- InChI
- InChI=1S/C11H24O/c1-3-4-5-6-7-8-9-10-11-12-2/h3-11H2,1-2H3
- InChI Key
- JPEWDCTZJFUITH-UHFFFAOYSA-N
- Formula
- C11H24O
- SMILES
- CCCCCCCCCCOC
- Molecular Weight1
- 172.31
- Other Names
-
- Decane, 1-methoxy-
- Decyl methyl ether
- Ether, decyl methyl
- Methyl n-decyl ether
- ω : Acentric Factor.
- 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).
- 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).
- Pc : Critical Pressure (kPa).
- 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).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (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.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.5919 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ΔcH°liquid | -7315.18 | kJ/mol | NIST |
| ΔfG° | -63.26 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -381.10 ± 2.10 | kJ/mol | NIST |
| ΔfH°liquid | -443.40 ± 2.10 | kJ/mol | NIST |
| ΔfusH° | 25.43 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [62.30; 62.60] | kJ/mol |
|
| ΔvapH° | 62.30 | kJ/mol | NIST |
| ΔvapH° | 62.60 | kJ/mol | NIST |
| ΔvapH° | 62.30 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 62.30 ± 0.30 | kJ/mol | NIST |
| IE | 9.45 | eV | Relay (1.0) Calculated Property |
| log10WS | -4.50 | Relay (1.0) Calculated Property | |
| logPoct/wat | 3.773 | Crippen Calculated Property | |
| McVol | 171.720 | ml/mol | McGowan Calculated Property |
| Pc | 1934.29 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Inp | [1227.30; 1227.30] |
|
|
| Inp | 1227.30 | NIST | |
| Inp | 1227.30 | NIST | |
| S°liquid | 490.50 | J/mol×K | NIST |
| Tboil | 477.97 | K | Relay (1.0) Calculated Property |
| Tc | 657.97 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tfus | 253.15 | K | Relay (1.0) Calculated Property |
| Ttriple | [243.42; 243.42] | K |
|
| Ttriple | 243.42 ± 0.07 | K | NIST |
| Ttriple | 243.42 ± 0.07 | K | NIST |
| Vc | 0.666 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [370.50; 370.80] | J/mol×K | [298.15; 298.15] |
|
| Cp,liquid | 370.80 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 370.50 | J/mol×K | 298.15 | NIST |
| ΔfusH | [31.71; 31.72] | kJ/mol | [243.47; 243.50] |
|
| ΔfusH | 31.72 | kJ/mol | 243.47 | NIST |
| ΔfusH | 31.72 | kJ/mol | 243.47 | NIST |
| ΔfusH | 31.71 | kJ/mol | 243.50 | NIST |
| ΔfusH | 31.71 | kJ/mol | 243.50 | NIST |
| ΔvapH | [45.50; 57.00] | kJ/mol | [385.00; 406.00] |
|
| ΔvapH | 56.90 | kJ/mol | 385.00 | NIST |
| ΔvapH | 57.00 | kJ/mol | 406.00 | NIST |
| ΔvapH | 45.50 | kJ/mol | 406.00 | NIST |
| ΔfusS | [130.31; 130.31] | J/mol×K | [243.47; 243.47] |
|
| ΔfusS | 130.31 | J/mol×K | 243.47 | NIST |
| ΔfusS | 130.31 | J/mol×K | 243.47 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [254.24; 605.33] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 1.83890e+01 | |||
| Coefficient B | 9.85640e-01 | |||
| Coefficient C | -4.63600e-04 | |||
| Coefficient D | 6.49000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 254.24 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 311.94 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 364.48 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 412.09 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 454.95 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 493.27 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 527.27 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 557.14 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 583.09 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 605.33 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0043175; 0.0002076] | Pa×s | [235.96; 460.58] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.16677e+01 | |||
| Coefficient B | 1.46829e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 235.96 | |||
| Temperature range, max. | 460.58 | |||
| η | 0.0043175 | Pa×s | 235.96 | Calculated Property |
| η | 0.0023809 | Pa×s | 260.92 | Calculated Property |
| η | 0.0014567 | Pa×s | 285.88 | Calculated Property |
| η | 0.0009644 | Pa×s | 310.83 | Calculated Property |
| η | 0.0006789 | Pa×s | 335.79 | Calculated Property |
| η | 0.0005017 | Pa×s | 360.75 | Calculated Property |
| η | 0.0003855 | Pa×s | 385.71 | Calculated Property |
| η | 0.0003059 | Pa×s | 410.66 | Calculated Property |
| η | 0.0002492 | Pa×s | 435.62 | Calculated Property |
| η | 0.0002076 | Pa×s | 460.58 | Calculated Property |
Similar Compounds
Find more compounds similar to METHYL DECYL ETHER.
Sources
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
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