- 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(methoxyethoxy)ethane
- 1,2-bis(2-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
- methyltriglyme
- triethylene glycol, dimethyl ether
- triglyme
- triglyme (triethylene glycol dimethyl ether)
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- BasG : Gas basicity (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- εr : Dielectric Constant (Relative permittivity).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- 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).
- 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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- NFPA Safety : NFPA Safety Rating.
- Pc : Critical Pressure (kPa).
- Ptriple : Triple Point 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).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Pressure Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.7915 | ChemSep v8.3 pure component data Compiled value | |
| PAff | 946.60 | kJ/mol | NIST |
| Tig | 463.15 | K | NCMS SOLV-DB |
| BasG | 892.40 | kJ/mol | NIST |
| μ | 2.24 | debye | ChemSep v8.3 pure component data Compiled value |
| Tflash,cc | 384.15 | K | NCMS SOLV-DB |
| ΔfG° | -375.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -676.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfusH° | 21.23 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [59.83; 63.70] | kJ/mol |
|
| ΔvapH° | 59.83 | kJ/mol | NCMS SOLV-DB |
| ΔvapH° | 63.70 ± 3.30 | kJ/mol | NIST |
| IE | 9.80 | eV | NIST |
| log10WS | 0.03 | Relay (1.0) Calculated Property | |
| logPoct/wat | 0.005 | NCMS SOLV-DB | |
| McVol | 147.060 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | NCMS SOLV-DB | |
| NFPA Health | 1 | NCMS SOLV-DB | |
| NFPA Safety | 0 | NCMS SOLV-DB | |
| Pc | 2310.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 8.07e-07 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [205.88; 1232.30] |
|
|
| Inp | 1232.00 | NIST | |
| Inp | 1232.30 | NIST | |
| Inp | 205.88 | NIST | |
| Inp | 208.42 | NIST | |
| Inp | 1232.30 | NIST | |
| Inp | 1232.00 | NIST | |
| Inp | 205.88 | NIST | |
| S°liquid | 492.90 | J/mol×K | NIST |
| Tboil | [489.00; 489.20] | K |
|
| Tboil | 489.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 489.15 | K | NCMS SOLV-DB |
| Tboil | 489.20 | K | NIST |
| Tboil | 489.00 ± 2.00 | K | NIST |
| Tboil | 489.15 | K | NIST |
| Tboil | 489.00 | K | NIST |
| Tc | [651.00; 681.20] | K |
|
| Tc | 681.20 | K | DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development |
| Tc | 651.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [228.00; 228.15] | K |
|
| Tfus | 228.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 228.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 228.15 | K | NCMS SOLV-DB |
| Tfus | 228.15 | K | NIST |
| Tfus | 228.00 | K | NIST |
| Ttriple | [229.30; 229.35] | K |
|
| Ttriple | 229.35 | K | ChemSep v8.3 pure component data Compiled value |
| Ttriple | 229.30 ± 0.20 | K | NIST |
| Ttriple | 229.30 ± 0.20 | K | NIST |
| UQi | 5.90 | ChemSep v8.3 pure component data Compiled value | |
| URi | 6.82 | ChemSep v8.3 pure component data Compiled value | |
| Vc | 0.548 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2340000 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
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 |
|---|---|---|---|---|
| Cp,gas | [205.70; 586.05] | J/mol×K | [255.00; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 1.28487e+02 | |||
| Coefficient B | -5.46647e+02 | |||
| Coefficient C | 6.49034e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 255.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 205.70 | J/mol×K | 255.00 | Calculated Property |
| Cp,gas | 292.60 | J/mol×K | 393.33 | Calculated Property |
| Cp,gas | 364.09 | J/mol×K | 531.67 | Calculated Property |
| Cp,gas | 419.82 | J/mol×K | 670.00 | Calculated Property |
