- InChI
- InChI=1S/C12H26O6/c1-13-3-5-15-7-9-17-11-12-18-10-8-16-6-4-14-2/h3-12H2,1-2H3
- InChI Key
- DMDPGPKXQDIQQG-UHFFFAOYSA-N
- Formula
- C12H26O6
- SMILES
- COCCOCCOCCOCCOCCOC
- Molecular Weight1
- 266.33
- CAS
- 1191-87-3
- Other Names
-
- Pentaethylene glycol dimethyl ether
- Pentaethyleneglycol dimethyl ether
- pentaglyme
- ω : Acentric Factor.
- 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).
- 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).
- 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).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (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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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 1.1388 | ChemSep v8.3 pure component data Compiled value | |
| μ | 2.73 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -552.10 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -1006.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfusH° | 33.96 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 80.52 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.49 | eV | Relay (1.0) Calculated Property |
| log10WS | -0.23 | Relay (1.0) Calculated Property | |
| logPoct/wat | 0.346 | Crippen Calculated Property | |
| McVol | 215.160 | ml/mol | McGowan Calculated Property |
| Pc | 1667.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 5.38e-10 | kPa | ChemSep v8.3 pure component data Compiled value |
| Tboil | 615.10 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 769.80 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 261.60 | K | ChemSep v8.3 pure component data Compiled value |
| Ttriple | 261.60 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 8.54 | ChemSep v8.3 pure component data Compiled value | |
| URi | 10.01 | ChemSep v8.3 pure component data Compiled value | |
| Vc | 0.821 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2140000 | ChemSep v8.3 pure component data Compiled value |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [304.57; 870.39] | 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 | 1.92000e+02 | |||
| Coefficient B | -5.51819e+02 | |||
| Coefficient C | 6.88759e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 255.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 304.57 | J/mol×K | 255.00 | Calculated Property |
| Cp,gas | 432.97 | J/mol×K | 393.33 | Calculated Property |
| Cp,gas | 539.13 | J/mol×K | 531.67 | Calculated Property |
| Cp,gas | 622.09 | J/mol×K | 670.00 | Calculated Property |
| Cp,gas | 687.19 | J/mol×K | 808.33 | Calculated Property |
| Cp,gas | 739.13 | J/mol×K | 946.67 | Calculated Property |
| Cp,gas | 781.34 | J/mol×K | 1085.00 | Calculated Property |
| Cp,gas | 816.23 | J/mol×K | 1223.33 | Calculated Property |
| Cp,gas | 845.50 | J/mol×K | 1361.67 | Calculated Property |
| Cp,gas | 870.39 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [546.49; 596.90] | J/mol×K | [261.60; 421.46] |
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 | 7.33220e+02 | |||
| Coefficient B | -1.35260e+00 | |||
| Coefficient C | 2.44190e-03 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 261.60 | |||
| Temperature range, max. | 421.46 | |||
| Cp,liquid | 546.49 | J/mol×K | 261.60 | Calculated Property |
| Cp,liquid | 545.93 | J/mol×K | 279.36 | Calculated Property |
| Cp,liquid | 546.91 | J/mol×K | 297.12 | Calculated Property |
| Cp,liquid | 549.43 | J/mol×K | 314.89 | Calculated Property |
| Cp,liquid | 553.49 | J/mol×K | 332.65 | Calculated Property |
| Cp,liquid | 559.09 | J/mol×K | 350.41 | Calculated Property |
