, Viscosity, and Excess Properties of Binary Mixtures of 2-(Methylamino)ethanol with 2-Methoxyethanol, 2-Ethoxyethanol, and 2-Butoxyethanol from 293.15 to 353.15 K
- Solubility Determination and Modeling of EGCG Peracetate in 12 Pure Solvents at Temperatures from 278.15 to 318.15 K
- Relative Permittivity, Viscosity, and Speed of Sound for 2-Methoxyethanol + Butylamine Mixtures
- Experimental Surface Tensions and Derived Surface Properties of Binary Mixtures of Water + Alkoxyethanols (C1Em, m = 1, 2, 3) and Water + Ethylene Glycol Dimethyl Ether (C1E1C1) at (298.15, 308.15, and 318.15) K
- 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
- Density and Relative Permittivity of 2-Methoxyethanol + Dipropylamine Mixtures at Various Temperatures
- High-Pressure Volumetric Properties of Three Monoethylene Glycol Alkyl Ethers
- Excess Molar Volumes and Surface Tensions of Trimethylbenzene + Ethylene Glycol Ester at 298.15 K and 313.15 K
- Density, Viscosity, and Speed of Sound of (1-Octanol + 2-Methoxyethanol), (1-Octanol + N,N-Dimethylacetamide), and (1-Octanol + Acetophenone) at Temperatures of (298.15, 308.15, and 318.15) K
- Excess Gibbs Energies of the Ternary System 2-Methoxyethanol + Tetrahydrofuran + Cyclohexane and Other Relevant Binaries at 298.15 K
- Solubility of CO2 in Alcohols, Glycols, Ethers, and Ketones at High Pressures from (288.15 to 318.15) K
- Volumetric and Acoustic Properties of Binary Mixtures of the Ionic Liquid 1-Butyl-3-methylimidazolium Tetrafluoroborate [bmim][BF4] with Alkoxyalkanols at Different Temperatures
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Evaluation of the 2-Methoxyethanol as Entrainer in Ethanol Water and 1-Propanol Water Mixtures
- Viscosity, Density, and Speed of Sound for the Binary Mixtures of Formamide with 2-Methoxyethanol, Acetophenone, Acetonitrile, 1,2-Dimethoxyethane, and Dimethylsulfoxide at Different Temperatures
- Density, Viscosity, Refractive Index, and Ultrasonic Speed of Binary Mixtures of 1,3-Dioxolane with 2-Methoxyethanol, 2-Ethoxyethanol, 2-Butoxyethanol, 2-Propylamine, and Cyclohexylamine
- Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures with Cyclohexane, Cyclohexene, and 2-Methoxyethanol at 100 kPa
- Volumetric and Viscometric Properties of Binary Liquid Mixtures of Ethylene Glycol Monomethyl Ether + 1-Hexanol, 1-Octanol, and 1-Decanol at Temperatures of T = (293.15, 298.15, 303.15, and 308.15) K
- Ion-Solvent Interactions of Some Halides of Common Cations with Organic Solvent Mixtures by Conductometric, Volumetric, Viscometric, and Refractometric Techniques
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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