- InChI
- InChI=1S/C10H22O5/c1-11-3-5-13-7-9-15-10-8-14-6-4-12-2/h3-10H2,1-2H3
- InChI Key
- ZUHZGEOKBKGPSW-UHFFFAOYSA-N
- Formula
- C10H22O5
- SMILES
- COCCOCCOCCOCCOC
- Molecular Weight1
- 222.28
- CAS
- 143-24-8
- Other Names
-
- 2,5,8,11,14-Pentaoxapentadecane
- Ansul Ether 181AT
- Bis[2-(2-methoxyethoxy)ethyl] ether
- CH3O[CH2CH2O]4CH3
- Dimethoxytetraethylene glycol
- Dimethoxytetraglycol
- E 181 (ether)
- Ether, bis[2-(2-methoxyethoxy)ethyl]
- Glyme-5
- NSC 65624
- Nissan Uniox MM 200
- Tetraethylene glycol dimethyl ether
- bis(2-(2-methoxyethoxy)ethyl) ether
- tetraethylene glycol, dimethyl ether
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (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).
- 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).
- 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.
- ρl : Liquid Density (kg/m3).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λ : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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.
Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| PAff | 953.80 | kJ/mol | NIST |
| BasG | 897.80 | kJ/mol | NIST |
| ΔfG° | -491.68 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -910.83 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 27.60 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 76.90 ± 2.60 | kJ/mol | NIST |
| log10WS | 0.56 | Crippen Calculated Property | |
| logPoct/wat | 0.329 | Crippen Calculated Property | |
| McVol | 181.110 | ml/mol | McGowan Calculated Property |
| Pc | 1952.68 | kPa | Joback Calculated Property |
| Tboil | [548.15; 549.00] | K |
|
| Tboil | 549.00 | K | NIST |
| Tboil | 548.15 | K | NIST |
| Tc | 702.78 | K | Joback Calculated Property |
| Tfus | 243.45 | K | NIST |
| Vc | 0.685 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [449.87; 529.06] | J/mol×K | [540.30; 702.78] |
|
| Cp,gas | 449.87 | J/mol×K | 540.30 | Joback Calculated Property |
| Cp,gas | 464.04 | J/mol×K | 567.38 | Joback Calculated Property |
| Cp,gas | 477.85 | J/mol×K | 594.46 | Joback Calculated Property |
| Cp,gas | 491.28 | J/mol×K | 621.54 | Joback Calculated Property |
| Cp,gas | 504.30 | J/mol×K | 648.62 | Joback Calculated Property |
| Cp,gas | 516.90 | J/mol×K | 675.70 | Joback Calculated Property |
| Cp,gas | 529.06 | J/mol×K | 702.78 | Joback Calculated Property |
| Cp,liquid | 457.10 | J/mol×K | 298.15 | NIST |
| η | [0.0011000; 0.0069800] | Pa×s | [273.15; 363.15] |
|
