- InChI
- InChI=1S/C8H18O4/c1-9-3-5-11-7-8-12-6-4-10-2/h3-8H2,1-2H3
- InChI Key
- YFNKIDBQEZZDLK-UHFFFAOYSA-N
- Formula
- C8H18O4
- SMILES
- COCCOCCOCCOC
- Molecular Weight1
- 178.23
- CAS
- 112-49-2
- Other Names
-
- (CH3O(CH2)2OCH2)2
- 1,2-Bis(2-methoxyethoxy)ethane
- 1,2-Bis(methoxyethoxy)ethane
- Ansul Ether 161
- Dimethyl ether of triethylene glycol
- Ethane, 1,2-bis(2-methoxyethoxy)-
- Glyme 4
- Glyme-3
- NSC 66400
- Triethylene glycol dimethyl ether
- Triglyme
- methyltriglyme
- triethylene glycol, dimethyl ether
- triglyme (triethylene 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).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (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.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- λ : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (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
- Pressure Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| PAff | 946.60 | kJ/mol | NIST |
| BasG | 892.40 | kJ/mol | NIST |
| ΔfG° | -403.52 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -737.33 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 21.23 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 63.70 ± 3.30 | kJ/mol | NIST |
| IE | 9.80 | eV | NIST |
| log10WS | 0.48 | Crippen Calculated Property | |
| logPoct/wat | 0.312 | Crippen Calculated Property | |
| McVol | 147.060 | ml/mol | McGowan Calculated Property |
| Pc | 2370.28 | kPa | Joback Calculated Property |
| Inp | [205.88; 1232.30] |
|
|
| Inp | 1232.00 | NIST | |
| Inp | 1232.30 | NIST | |
| Inp | 205.88 | NIST | |
| Inp | 208.42 | NIST | |
| Inp | 205.88 | NIST | |
| Inp | 1232.30 | NIST | |
| Inp | 1232.00 | NIST | |
| S°liquid | 492.90 | J/mol×K | NIST |
| Tboil | [489.00; 489.20] | K |
|
| Tboil | 489.20 | K | NIST |
| Tboil | 489.00 ± 2.00 | K | NIST |
| Tboil | 489.15 | K | NIST |
| Tboil | 489.00 | K | NIST |
| Tc | 636.37 | K | Joback Calculated Property |
| Tfus | [228.00; 228.15] | K |
|
| Tfus | 228.15 | K | NIST |
| Tfus | 228.00 | K | NIST |
| Ttriple | 229.30 ± 0.20 | K | NIST |
| Vc | 0.555 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [331.93; 401.19] | J/mol×K | [472.12; 636.37] |
|
| Cp,gas | 331.93 | J/mol×K | 472.12 | Joback Calculated Property |
| Cp,gas | 344.16 | J/mol×K | 499.50 | Joback Calculated Property |
| Cp,gas | 356.14 | J/mol×K | 526.87 | Joback Calculated Property |
| Cp,gas | 367.85 | J/mol×K | 554.25 | Joback Calculated Property |
| Cp,gas | 379.27 | J/mol×K | 581.62 | Joback Calculated Property |
| Cp,gas | 390.39 | J/mol×K | 609.00 | Joback Calculated Property |
| Cp,gas | 401.19 | J/mol×K | 636.37 | Joback Calculated Property |
| Cp,liquid | [359.00; 382.00] | J/mol×K | [298.15; 353.15] |