| Cp,gas | 463.47 | J/mol×K | 808.33 | Calculated Property |
| Cp,gas | 498.26 | J/mol×K | 946.67 | Calculated Property |
| Cp,gas | 526.51 | J/mol×K | 1085.00 | Calculated Property |
| Cp,gas | 549.85 | J/mol×K | 1223.33 | Calculated Property |
| Cp,gas | 569.42 | J/mol×K | 1361.67 | Calculated Property |
| Cp,gas | 586.05 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [367.20; 378.30] | J/mol×K | [229.35; 350.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 4.72930e+02 | |||
| Coefficient B | -8.23400e-01 | |||
| Coefficient C | 1.58010e-03 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 229.35 | |||
| Temperature range, max. | 350.00 | |||
| Cp,liquid | 367.20 | J/mol×K | 229.35 | Calculated Property |
| Cp,liquid | 366.16 | J/mol×K | 242.76 | Calculated Property |
| Cp,liquid | 365.69 | J/mol×K | 256.16 | Calculated Property |
| Cp,liquid | 365.79 | J/mol×K | 269.57 | Calculated Property |
| Cp,liquid | 366.45 | J/mol×K | 282.97 | Calculated Property |
| Cp,liquid | 367.69 | J/mol×K | 296.38 | Calculated Property |
| Cp,liquid | 369.49 | J/mol×K | 309.78 | Calculated Property |
| Cp,liquid | 371.86 | J/mol×K | 323.19 | Calculated Property |
| Cp,liquid | 374.80 | J/mol×K | 336.59 | Calculated Property |
| Cp,liquid | 378.30 | J/mol×K | 350.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0181220; 0.0002839] | Pa×s | [229.35; 489.15] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -8.90680e+00 | |||
| Coefficient B | 1.65510e+03 | |||
| Coefficient C | -4.26900e-01 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 229.35 | |||
| Temperature range, max. | 489.15 | |||
| η | 0.0181220 | Pa×s | 229.35 | Calculated Property |
| η | 0.0076889 | Pa×s | 258.22 | Calculated Property |
| η | 0.0038575 | Pa×s | 287.08 | Calculated Property |
| η | 0.0021867 | Pa×s | 315.95 | Calculated Property |
| η | 0.0013587 | Pa×s | 344.82 | Calculated Property |
| η | 0.0009061 | Pa×s | 373.68 | Calculated Property |
| η | 0.0006389 | Pa×s | 402.55 | Calculated Property |
| η | 0.0004711 | Pa×s | 431.42 | Calculated Property |
| η | 0.0003603 | Pa×s | 460.28 | Calculated Property |
| η | 0.0002839 | Pa×s | 489.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [74.47; 0.00] | kJ/mol | [229.35; 651.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 8.85000e+01 | |||
| Coefficient B | 3.97400e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 6.51000e+02 | |||
| Temperature range, min. | 229.35 | |||
| Temperature range, max. | 651.00 | |||
| ΔvapH | 74.47 | kJ/mol | 229.35 | Calculated Property |
| ΔvapH | 71.06 | kJ/mol | 276.20 | Calculated Property |
| ΔvapH | 67.39 | kJ/mol | 323.05 | Calculated Property |
| ΔvapH | 63.39 | kJ/mol | 369.90 | Calculated Property |
| ΔvapH | 58.96 | kJ/mol | 416.75 | Calculated Property |
| ΔvapH | 53.95 | kJ/mol | 463.60 | Calculated Property |
| ΔvapH | 48.13 | kJ/mol | 510.45 | Calculated Property |
| ΔvapH | 40.96 | kJ/mol | 557.30 | Calculated Property |
| ΔvapH | 31.10 | kJ/mol | 604.15 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 651.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [372.99; 516.68] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| 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 |
| Pvap | [8.07e-07; 2318.46] | kPa | [229.35; 651.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 9.68422e+01 | |||
| Coefficient B | -1.16330e+04 | |||
| Coefficient C | -1.10670e+01 | |||
| Coefficient D | 6.22080e-18 | |||
| Coefficient E | 6.00000e+00 | |||
| Temperature range, min. | 229.35 | |||
| Temperature range, max. | 651.00 | |||
| Pvap | 8.07e-07 | kPa | 229.35 | Calculated Property |
| Pvap | 5.63e-04 | kPa | 276.20 | Calculated Property |
| Pvap | 0.04 | kPa | 323.05 | Calculated Property |
| Pvap | 0.97 | kPa | 369.90 | Calculated Property |
| Pvap | 9.02 | kPa | 416.75 | Calculated Property |