| η | 0.0069800 | Pa×s | 273.15 | Density... |
| η | 0.0059100 | Pa×s | 278.15 | Density... |
| η | 0.0050600 | Pa×s | 283.15 | Density... |
| η | 0.0043700 | Pa×s | 288.15 | Density... |
| η | 0.0038400 | Pa×s | 293.15 | Density... |
| η | 0.0034000 | Pa×s | 298.15 | Density... |
| η | 0.0033800 | Pa×s | 298.15 | Densiti... |
| η | 0.0029900 | Pa×s | 303.15 | Density... |
| η | 0.0024200 | Pa×s | 313.15 | Densiti... |
| η | 0.0024500 | Pa×s | 313.15 | Density... |
| η | 0.0020200 | Pa×s | 323.15 | Density... |
| η | 0.0020040 | Pa×s | 323.15 | Densiti... |
| η | 0.0017000 | Pa×s | 333.15 | Density... |
| η | 0.0016900 | Pa×s | 333.15 | Densiti... |
| η | 0.0014500 | Pa×s | 343.15 | Density... |
| η | 0.0014200 | Pa×s | 343.15 | Densiti... |
| η | 0.0012600 | Pa×s | 353.15 | Density... |
| η | 0.0011000 | Pa×s | 363.15 | Density... |
| ΔvapH | 58.00 | kJ/mol | 486.00 | NIST |
| n0 | [1.42210; 1.43440] | [288.15; 318.15] |
|
|
| n0 | 1.43440 | 288.15 | Liquid ... | |
| n0 | 1.43030 | 298.15 | Liquid ... | |
| n0 | 1.42620 | 308.15 | Liquid ... | |
| n0 | 1.42210 | 318.15 | Liquid ... | |
| ρl | [938.90; 1020.70] | kg/m3 | [283.15; 373.15] |
|
| ρl | 1020.30 | kg/m3 | 283.15 | The Vis... |
| ρl | 1020.70 | kg/m3 | 283.15 | Thermop... |
| ρl | 1015.63 | kg/m3 | 288.15 | Volumet... |
| ρl | 1016.70 | kg/m3 | 288.15 | Volumet... |
| ρl | 1017.00 | kg/m3 | 288.15 | Thermop... |
| ρl | 1016.10 | kg/m3 | 288.15 | Thermop... |
| ρl | 1015.63 | kg/m3 | 288.15 | Volumet... |
| ρl | 1015.63 | kg/m3 | 288.15 | Volumet... |
| ρl | 1015.60 | kg/m3 | 288.15 | The Vis... |
| ρl | 1011.00 | kg/m3 | 293.15 | Volumet... |
| ρl | 1012.30 | kg/m3 | 293.15 | Thermop... |
| ρl | 1012.06 | kg/m3 | 293.15 | Volumet... |
| ρl | 1011.00 | kg/m3 | 293.15 | Volumet... |
| ρl | 1011.00 | kg/m3 | 293.15 | Volumet... |
| ρl | 1011.50 | kg/m3 | 293.15 | Thermop... |
| ρl | 1011.00 | kg/m3 | 293.15 | The Vis... |
| ρl | 1009.20 | kg/m3 | 295.15 | The Vis... |
| ρl | 1007.12 | kg/m3 | 298.15 | Thermod... |
| ρl | 1006.40 | kg/m3 | 298.15 | The Vis... |
| ρl | 1007.42 | kg/m3 | 298.15 | Volumet... |
| ρl | 1006.36 | kg/m3 | 298.15 | Volumet... |
| ρl | 1006.36 | kg/m3 | 298.15 | Volumet... |
| ρl | 1006.20 | kg/m3 | 298.15 | Liquid-... |
| ρl | 1006.36 | kg/m3 | 298.15 | Volumet... |
| ρl | 1007.60 | kg/m3 | 298.15 | Thermop... |
| ρl | 1006.80 | kg/m3 | 298.15 | Thermop... |
| ρl | 1002.20 | kg/m3 | 303.15 | Thermop... |
| ρl | 1001.73 | kg/m3 | 303.15 | Volumet... |
| ρl | 1001.73 | kg/m3 | 303.15 | Volumet... |