|
| Cp,liquid | 368.20 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 367.78 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 359.00 | J/mol×K | 303.15 | Molar H... |
| Cp,liquid | 364.00 | J/mol×K | 308.15 | Molar H... |
| Cp,liquid | 366.00 | J/mol×K | 313.15 | Molar H... |
| Cp,liquid | 368.00 | J/mol×K | 318.15 | Molar H... |
| Cp,liquid | 370.00 | J/mol×K | 323.15 | Molar H... |
| Cp,liquid | 371.00 | J/mol×K | 328.15 | Molar H... |
| Cp,liquid | 373.00 | J/mol×K | 333.15 | Molar H... |
| Cp,liquid | 375.00 | J/mol×K | 338.15 | Molar H... |
| Cp,liquid | 379.00 | J/mol×K | 343.15 | Molar H... |
| Cp,liquid | 381.00 | J/mol×K | 348.15 | Molar H... |
| Cp,liquid | 382.00 | J/mol×K | 353.15 | Molar H... |
| η | [0.0007260; 0.0035600] | Pa×s | [273.15; 363.15] |
|
| η | 0.0035600 | Pa×s | 273.15 | Density... |
| η | 0.0031000 | Pa×s | 278.15 | Density... |
| η | 0.0027500 | Pa×s | 283.15 | Density... |
| η | 0.0024500 | Pa×s | 288.15 | Density... |
| η | 0.0021900 | Pa×s | 293.15 | Density... |
| η | 0.0019600 | Pa×s | 298.15 | Density... |
| η | 0.0017800 | Pa×s | 303.15 | Density... |
| η | 0.0017700 | Pa×s | 303.15 | Densiti... |
| η | 0.0014800 | Pa×s | 313.15 | Densiti... |
| η | 0.0014800 | Pa×s | 313.15 | Density... |
| η | 0.0012500 | Pa×s | 323.15 | Density... |
| η | 0.0012600 | Pa×s | 323.15 | Densiti... |
| η | 0.0010800 | Pa×s | 333.15 | Density... |
| η | 0.0010800 | Pa×s | 333.15 | Densiti... |
| η | 0.0009360 | Pa×s | 343.15 | Density... |
| η | 0.0009450 | Pa×s | 343.15 | Densiti... |
| η | 0.0008210 | Pa×s | 353.15 | Density... |
| η | 0.0007260 | Pa×s | 363.15 | Density... |
| ΔfusH | [23.71; 23.71] | kJ/mol | [229.30; 229.30] |
|
| ΔfusH | 23.71 | kJ/mol | 229.30 | NIST |
| ΔfusH | 23.71 | kJ/mol | 229.30 | NIST |
| ΔfusH | 23.71 | kJ/mol | 229.30 | NIST |
| n0 | [1.41250; 1.42500] | [288.15; 318.15] |
|
|
| n0 | 1.42500 | 288.15 | Liquid ... | |
| n0 | 1.42090 | 298.15 | Liquid ... | |
| n0 | 1.41670 | 308.15 | Liquid ... | |
| n0 | 1.41250 | 318.15 | Liquid ... | |
| ρl | [909.70; 994.10] | kg/m3 | [283.15; 373.15] |
|
| ρl | 994.10 | kg/m3 | 283.15 | Thermop... |
| ρl | 990.80 | kg/m3 | 288.15 | Thermop... |
| ρl | 989.40 | kg/m3 | 288.15 | Thermop... |
| ρl | 984.60 | kg/m3 | 293.15 | Thermop... |
| ρl | 986.00 | kg/m3 | 293.15 | Thermop... |
| ρl | 981.50 | kg/m3 | 298.15 | Thermop... |
| ρl | 980.62 | kg/m3 | 298.15 | Thermod... |
| ρl | 979.90 | kg/m3 | 298.15 | Thermop... |
| ρl | 980.42 | kg/m3 | 298.15 | Liquid-... |
| ρl | 976.70 | kg/m3 | 303.15 | Thermop... |
| ρl | 975.10 | kg/m3 | 303.15 | Thermop... |
| ρl | 971.90 | kg/m3 | 308.15 | Thermop... |
| ρl | 970.40 | kg/m3 | 308.15 | Thermop... |