| Cp,liquid | 566.23 | J/mol×K | 368.17 | Calculated Property |
| Cp,liquid | 574.92 | J/mol×K | 385.94 | Calculated Property |
| Cp,liquid | 585.14 | J/mol×K | 403.70 | Calculated Property |
| Cp,liquid | 596.90 | J/mol×K | 421.46 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0200844; 0.0001864] | Pa×s | [261.60; 615.84] |
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 | 3.74910e+01 | |||
| Coefficient B | -1.99070e+03 | |||
| Coefficient C | -6.68820e+00 | |||
| Coefficient D | 1.61240e+10 | |||
| Coefficient E | -4.00000e+00 | |||
| Temperature range, min. | 261.60 | |||
| Temperature range, max. | 615.84 | |||
| η | 0.0200844 | Pa×s | 261.60 | Calculated Property |
| η | 0.0048559 | Pa×s | 300.96 | Calculated Property |
| η | 0.0021380 | Pa×s | 340.32 | Calculated Property |
| η | 0.0012314 | Pa×s | 379.68 | Calculated Property |
| η | 0.0008089 | Pa×s | 419.04 | Calculated Property |
| η | 0.0005699 | Pa×s | 458.40 | Calculated Property |
| η | 0.0004179 | Pa×s | 497.76 | Calculated Property |
| η | 0.0003143 | Pa×s | 537.12 | Calculated Property |
| η | 0.0002405 | Pa×s | 576.48 | Calculated Property |
| η | 0.0001864 | Pa×s | 615.84 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [114.25; 0.00] | kJ/mol | [261.60; 769.80] |
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 | 1.55720e+02 | |||
| Coefficient B | 9.23500e-01 | |||
| Coefficient C | -5.26180e-01 | |||
| Coefficient D | 9.17860e-03 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 7.69800e+02 | |||
| Temperature range, min. | 261.60 | |||
| Temperature range, max. | 769.80 | |||
| ΔvapH | 114.25 | kJ/mol | 261.60 | Calculated Property |
| ΔvapH | 106.79 | kJ/mol | 318.07 | Calculated Property |
| ΔvapH | 99.65 | kJ/mol | 374.53 | Calculated Property |
| ΔvapH | 92.72 | kJ/mol | 431.00 | Calculated Property |
| ΔvapH | 85.82 | kJ/mol | 487.47 | Calculated Property |
| ΔvapH | 78.72 | kJ/mol | 543.93 | Calculated Property |
| ΔvapH | 71.01 | kJ/mol | 600.40 | Calculated Property |
| ΔvapH | 61.84 | kJ/mol | 656.87 | Calculated Property |
| ΔvapH | 48.84 | kJ/mol | 713.33 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 769.80 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [5.38e-10; 1672.11] | kPa | [261.60; 769.80] |
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 | 1.33222e+02 | |||
| Coefficient B | -1.77940e+04 | |||
| Coefficient C | -1.55470e+01 | |||
| Coefficient D | 3.08550e-18 | |||
| Coefficient E | 6.00000e+00 | |||
| Temperature range, min. | 261.60 | |||
| Temperature range, max. | 769.80 | |||
| Pvap | 5.38e-10 | kPa | 261.60 | Calculated Property |
| Pvap | 4.53e-06 | kPa | 318.07 | Calculated Property |
| Pvap | 1.65e-03 | kPa | 374.53 | Calculated Property |
| Pvap | 0.10 | kPa | 431.00 | Calculated Property |
| Pvap | 1.71 | kPa | 487.47 | Calculated Property |
| Pvap | 14.31 | kPa | 543.93 | Calculated Property |
| Pvap | 71.27 | kPa | 600.40 | Calculated Property |
| Pvap | 249.64 | kPa | 656.87 | Calculated Property |
| Pvap | 692.92 | kPa | 713.33 | Calculated Property |
| Pvap | 1672.11 | kPa | 769.80 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1056.13; 324.41] | kg/m3 | [261.60; 769.80] |
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 | 8.29168e+01 | |||
| Coefficient B | 2.55590e-01 | |||
| Coefficient C | 7.69800e+02 | |||
| Coefficient D | 3.48570e-01 | |||
| Temperature range, min. | 261.60 | |||
| Temperature range, max. | 769.80 | |||
| ρl | 1056.13 | kg/m3 | 261.60 | Calculated Property |
| ρl | 1007.16 | kg/m3 | 318.07 | Calculated Property |
| ρl | 956.58 | kg/m3 | 374.53 | Calculated Property |