| ρl | 1001.73 | kg/m3 | 303.15 | Volumet... |
| ρl | 1002.79 | kg/m3 | 303.15 | Volumet... |
| ρl | 1003.10 | kg/m3 | 303.15 | Thermop... |
| ρl | 1001.80 | kg/m3 | 303.15 | The Vis... |
| ρl | 998.15 | kg/m3 | 308.15 | Volumet... |
| ρl | 997.10 | kg/m3 | 308.15 | Volumet... |
| ρl | 998.80 | kg/m3 | 308.15 | Thermop... |
| ρl | 997.10 | kg/m3 | 308.15 | Volumet... |
| ρl | 997.20 | kg/m3 | 308.15 | The Vis... |
| ρl | 997.10 | kg/m3 | 308.15 | Volumet... |
| ρl | 997.60 | kg/m3 | 308.15 | Thermop... |
| ρl | 992.48 | kg/m3 | 313.15 | Volumet... |
| ρl | 994.10 | kg/m3 | 313.15 | Thermop... |
| ρl | 992.48 | kg/m3 | 313.15 | Volumet... |
| ρl | 992.48 | kg/m3 | 313.15 | Volumet... |
| ρl | 993.52 | kg/m3 | 313.15 | Volumet... |
| ρl | 993.00 | kg/m3 | 313.15 | Thermop... |
| ρl | 992.60 | kg/m3 | 313.15 | The Vis... |
| ρl | 987.86 | kg/m3 | 318.15 | Volumet... |
| ρl | 988.00 | kg/m3 | 318.15 | The Vis... |
| ρl | 987.86 | kg/m3 | 318.15 | Volumet... |
| ρl | 987.86 | kg/m3 | 318.15 | Volumet... |
| ρl | 989.50 | kg/m3 | 318.15 | Thermop... |
| ρl | 988.89 | kg/m3 | 318.15 | Volumet... |
| ρl | 983.70 | kg/m3 | 323.15 | Thermop... |
| ρl | 983.23 | kg/m3 | 323.15 | Volumet... |
| ρl | 983.23 | kg/m3 | 323.15 | Volumet... |
| ρl | 983.23 | kg/m3 | 323.15 | Volumet... |
| ρl | 984.90 | kg/m3 | 323.15 | Thermop... |
| ρl | 983.40 | kg/m3 | 323.15 | The Vis... |
| ρl | 984.26 | kg/m3 | 323.15 | Volumet... |
| ρl | 978.61 | kg/m3 | 328.15 | Volumet... |
| ρl | 980.20 | kg/m3 | 328.15 | Thermop... |
| ρl | 978.61 | kg/m3 | 328.15 | Volumet... |
| ρl | 978.80 | kg/m3 | 328.15 | The Vis... |
| ρl | 974.50 | kg/m3 | 333.15 | Thermop... |
| ρl | 975.60 | kg/m3 | 333.15 | Thermop... |
| ρl | 973.99 | kg/m3 | 333.15 | Volumet... |
| ρl | 974.20 | kg/m3 | 333.15 | The Vis... |
| ρl | 973.99 | kg/m3 | 333.15 | Volumet... |
| ρl | 969.60 | kg/m3 | 338.15 | The Vis... |
| ρl | 971.00 | kg/m3 | 338.15 | Thermop... |
| ρl | 965.00 | kg/m3 | 343.15 | The Vis... |
| ρl | 965.30 | kg/m3 | 343.15 | Thermop... |
| ρl | 966.50 | kg/m3 | 343.15 | Thermop... |
| ρl | 961.90 | kg/m3 | 348.15 | Thermop... |
| ρl | 960.40 | kg/m3 | 348.15 | The Vis... |
| ρl | 957.30 | kg/m3 | 353.15 | Thermop... |
| ρl | 955.80 | kg/m3 | 353.15 | The Vis... |
| ρl | 952.70 | kg/m3 | 358.15 | Thermop... |
| ρl | 948.10 | kg/m3 | 363.15 | Thermop... |
| ρl | 943.50 | kg/m3 | 368.15 | Thermop... |
| ρl | 938.90 | kg/m3 | 373.15 | Thermop... |
| γ | [0.03; 0.03] | N/m | [298.15; 318.15] |