| ρl | 967.20 | kg/m3 | 313.15 | Thermop... |
| ρl | 965.60 | kg/m3 | 313.15 | Thermop... |
| ρl | 962.40 | kg/m3 | 318.15 | Thermop... |
| ρl | 956.10 | kg/m3 | 323.15 | Thermop... |
| ρl | 957.70 | kg/m3 | 323.15 | Thermop... |
| ρl | 952.90 | kg/m3 | 328.15 | Thermop... |
| ρl | 946.50 | kg/m3 | 333.15 | Thermop... |
| ρl | 948.10 | kg/m3 | 333.15 | Thermop... |
| ρl | 943.30 | kg/m3 | 338.15 | Thermop... |
| ρl | 936.90 | kg/m3 | 343.15 | Thermop... |
| ρl | 938.60 | kg/m3 | 343.15 | Thermop... |
| ρl | 933.80 | kg/m3 | 348.15 | Thermop... |
| ρl | 929.00 | kg/m3 | 353.15 | Thermop... |
| ρl | 924.20 | kg/m3 | 358.15 | Thermop... |
| ρl | 919.40 | kg/m3 | 363.15 | Thermop... |
| ρl | 914.50 | kg/m3 | 368.15 | Thermop... |
| ρl | 909.70 | kg/m3 | 373.15 | Thermop... |
| ΔfusS | 103.40 | J/mol×K | 229.30 | NIST |
| 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 | [0.12; 0.14] | W/m×K | [302.75; 392.16] |
|
| λ | 0.14 | 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 | 0.12 | W/m×K | 392.16 | Thermal... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [376.60; 376.70] | K | [1.30; 1.30] |
|
| Tboilr | 376.70 | K | 1.30 | NIST |
| Tboilr | 376.60 | K | 1.30 | NIST |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 100.00 | 0.0021 |
| 293.15 | 20000.00 | 0.0025 |
| 293.15 | 40000.00 | 0.0030 |
| 293.15 | 60000.00 | 0.0034 |
| 293.15 | 80000.00 | 0.0039 |
| 293.15 | 100000.00 | 0.0044 |
| 313.15 | 100.00 | 0.0015 |
| 313.15 | 20000.00 | 0.0018 |
| 313.15 | 40000.00 | 0.0020 |
| 313.15 | 60000.00 | 0.0024 |
| 313.15 | 80000.00 | 0.0027 |
| 313.15 | 100000.00 | 0.0030 |
| 333.15 | 100.00 | 0.0011 |
| 333.15 | 20000.00 | 0.0013 |
| 333.15 | 40000.00 | 0.0015 |
| 333.15 | 60000.00 | 0.0017 |
| 333.15 | 80000.00 | 0.0019 |
| 333.15 | 100000.00 | 0.0021 |
| 353.15 | 100.00 | 0.0008 |
| 353.15 | 20000.00 | 0.0010 |
| 353.15 | 40000.00 | 0.0011 |
| 353.15 | 60000.00 | 0.0013 |
| 353.15 | 80000.00 | 0.0015 |
| 353.15 | 100000.00 | 0.0016 |
| Reference | ||
Speed of sound, m/s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Speed of sound, m/s - Liquid |
| 293.15 | 100.00 | 1361.9 |
| 293.15 | 10000.00 | 1403.1 |
| 293.15 | 20000.00 | 1442.5 |
| 293.15 | 30000.00 | 1479.3 |
| 293.15 | 40000.00 | 1514.7 |
| 293.15 | 50000.00 | 1547.8 |
| 293.15 | 60000.00 | 1579.5 |
| 293.15 | 70000.00 | 1610.0 |
| 293.15 | 80000.00 | 1639.3 |
| 293.15 | 90000.00 | 1667.4 |
| 293.15 | 100000.00 | 1694.6 |
| 303.15 | 100.00 | 1323.2 |
| 303.15 | 10000.00 | 1366.5 |
| 303.15 | 20000.00 | 1407.2 |
| 303.15 | 30000.00 | 1445.2 |
| 303.15 | 40000.00 | 1481.6 |
| 303.15 | 50000.00 | 1515.7 |
| 303.15 | 60000.00 | 1548.2 |
| 303.15 | 70000.00 | 1579.4 |
| 303.15 | 80000.00 | 1609.3 |
| 303.15 | 90000.00 | 1638.2 |