| Pvap | 47.98 | kPa | 463.60 | Calculated Property |
| Pvap | 173.57 | kPa | 510.45 | Calculated Property |
| Pvap | 481.53 | kPa | 557.30 | Calculated Property |
| Pvap | 1117.09 | kPa | 604.15 | Calculated Property |
| Pvap | 2318.46 | kPa | 651.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1060.75; 325.23] | kg/m3 | [229.35; 651.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 8.00769e+01 | |||
| Coefficient B | 2.46220e-01 | |||
| Coefficient C | 6.51000e+02 | |||
| Coefficient D | 3.91800e-01 | |||
| Temperature range, min. | 229.35 | |||
| Temperature range, max. | 651.00 | |||
| ρl | 1060.75 | kg/m3 | 229.35 | Calculated Property |
| ρl | 1005.68 | kg/m3 | 276.20 | Calculated Property |
| ρl | 949.44 | kg/m3 | 323.05 | Calculated Property |
| ρl | 891.66 | kg/m3 | 369.90 | Calculated Property |
| ρl | 831.77 | kg/m3 | 416.75 | Calculated Property |
| ρl | 768.89 | kg/m3 | 463.60 | Calculated Property |
| ρl | 701.50 | kg/m3 | 510.45 | Calculated Property |
| ρl | 626.60 | kg/m3 | 557.30 | Calculated Property |
| ρl | 536.12 | kg/m3 | 604.15 | Calculated Property |
| ρl | 325.23 | kg/m3 | 651.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 0.00] | N/m | [229.35; 651.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is γ in N/m, T in K | |||
| Coefficient A | 6.98600e-02 | |||
| Coefficient B | 1.46840e+00 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 6.51000e+02 | |||
| Temperature range, min. | 229.35 | |||
| Temperature range, max. | 651.00 | |||
| γ | 0.04 | N/m | 229.35 | Calculated Property |
| γ | 0.03 | N/m | 276.20 | Calculated Property |
| γ | 0.03 | N/m | 323.05 | Calculated Property |
| γ | 0.02 | N/m | 369.90 | Calculated Property |
| γ | 0.02 | N/m | 416.75 | Calculated Property |
| γ | 0.01 | N/m | 463.60 | Calculated Property |
| γ | 0.01 | N/m | 510.45 | Calculated Property |
| γ | 0.00 | N/m | 557.30 | Calculated Property |
| γ | 0.00 | N/m | 604.15 | Calculated Property |
| γ | 0.00 | N/m | 651.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.02; 0.06] | W/m×K | [489.15; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | 1.72470e-04 | |||
| Coefficient B | 9.29620e-01 | |||
| Coefficient C | 7.34400e+02 | |||
| Coefficient D | 0.00000e+00 | |||
| Temperature range, min. | 489.15 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.02 | W/m×K | 489.15 | Calculated Property |
| λgas | 0.03 | W/m×K | 545.91 | Calculated Property |
| λgas | 0.03 | W/m×K | 602.67 | Calculated Property |
| λgas | 0.03 | W/m×K | 659.43 | Calculated Property |
| λgas | 0.04 | W/m×K | 716.19 | Calculated Property |
| λgas | 0.04 | W/m×K | 772.96 | Calculated Property |
| λgas | 0.05 | W/m×K | 829.72 | Calculated Property |
| λgas | 0.05 | W/m×K | 886.48 | Calculated Property |
| λgas | 0.06 | W/m×K | 943.24 | Calculated Property |
| λgas | 0.06 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.20; 0.09] | W/m×K | [229.35; 489.15] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λliquid in W/m×K, T in K | |||
| Coefficient A | 2.98150e-01 | |||
| Coefficient B | -4.34970e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 229.35 | |||
| Temperature range, max. | 489.15 | |||
| λliquid | 0.20 | W/m×K | 229.35 | Calculated Property |
| λliquid | 0.19 | W/m×K | 258.22 | Calculated Property |
| λliquid | 0.17 | W/m×K | 287.08 | Calculated Property |
| λliquid | 0.16 | W/m×K | 315.95 | Calculated Property |
| λliquid | 0.15 | W/m×K | 344.82 | Calculated Property |
| λliquid | 0.14 | W/m×K | 373.68 | Calculated Property |
| λliquid | 0.12 | W/m×K | 402.55 | Calculated Property |
| λliquid | 0.11 | W/m×K | 431.42 | Calculated Property |
| λliquid | 0.10 | W/m×K | 460.28 | Calculated Property |
| λliquid | 0.09 | W/m×K | 489.15 | Calculated Property |
Similar Compounds
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Find more compounds similar to 2,5,8,11-Tetraoxadodecane.