|
| γ | 0.03 | N/m | 298.15 | Volumet... |
| γ | 0.03 | N/m | 308.15 | Volumet... |
| γ | 0.03 | N/m | 318.15 | Volumet... |
| λ | [0.13; 0.15] | W/m×K | [302.75; 392.16] |
|
| λ | 0.15 | W/m×K | 302.75 | Thermal... |
| λ | 0.14 | W/m×K | 332.54 | Thermal... |
| λ | 0.13 | W/m×K | 362.39 | Thermal... |
| λ | 0.13 | W/m×K | 392.16 | Thermal... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 100.00 | 278.15 | 1025.1 |
| 100.00 | 283.15 | 1020.4 |
| 100.00 | 293.15 | 1011.1 |
| 100.00 | 303.15 | 1002.1 |
| 100.00 | 313.15 | 992.9 |
| 100.00 | 323.15 | 983.6 |
| 100.00 | 333.15 | 974.1 |
| 100.00 | 343.15 | 965.0 |
| 100.00 | 353.15 | 955.7 |
| 1000.00 | 278.15 | 1025.6 |
| 1000.00 | 283.15 | 1020.9 |
| 1000.00 | 293.15 | 1011.6 |
| 1000.00 | 303.15 | 1002.7 |
| 1000.00 | 313.15 | 993.5 |
| 1000.00 | 323.15 | 984.3 |
| 1000.00 | 333.15 | 974.8 |
| 1000.00 | 343.15 | 965.8 |
| 1000.00 | 353.15 | 956.5 |
| 2500.00 | 278.15 | 1026.5 |
| 2500.00 | 283.15 | 1021.8 |
| 2500.00 | 293.15 | 1012.6 |
| 2500.00 | 303.15 | 1003.7 |
| 2500.00 | 313.15 | 994.6 |
| 2500.00 | 323.15 | 985.3 |
| 2500.00 | 333.15 | 976.0 |
| 2500.00 | 343.15 | 967.0 |
| 2500.00 | 353.15 | 957.8 |
| 5000.00 | 278.15 | 1027.9 |
| 5000.00 | 283.15 | 1023.3 |
| 5000.00 | 293.15 | 1014.1 |
| 5000.00 | 303.15 | 1005.3 |
| 5000.00 | 313.15 | 996.3 |
| 5000.00 | 323.15 | 987.1 |
| 5000.00 | 333.15 | 977.9 |
| 5000.00 | 343.15 | 969.0 |
| 5000.00 | 353.15 | 959.9 |
| 7500.00 | 278.15 | 1029.3 |
| 7500.00 | 283.15 | 1024.7 |
| 7500.00 | 293.15 | 1015.6 |
| 7500.00 | 303.15 | 1006.9 |
| 7500.00 | 313.15 | 997.9 |
| 7500.00 | 323.15 | 988.9 |
| 7500.00 | 333.15 | 979.8 |
| 7500.00 | 343.15 | 971.0 |
| 7500.00 | 353.15 | 962.0 |
| 10000.00 | 278.15 | 1030.7 |
| 10000.00 | 283.15 | 1026.1 |
| 10000.00 | 293.15 | 1017.1 |
| 10000.00 | 303.15 | 1008.5 |
| 10000.00 | 313.15 | 999.6 |
| 10000.00 | 323.15 | 990.6 |
| 10000.00 | 333.15 | 981.6 |
| 10000.00 | 343.15 | 972.9 |
| 10000.00 | 353.15 | 964.0 |
| 15000.00 | 278.15 | 1033.4 |
| 15000.00 | 283.15 | 1028.9 |
| 15000.00 | 293.15 | 1020.0 |
| 15000.00 | 303.15 | 1011.5 |
| 15000.00 | 313.15 | 1002.8 |
| 15000.00 | 323.15 | 994.0 |
| 15000.00 | 333.15 | 985.1 |
| 15000.00 | 343.15 | 976.6 |
| 15000.00 | 353.15 | 967.9 |
| 20000.00 | 278.15 | 1036.1 |
| 20000.00 | 283.15 | 1031.6 |
| 20000.00 | 293.15 | 1022.9 |
| 20000.00 | 303.15 | 1014.5 |
| 20000.00 | 313.15 | 1006.0 |
| 20000.00 | 323.15 | 997.3 |
| 20000.00 | 333.15 | 988.5 |