| ρl | 903.97 | kg/m3 | 431.00 | Calculated Property |
| ρl | 848.69 | kg/m3 | 487.47 | Calculated Property |
| ρl | 789.76 | kg/m3 | 543.93 | Calculated Property |
| ρl | 725.48 | kg/m3 | 600.40 | Calculated Property |
| ρl | 652.47 | kg/m3 | 656.87 | Calculated Property |
| ρl | 561.60 | kg/m3 | 713.33 | Calculated Property |
| ρl | 324.41 | kg/m3 | 769.80 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 0.00] | N/m | [261.60; 769.80] |
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 | 7.83630e-02 | |||
| Coefficient B | 1.54590e+00 | |||
| Coefficient C | 5.49290e-01 | |||
| Coefficient D | -8.57920e-01 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 7.69800e+02 | |||
| Temperature range, min. | 261.60 | |||
| Temperature range, max. | 769.80 | |||
| γ | 0.04 | N/m | 261.60 | Calculated Property |
| γ | 0.03 | N/m | 318.07 | Calculated Property |
| γ | 0.03 | N/m | 374.53 | Calculated Property |
| γ | 0.02 | N/m | 431.00 | Calculated Property |
| γ | 0.02 | N/m | 487.47 | Calculated Property |
| γ | 0.01 | N/m | 543.93 | Calculated Property |
| γ | 0.01 | N/m | 600.40 | Calculated Property |
| γ | 0.01 | N/m | 656.87 | Calculated Property |
| γ | 0.00 | N/m | 713.33 | Calculated Property |
| γ | 0.00 | N/m | 769.80 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.03; 0.05] | W/m×K | [615.10; 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 | 1.44600e-04 | |||
| Coefficient B | 9.32300e-01 | |||
| Coefficient C | 8.01500e+02 | |||
| Coefficient D | 0.00000e+00 | |||
| Temperature range, min. | 615.10 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.03 | W/m×K | 615.10 | Calculated Property |
| λgas | 0.03 | W/m×K | 657.87 | Calculated Property |
| λgas | 0.03 | W/m×K | 700.63 | Calculated Property |
| λgas | 0.03 | W/m×K | 743.40 | Calculated Property |
| λgas | 0.04 | W/m×K | 786.17 | Calculated Property |
| λgas | 0.04 | W/m×K | 828.93 | Calculated Property |
| λgas | 0.04 | W/m×K | 871.70 | Calculated Property |
| λgas | 0.04 | W/m×K | 914.47 | Calculated Property |
| λgas | 0.05 | W/m×K | 957.23 | Calculated Property |
| λgas | 0.05 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.11; 0.06] | W/m×K | [230.94; 615.84] |
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 | 1.43730e-01 | |||
| Coefficient B | -1.34530e-04 | |||
| Coefficient C | -1.26190e-09 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 230.94 | |||
| Temperature range, max. | 615.84 | |||
| λliquid | 0.11 | W/m×K | 230.94 | Calculated Property |
| λliquid | 0.11 | W/m×K | 273.71 | Calculated Property |
| λliquid | 0.10 | W/m×K | 316.47 | Calculated Property |
| λliquid | 0.10 | W/m×K | 359.24 | Calculated Property |
| λliquid | 0.09 | W/m×K | 402.01 | Calculated Property |
| λliquid | 0.08 | W/m×K | 444.77 | Calculated Property |
| λliquid | 0.08 | W/m×K | 487.54 | Calculated Property |
| λliquid | 0.07 | W/m×K | 530.31 | Calculated Property |
| λliquid | 0.07 | W/m×K | 573.07 | Calculated Property |
| λliquid | 0.06 | W/m×K | 615.84 | Calculated Property |
Similar Compounds
![Ethanol, 2-[2-(2-methoxyethoxy)ethoxy]-.](data:image/png;base64,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)
Find more compounds similar to 2,5,8,11,14,17-Hexaoxaoctadecane.
Sources
- 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
- Crippen Method
- 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
- Enthalpy of Solvation of Monoglyme, Diglyme, Triglyme, Tetraglyme, and Pentaglyme in Mixtures of Water with N,N-Dimethylformamide at 298.15 K
- Joback Method
- McGowan Method
- NIST Webbook
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