| 303.15 | 100000.00 | 1665.9 |
| 313.15 | 100.00 | 1285.1 |
| 313.15 | 10000.00 | 1330.0 |
| 313.15 | 20000.00 | 1372.2 |
| 313.15 | 30000.00 | 1411.8 |
| 313.15 | 40000.00 | 1448.8 |
| 313.15 | 50000.00 | 1484.1 |
| 313.15 | 60000.00 | 1517.5 |
| 313.15 | 70000.00 | 1549.7 |
| 313.15 | 80000.00 | 1580.3 |
| 313.15 | 90000.00 | 1609.9 |
| 313.15 | 100000.00 | 1638.1 |
| 323.15 | 100.00 | 1247.7 |
| 323.15 | 10000.00 | 1294.6 |
| 323.15 | 20000.00 | 1338.5 |
| 323.15 | 30000.00 | 1379.1 |
| 323.15 | 40000.00 | 1417.3 |
| 323.15 | 50000.00 | 1453.6 |
| 323.15 | 60000.00 | 1487.9 |
| 323.15 | 70000.00 | 1520.7 |
| 323.15 | 80000.00 | 1552.0 |
| 323.15 | 90000.00 | 1581.9 |
| 323.15 | 100000.00 | 1610.8 |
| 333.15 | 100.00 | 1210.9 |
| 333.15 | 10000.00 | 1259.5 |
| 333.15 | 20000.00 | 1304.8 |
| 333.15 | 30000.00 | 1346.9 |
| 333.15 | 40000.00 | 1386.3 |
| 333.15 | 50000.00 | 1423.4 |
| 333.15 | 60000.00 | 1458.8 |
| 333.15 | 70000.00 | 1492.1 |
| 333.15 | 80000.00 | 1524.3 |
| 333.15 | 90000.00 | 1554.8 |
| 333.15 | 100000.00 | 1584.3 |
| 343.15 | 100.00 | 1174.6 |
| 343.15 | 10000.00 | 1225.1 |
| 343.15 | 20000.00 | 1272.0 |
| 343.15 | 30000.00 | 1315.6 |
| 343.15 | 40000.00 | 1356.2 |
| 343.15 | 50000.00 | 1394.1 |
| 343.15 | 60000.00 | 1430.3 |
| 343.15 | 70000.00 | 1464.6 |
| 343.15 | 80000.00 | 1497.2 |
| 343.15 | 90000.00 | 1528.4 |
| 343.15 | 100000.00 | 1558.5 |
| 353.15 | 100.00 | 1138.7 |
| 353.15 | 10000.00 | 1191.5 |
| 353.15 | 20000.00 | 1240.0 |
| 353.15 | 30000.00 | 1284.6 |
| 353.15 | 40000.00 | 1326.2 |
| 353.15 | 50000.00 | 1365.6 |
| 353.15 | 60000.00 | 1402.4 |
| 353.15 | 70000.00 | 1437.6 |
| 353.15 | 80000.00 | 1470.9 |
| 353.15 | 90000.00 | 1502.6 |
| 353.15 | 100000.00 | 1533.4 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [372.99; 516.68] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.57644e+01 | |||
| Coefficient B | -4.62697e+03 | |||
| Coefficient C | -7.40300e+01 | |||
| Temperature range, min. | 372.99 | |||
| Temperature range, max. | 516.68 | |||
| Pvap | 1.33 | kPa | 372.99 | Calculated Property |
| Pvap | 2.92 | kPa | 388.96 | Calculated Property |
| Pvap | 5.94 | kPa | 404.92 | Calculated Property |
| Pvap | 11.30 | kPa | 420.89 | Calculated Property |
| Pvap | 20.32 | kPa | 436.85 | Calculated Property |
| Pvap | 34.79 | kPa | 452.82 | Calculated Property |
| Pvap | 57.01 | kPa | 468.78 | Calculated Property |
| Pvap | 89.92 | kPa | 484.75 | Calculated Property |
| Pvap | 137.06 | kPa | 500.71 | Calculated Property |
| Pvap | 202.66 | kPa | 516.68 | 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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)
Find more compounds similar to 2,5,8,11-Tetraoxadodecane.
Mixtures
- 2,5,8,11-Tetraoxadodecane + Norflurane
- 2,5,8,11-Tetraoxadodecane + Carbon dioxide
- 2,5,8,11-Tetraoxadodecane + Ethanol
- 2,5,8,11-Tetraoxadodecane + Decane
- 2,5,8,11-Tetraoxadodecane + Tetradecane
- 2,5,8,11-Tetraoxadodecane + Water
- 2,5,8,11-Tetraoxadodecane + Hexadecane + Ethanol
- Ethane, fluoro- + 2,5,8,11-Tetraoxadodecane
- 2,5,8,11-Tetraoxadodecane + Ethane, 1,1-difluoro-
- Difluoromethane + 2,5,8,11-Tetraoxadodecane
- helium + 2,5,8,11-Tetraoxadodecane
- 2,5,8,11-Tetraoxadodecane + neon
- 2,5,8,11-Tetraoxadodecane + Argon
- 2,5,8,11-Tetraoxadodecane + Krypton
- Xenon + 2,5,8,11-Tetraoxadodecane
- Hydrogen + 2,5,8,11-Tetraoxadodecane
- Nitrogen + 2,5,8,11-Tetraoxadodecane
- 2,5,8,11-Tetraoxadodecane + Methane
- 2,5,8,11-Tetraoxadodecane + Ethylene
- 2,5,8,11-Tetraoxadodecane + Ethane
Find more mixtures with 2,5,8,11-Tetraoxadodecane.
Sources
- Crippen Method
- Crippen Method
- High-pressure viscosity behavior of x 1,1,1,2-tetrafluoroethane (HFC-134a) + (1-x) triethylene glycol dimethylether (TriEGDME) mixtures: Measurements and modeling
- Density, viscosity and solubility of carbon dioxide in glymes
- Bubble pressure measurements for the (1,1,1,2-tetrafluoroethane + triethylene glycol dimethyl ether) system
- Thermophysical properties of glycols and glymes
- Measurement and Correlation of Isothermal Vapor Liquid Equilibrium of Fluoroethane + Dimethyl Ether Triethylene Glycol, 1,1-Difluoroethane + Dimethyl Ether Triethylene Glycol, and 1,1-Difluoroethane + N-Methyl-2-pyrrolidone Systems
- Isothermal Vapor Liquid Equilibrium of HFC-161 + DMETrEG within the Temperature Range of 293.15 353.15 K and Comparison for HFC-161 Combined with Different Absorbents
- Isothermal Vapor-Liquid Equilibria of the Absorption Working Pairs (R1234yf + NMP, R1234yf + DMETrEG) at Temperatures from 293.15 K to 353.15 K
- Isothermal Vapor-Liquid Equilibrium of the Absorption Working Pairs (HFC-32 + DMETrEG, HFC-32 + NMP) at Temperatures from 293.15 to 343.15 K
- 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
- 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
- Densities, Viscosities and Derived Functions of Binary Mixtures: (Triethylene Glycol Dimethyl Ether + Water) and (N-acetylmorpholine+ Water) from 298.15 to 343.15 K
- Solubility Study of Methane and Ethane In Promising Physical Solvents for Natural Gas Sweetening Operations
- P-rho-T-x Measurements for (1,1,1,2-Tetrafluoroethane + Triethylene Glycol Dimethyl Ether) at High Haloalkane Content
- Volumetric and Surface Properties of Aqueous Mixtures of Polyethers at T = (298.15, 308.15, and 318.15) K
- Liquid-Liquid Equilibrium of Ternary Mixtures Formed by Some Oligooxaethylenes with Ethanol and Hexadecane
- Molar Heat Capacity of Aqueous Sulfolane, 4-Formylmorpholine, 1-Methyl-2-pyrrolidinone, and Triethylene Glycol Dimethyl Ether Solutions from (303.15 to 353.15) K
- Thermal Conductivity Measurement of Polyglycol Alkyl Ethers at Temperatures from (303.15 to 393.15) K
- p-T-x Measurements for Some Working Fluids for an Absorption Heat Transformer: 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylether Diethylene Glycol (DMEDEG) and Dimethylether Triethylene Glycol (DMETrEG)
- 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.