| 20000.00 | 343.15 | 980.2 |
| 20000.00 | 353.15 | 971.7 |
| 25000.00 | 278.15 | 1038.7 |
| 25000.00 | 283.15 | 1034.3 |
| 25000.00 | 293.15 | 1025.6 |
| 25000.00 | 303.15 | 1017.4 |
| 25000.00 | 313.15 | 1009.0 |
| 25000.00 | 323.15 | 1000.5 |
| 25000.00 | 333.15 | 991.8 |
| 25000.00 | 343.15 | 983.7 |
| 25000.00 | 353.15 | 975.3 |
| Reference | ||
Speed of sound, m/s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Speed of sound, m/s - Liquid |
| 293.15 | 100.00 | 1400.2 |
| 293.15 | 10000.00 | 1439.3 |
| 293.15 | 20000.00 | 1477.3 |
| 293.15 | 30000.00 | 1512.3 |
| 293.15 | 40000.00 | 1546.2 |
| 293.15 | 50000.00 | 1578.2 |
| 293.15 | 60000.00 | 1609.1 |
| 293.15 | 70000.00 | 1638.4 |
| 293.15 | 80000.00 | 1666.8 |
| 293.15 | 90000.00 | 1694.2 |
| 293.15 | 100000.00 | 1720.6 |
| 303.15 | 100.00 | 1361.6 |
| 303.15 | 10000.00 | 1402.8 |
| 303.15 | 20000.00 | 1441.7 |
| 303.15 | 30000.00 | 1478.2 |
| 303.15 | 40000.00 | 1513.0 |
| 303.15 | 50000.00 | 1546.1 |
| 303.15 | 60000.00 | 1577.7 |
| 303.15 | 70000.00 | 1607.6 |
| 303.15 | 80000.00 | 1637.0 |
| 303.15 | 90000.00 | 1664.9 |
| 303.15 | 100000.00 | 1692.0 |
| 313.15 | 100.00 | 1324.5 |
| 313.15 | 10000.00 | 1367.0 |
| 313.15 | 20000.00 | 1407.3 |
| 313.15 | 30000.00 | 1444.9 |
| 313.15 | 40000.00 | 1480.9 |
| 313.15 | 50000.00 | 1514.8 |
| 313.15 | 60000.00 | 1547.2 |
| 313.15 | 70000.00 | 1578.1 |
| 313.15 | 80000.00 | 1607.8 |
| 313.15 | 90000.00 | 1636.4 |
| 313.15 | 100000.00 | 1663.9 |
| 323.15 | 100.00 | 1288.0 |
| 323.15 | 10000.00 | 1332.1 |
| 323.15 | 20000.00 | 1373.8 |
| 323.15 | 30000.00 | 1412.5 |
| 323.15 | 40000.00 | 1449.5 |
| 323.15 | 50000.00 | 1484.2 |
| 323.15 | 60000.00 | 1517.4 |
| 323.15 | 70000.00 | 1548.8 |
| 323.15 | 80000.00 | 1579.3 |
| 323.15 | 90000.00 | 1608.6 |
| 323.15 | 100000.00 | 1636.7 |
| 333.15 | 100.00 | 1252.0 |
| 333.15 | 10000.00 | 1297.9 |
| 333.15 | 20000.00 | 1340.7 |
| 333.15 | 30000.00 | 1380.8 |
| 333.15 | 40000.00 | 1418.3 |
| 333.15 | 50000.00 | 1454.2 |
| 333.15 | 60000.00 | 1488.4 |
| 333.15 | 70000.00 | 1520.7 |
| 333.15 | 80000.00 | 1551.9 |
| 333.15 | 90000.00 | 1581.5 |
| 333.15 | 100000.00 | 1610.2 |
| 343.15 | 100.00 | 1216.6 |
| 343.15 | 10000.00 | 1264.2 |
| 343.15 | 20000.00 | 1308.6 |
| 343.15 | 30000.00 | 1349.9 |
| 343.15 | 40000.00 | 1388.8 |
| 343.15 | 50000.00 | 1425.3 |
| 343.15 | 60000.00 | 1460.1 |
| 343.15 | 70000.00 | 1493.1 |
| 343.15 | 80000.00 | 1524.7 |
| 343.15 | 90000.00 | 1555.3 |
| 343.15 | 100000.00 | 1584.4 |