Mixtures
- Ethane, fluoro- + 2,5,8,11-Tetraoxadodecane
- 2,5,8,11-Tetraoxadodecane + Carbonic acid, dimethyl ester
- Diethyl carbonate + 2,5,8,11-Tetraoxadodecane
- 2,5,8,11-Tetraoxadodecane + Heptane
- 2,5,8,11-Tetraoxadodecane + Nonane
- 2,5,8,11-Tetraoxadodecane + Dodecane
- 2,5,8,11-Tetraoxadodecane + Norflurane
- 2,5,8,11-Tetraoxadodecane + Carbon dioxide
- 2,5,8,11-Tetraoxadodecane + Water
- 2,5,8,11-Tetraoxadodecane + Ethane, 1,1-difluoro-
- 2,5,8,11-Tetraoxadodecane + Ethanol
- 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
Find more mixtures with 2,5,8,11-Tetraoxadodecane.
Sources
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- Cheméo Relay (1.0)
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- 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
- On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
- Bubble pressure measurements for the (1,1,1,2-tetrafluoroethane + triethylene glycol dimethyl ether) system
- On permittivity and density of the systems {triglyme + (dimethyl or diethyl carbonate)} and formulation of De in terms of volume or mole fraction
- Permittivity and density of the systems (monoglyme, diglyme, triglyme, or tetraglyme + n-heptane) at several temperatures
- Enthalpies of solvation of ethylene oxide oligomers CH3O(CH2CH2O)nCH3 (n = 1 to 4) in different H-bonding solvents: Methanol, chloroform, and water. Group contribution method as applied to the polar oligomers
- Sync-measurement experimental study of (fluoroethane + dimethylether tetraethylene glycol), (fluoroethane + dimethylether triethylene glycol) and (fluoroethane + dimethylether diethylene glycol) systems
- Partial molar volumes of organic solutes in water. XXVII. Two aliphatic polyethers (triglyme, tetraglyme) at temperatures T = 298 573 K and pressures up to 30 MPa
- Thermochemical behaviour of straight-chain ethers CH3O(CH2CH2O)nCH3 (n = 1 4) in aqueous and tetrachlormethane solutions
- Effect of properties of the N,N-dimethylformamide-methanol and N,N-dimethylformamide-water mixtures on the solution enthalpy of glymes in these mixtures at 298.15 K
- 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
- DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
- 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
- Enthalpy of Solvation of Monoglyme, Diglyme, Triglyme, Tetraglyme, and Pentaglyme in Mixtures of Water with N,N-Dimethylformamide at 298.15 K
- Volumetric and Surface Properties of Aqueous Mixtures of Polyethers at T = (298.15, 308.15, and 318.15) K
- Partial Molar Volumes and Partial Molar Isentropic Compressions of Four Aliphatic Linear Polyethers at Infinite Dilution in Water at Temperatures T = (278 to 343) K and Atmospheric Pressure.
- 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
- NCMS SOLV-DB
- The Yaws Handbook of Vapor Pressure
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