| 353.15 | 100.00 | 1181.6 |
| 353.15 | 10000.00 | 1231.2 |
| 353.15 | 20000.00 | 1276.9 |
| 353.15 | 30000.00 | 1319.8 |
| 353.15 | 40000.00 | 1359.8 |
| 353.15 | 50000.00 | 1397.1 |
| 353.15 | 60000.00 | 1432.8 |
| 353.15 | 70000.00 | 1466.5 |
| 353.15 | 80000.00 | 1498.9 |
| 353.15 | 90000.00 | 1529.8 |
| 353.15 | 100000.00 | 1559.5 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [419.76; 578.51] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.70035e+01 | |||
| Coefficient B | -6.17570e+03 | |||
| Coefficient C | -5.03140e+01 | |||
| Temperature range, min. | 419.76 | |||
| Temperature range, max. | 578.51 | |||
| Pvap | 1.33 | kPa | 419.76 | Calculated Property |
| Pvap | 2.86 | kPa | 437.40 | Calculated Property |
| Pvap | 5.72 | kPa | 455.04 | Calculated Property |
| Pvap | 10.82 | kPa | 472.68 | Calculated Property |
| Pvap | 19.45 | kPa | 490.32 | Calculated Property |
| Pvap | 33.41 | kPa | 507.95 | Calculated Property |
| Pvap | 55.13 | kPa | 525.59 | Calculated Property |
| Pvap | 87.76 | kPa | 543.23 | Calculated Property |
| Pvap | 135.30 | kPa | 560.87 | Calculated Property |
| Pvap | 202.64 | kPa | 578.51 | Calculated Property |
Similar Compounds
![2-[2-[2-[2-[2-[2-(2-Methoxyethoxy)ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethanol.](data:image/png;base64,iVBORw0KGgoAAAANSUhEUgAAAPoAAAD6CAIAAAAHjs1qAAAM7klEQVR4nO3abVDU5RrH8WuBJXQRRTFHZRQ11CYYDUtIKsiSFx585eDYJI0WkNEE0yhBaKxM2gSis9hsLZkQJ9+Edkzx8eBoagkqBLJTM0oipShO8uS6gLvsXufFH9YNZNntCc9cv88LhgWu5Wb93v+9F1ExMwHI4DXSCwD45yB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdBkDsIgtxBEOQOgiB3EAS5gyDIHQRB7iAIcgdB/lzuXV1ktf5FK/kH3blDdvtIL8JzHR0jvQLP2WxkMo30Iu7z+eOjBQXU20ttbRQbS0uX/nVL+jsxU3o6hYaS0Ujr1tGcOSO9IPe0t1NGBs2fT7W1tGMHaTQjvSD31NdTURGFhtK1a7Rt20ivhuiP526z0ZUr9OmnREQpKZ7mbjQa9Xr9rFmzQkJCEhISPJptbW3dtGlTZGRkU1PTunXrRo0a5cFwXR3NnUupqdTZSR98QAUFHn3rY8eOnT17trOzc+XKlVFRUR7NNjQ0bN26NTw8PCAg4NVXX1WpVB4M791LyckUGUknTlB5Oa1c6f6o3W7ftWuXzWarqanJzs6eMWOGR8s+ffr0wYMHvb294+LiXnjhBY9maedO2raN/PwoP58aGig01P1Rs9mcl5c3Z86cmpqanJyccePGefath8J/QH09X7/Ob73Vd/ONN7i+nm/dcmf09u3bqampPj4+RKS8jYmJqa2tdWfWarUWFhYGBgYSUUBAABGFhISUlZW5u+yTJ7mykj//nJm5q4vT0/n777mry53RS5cuxcfHE5GSqUqlWrVq1fXr192Z7ejoWL9+va+vLxE98sgjRLRw4cLKykq31myz8YkTrNez8hCdOcOlpXziBNvt7kyfOnXqySefJCI/Pz/l7XvvvWcymdyZbWpqWrFihXMqy5cvb2xsdGvZd+9yZSWnpnJvLzOzTsd1dXz6tDujdrt99+7dwcHBRDR27FgiCgoKMhgMvcpd/Tke5t7aymlp7OPDSUmckcF79nBhIe/axeHh7O/PWi339Aw1arVai4qKJk6cqISenJxcUFCg3PT29q56//1hNsyxYy8995zyuMfFxX3xxRfz589XbkZGRlZVVbmavXyZExKYiPV6Xr2ajxzh9ev5yBEOCODgYC4tdVGPyWTSarVKphqNJjs7OzMzU6lHo9G06HTc3T3k97XZzCUlU6dMISIvL6/XX399586d06dPVzZMQkJCU1OTq2VXVXFUFKtUXF7OSUl87Bi/9hofPMgqFS9YwGfOuBi9du1aYmKisjmnTp1aWFjouPn4jBnWL790tWHu3jUWFChPm6NHj87Jydm6datyffH19U1LS+vs7Bxy1m7nsjKePp0DA3n/ft6wgQ8d4qQkzs9nIo6P5ytXXCy7urr62WefVf5ZIyIiSkpKYmNjlZvJS5bwyZOuHi43uJu71Wrt0et5/HgmYh8fTk9nm41ra7mxkW/f5qVLmYiJePbsjqNHB48fP348PDxcWffixYvr6+uVjysxRU+fzhrNkBumoUGJ9d/R0Y899pjjcm6z2UpLSydNmqTElJiY2NLSMmC0s6ODMzLY15eJOCCADQbu6eHz5/nWLTYaed68vmXHxHRcvDhgdvD937x5U/mUElNGRAQTDblhzp3jqCgmSo+Jcb6cm81mrVbriEmr1XYNeobp/OUXXrGib23TpnFFBXd0cFUVm0x86BBPncpErFLxqlUdzc0DZs1m80cffeTv76/cf2ZmpuNyfuHChejo6P/GxjIRL1jA3303cM2OWImenzcvPj7+6tWrymeam5tTUlK8vLyIaPLkyUVFRTabbcD0nepqfuaZvmU/9RRfusQ3bvCFC2yxsE7HGg0TsZ9f78aNg59hbty4MeD+HZfzAwcOzJw5szky0p0N45pbuSux/icmhol48WLuj/V3Kio4LMzm5bXwiSdefPFFo9GofLihocFxOneO1dm9S5fub5g5c9ho5OZmPn+e793jLVscsdrz8+/duzdgtr29PTMzU7n6+vv7a7Xanp4edor1SnQ0e3lxYiL3x3qfzcalpTxpUmtg4MQJE5w3TFVVleN0PtTZw3LqlPOG4bY2vnyZ6+q4t5dffplVKiXWnrIy+6DN4Hz1DQ4OLi0tVb5GiXX82LHds2fz6NGcmcmDzx5mM2u1PGpU9eOPKz+yY8McOHBAefYgIudYHex2u3X3bp4ypW/DrFnDdjv/8ANfucK3bvGiRY5Ye86eHfwjKxtGuf8FCxZ8179hlFjDJ02yBwTw5MlcVMSDzx7NzZySwl5enzz/vPOGsVgsOp1OefZQq9UPfPbo6e7mzZsdG4a3bePubj53jltauLeXlT3f1sZ37gxes7Nhcr98+fKyZcuUHy987lxLebmrr7ZYfvzsM+VVhVqtTk1NdYSo0WgcIQ6pooLDwvjRR7m8nDds4MOHec0a1utZpXpwrL9fp2NThYaG5ubmKmdWInpj2TKuqXH1fdvbv968Wa1WE9G4ceNycnJeeeUVxzHAEeKD9W8YXrSId+xgg4G/+oqzsjgpachYnXz77bfOR7Lc3FzlzKpSqYrT0/nXX10t++pVbWqqMhsSEpKXl+d8DDjj8qjTt2H8/Dg9ndet46+/5sJC3rmTn36ag4JYp3tArP3sdntZWdm0adOUdS5fvjwzM3PMmDHKK5OqvLxhmquq+teSJY4fuaCgYNasWY79+fPPP7ua7d8wXFLCq1fz0aO8fj0fPcpaLTPznj3DnnaGyf3DDz90N9Z+ra2taWlp3t7eyhlApVI5HwOGYbGw0chvvtn3cH/8MV+8yIOOGUOpqKgICwsjovHjx7sVqxPHhlHO5QOOAcNob+fGRk5J6bu5di23tAwTaz/nI5NypYiIiDjt3qs6dtowymxQUJBOp3P3VV1jI9+8yW+/3XczJYUbGoa9QCqUI5nyWClXtOFj7ee8YSZMmEBEc+fOPXz4sFtrZubaWj57lktKmJm7unjtWo6PZ4OBU1L+bO7d3d0ZGRmDz8TDqqur27JlS15eXnV1taeznJbW9wuT/HxuaPBo1GKxbN++ff/+/bm5uYPPxMM6dOhQcXHxu++++6t7sf5OUlLfO8nJno62t7dnZWXt3bu3uLh48JnYtd7eXoPBsG/fvuzs7DvuxXqf1cpr1/a97/myGxsbs7KyDAbD8ePHPZ01mUwbN27ct2+fXq+3Wq2eDdfWsl7P3P+7k4wM/u03Li4eNncVM9PD5scfSa+n2bPp5k3Kyxvp1bjtm2/o/HnSaCgwkPqPGf8Htm8ni4Xa2uillygubqRX4x5meucdmjmTfvqJkpLo4EHatIn27qWgIOr/Tc4DPZS5E5HdTmYzjRkz0uvwkMVCNht59D9fD4OuLlKrSa0e6XV4yGQif39SqchqJbWabDZSqcjL1d/FPKy5A/wN8BeRIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQBLmDIMgdBEHuIAhyB0GQOwiC3EEQ5A6CIHcQ5H/0nY79X1gdWwAAAABJRU5ErkJggg==)
Find more compounds similar to Tetraglyme.
Mixtures
- Tetraglyme + 1-Butanol
- Carbon dioxide + Tetraglyme
- Tetraglyme + Propanoic acid, 2-hydroxy-, ethyl ester
- Tetraglyme + Heptane
- Tetraglyme + Octane
- Ethanol + Tetraglyme
- Tetraglyme + Water
- Tetraglyme + Tetradecane
- Hexadecane + Ethanol + Tetraglyme
- Tetraglyme + Norflurane
- 1,2-Ethanediol + Tetraglyme + Sulfur dioxide
- helium + Tetraglyme
- neon + Tetraglyme
- Tetraglyme + Argon
- Tetraglyme + Krypton
- Xenon + Tetraglyme
- Hydrogen + Tetraglyme
- Nitrogen + Tetraglyme
- Methane + Tetraglyme
- Tetraglyme + Ethylene
Find more mixtures with Tetraglyme.
Sources
- Crippen Method
- Crippen Method
- Volumetric Properties, Viscosities, and Refractive Indices of the Binary Systems 1-Butanol + PEG 200, + PEG 400, and + TEGDME
- Viscosity measurements and correlations of binary mixtures: 1,1,1,2-tetrafluoroethane (HFC-134a) + tetraethylene glycol dimethylether (TEGDME)
- Density, viscosity and solubility of carbon dioxide in glymes
- Volumetric and viscometric behavior of the binary systems ethyl lactate + 1,2- propanediol, + 1,3-propanediol, + tetrahydrofuran and + tetraethylene glycol dimethyl ether. New UNIFAC-VISCO and ASOG-VISCO parameters determination
- Solubility of dilute sulfur dioxide in binary mixtures of ethylene glycol and tetraethylene glycol dimethyl ether
- Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes
- Thermophysical properties of glycols and glymes
- The Viscosity and Density of Ionic Liquid + Tetraglyme Mixtures and the Effect of Tetraglyme on CO2 Solubility
- Solubility Measurement and Thermodynamic Properties Calculation for Several CO2 + Ether Absorbent Systems
- Solubilities of Nonpolar Gases in Triethylene Glycol Dimethyl Ether, Tetraethylene Glycol Dimethyl Ether, Dimethyl Carbonate, and Diethyl Carbonate at 298.15 K and 101.33 kPa Partial Pressure of Gas
- Liquid Densities and Refractive Indices of Binary Mixtures for the Dimethyl Ether of a Glycol + Ethanol from T=288.15 K to 318.15 K
- Thermophysical properties of two PAG-derivative lubricants from high pressure acoustic measurements
- Volumetric Properties of Binary Tetraethylene Glycol Dimethyl Ether + Heptane Mixtures between (278.15 and 353.15) K and up to 25 MPa
- Densities, Viscosities, and Derived Functions of Binary Mixtures: (Tetraethylene Glycol Dimethyl Ether + Water) from 298.15 K to 343.15 K
- Thermodynamics of Mixtures Containing Ethers. Part III. Liquid-Liquid Equilibria for 2,5,8,11-Tetraoxadodecane or 2,5,8,11,14-Pentaoxapentadecane + Selected N-Alkanes
- Solubility Study of Methane and Ethane In Promising Physical Solvents for Natural Gas Sweetening Operations
- Volumetric and Surface Properties of Aqueous Mixtures of Polyethers at T = (298.15, 308.15, and 318.15) K
- Volumetric and Viscometric Behavior of Binary Systems 2-Butanol + PEG 200, + PEG 400, + Tetraethylene Glycol Dimethyl Ether, and + N-Methyl-2-pyrrolidone
- Liquid-Liquid Equilibrium of Ternary Mixtures Formed by Some Oligooxaethylenes with Ethanol and Hexadecane
- Thermal Conductivity Measurement of Polyglycol Alkyl Ethers at Temperatures from (303.15 to 393.15) K
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.