- InChI
- InChI=1S/C5H12O/c1-3-5-6-4-2/h3-5H2,1-2H3
- InChI Key
- NVJUHMXYKCUMQA-UHFFFAOYSA-N
- Formula
- C5H12O
- SMILES
- CCCOCC
- Molecular Weight1
- 88.15
- CAS
- 628-32-0
- Other Names
-
- 1-ETHOXYPROPANE
- Ether, ethyl propyl
- Ethyl n-propyl ether
- Ethyl propyl ether
- PROPYL ETHYL ETHER
- UN 2615
- n-C3H7OC2H5
- 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).
- 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).
- 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).
- Pvap : Vapor pressure (kPa).
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°gas : Molar entropy at standard conditions (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).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3330 | KDB | |
| ΔcH°liquid | -3378.97 | kJ/mol | NIST |
| μ | 1.20 | debye | KDB |
| ΔfG° | -125.50 | kJ/mol | KDB |
| ΔfH°gas | -272.20 ± 1.20 | kJ/mol | NIST |
| ΔfH°liquid | -303.60 ± 1.20 | kJ/mol | NIST |
| ΔfusH° | 9.89 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [31.39; 31.57] | kJ/mol |
|
| ΔvapH° | Outlier 31.57 | kJ/mol | NIST |
| ΔvapH° | 31.39 | kJ/mol | NIST |
| ΔvapH° | 31.40 | kJ/mol | NIST |
| ΔvapH° | 31.40 | kJ/mol | NIST |
| ΔvapH° | 31.43 ± 0.11 | kJ/mol | NIST |
| ΔvapH° | 31.40 ± 0.10 | kJ/mol | NIST |
| IE | 9.50 ± 0.10 | eV | NIST |
| log10WS | [-0.66; -0.66] |
|
|
| log10WS | -0.66 | Aq. Sol... | |
| log10WS | -0.66 | Estimat... | |
| logPoct/wat | 1.433 | Crippen Calculated Property | |
| McVol | 87.180 | ml/mol | McGowan Calculated Property |
| Pc | [3250.00; 3370.00] | kPa |
|
| Pc | 3370.00 | kPa | KDB |
| Pc | 3370.00 ± 6.00 | kPa | NIST |
| Pc | 3250.00 ± 40.53 | kPa | NIST |
| ρc | 260.13 ± 1.76 | kg/m3 | NIST |
| Inp | [566.50; 590.00] |
|
|
| Inp | 590.00 | NIST | |
| Inp | 566.50 | NIST | |
| Inp | 572.10 | NIST | |
| Inp | 590.00 | NIST | |
| S°gas | 388.10 | J/mol×K | NIST |
| S°liquid | 295.00 | J/mol×K | NIST |
| Tboil | [336.30; 336.80] | K |
|
| Tboil | 336.36 | K | KDB |
| Tboil | 336.80 | K | NIST |
| Tboil | 336.30 | K | NIST |
| Tboil | 336.40 ± 0.50 | K | NIST |
| Tc | [500.20; 500.60] | K |
|
| Tc | 500.23 | K | KDB |
| Tc | 500.20 | K | NIST |
| Tc | 500.23 ± 0.20 | K | NIST |
| Tc | 500.60 ± 0.50 | K | NIST |
| Tfus | [145.60; 146.45] | K |
|
| Tfus | 145.60 | K | KDB |
| Tfus | 145.90 | K | Aq. Sol... |
| Tfus | 146.45 ± 0.40 | K | NIST |
| Ttriple | 145.65 ± 0.05 | K | NIST |
| Vc | 0.339 | m3/kmol | KDB |
| Zc | 0.2746780 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [147.83; 196.68] | J/mol×K | [336.22; 500.48] |
|
| Cp,gas | 147.83 | J/mol×K | 336.22 | Joback Calculated Property |
| Cp,gas | 156.52 | J/mol×K | 363.60 | Joback Calculated Property |
| Cp,gas | 164.99 | J/mol×K | 390.97 | Joback Calculated Property |
| Cp,gas | 173.24 | J/mol×K | 418.35 | Joback Calculated Property |
| Cp,gas | 181.27 | J/mol×K | 445.73 | Joback Calculated Property |
| Cp,gas | 189.09 | J/mol×K | 473.10 | Joback Calculated Property |
| Cp,gas | 196.68 | J/mol×K | 500.48 | Joback Calculated Property |
| Cp,liquid | [197.20; 197.50] | J/mol×K | [298.15; 298.15] |
|
| Cp,liquid | 197.20 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 197.50 | J/mol×K | 298.15 | NIST |
| η | [0.0002124; 0.0030953] | Pa×s | [168.34; 336.22] |
|
| η | 0.0030953 | Pa×s | 168.34 | Joback Calculated Property |
| η | 0.0014407 | Pa×s | 196.32 | Joback Calculated Property |
| η | 0.0008115 | Pa×s | 224.30 | Joback Calculated Property |
| η | 0.0005192 | Pa×s | 252.28 | Joback Calculated Property |
| η | 0.0003631 | Pa×s | 280.26 | Joback Calculated Property |
| η | 0.0002710 | Pa×s | 308.24 | Joback Calculated Property |
| η | 0.0002124 | Pa×s | 336.22 | Joback Calculated Property |
| ΔfusH | [8.39; 8.39] | kJ/mol | [145.65; 145.70] |
|
| ΔfusH | 8.39 | kJ/mol | 145.65 | NIST |
| ΔfusH | 8.39 | kJ/mol | 145.70 | NIST |
| ΔfusH | 8.39 | kJ/mol | 145.70 | NIST |
| ΔvapH | [28.94; 33.00] | kJ/mol | [311.50; 336.30] |
|
| ΔvapH | 33.00 | kJ/mol | 311.50 | NIST |
| ΔvapH | 29.00 | kJ/mol | 311.50 | NIST |
| ΔvapH | 31.60 | kJ/mol | 314.00 | NIST |
| ΔvapH | 28.94 | kJ/mol | 336.30 | NIST |
| ρl | 733.00 | kg/m3 | 293.00 | KDB |
| ΔfusS | 57.64 | J/mol×K | 145.65 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [250.01; 357.64] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.53548e+01 | |||
| Coefficient B | -3.24200e+03 | |||
| Coefficient C | -3.48390e+01 | |||
| Temperature range, min. | 250.01 | |||
| Temperature range, max. | 357.64 | |||
| Pvap | 1.33 | kPa | 250.01 | Calculated Property |
| Pvap | 2.95 | kPa | 261.97 | Calculated Property |
| Pvap | 6.02 | kPa | 273.93 | Calculated Property |
| Pvap | 11.48 | kPa | 285.89 | Calculated Property |
| Pvap | 20.66 | kPa | 297.85 | Calculated Property |
| Pvap | 35.31 | kPa | 309.80 | Calculated Property |
| Pvap | 57.72 | kPa | 321.76 | Calculated Property |
| Pvap | 90.72 | kPa | 333.72 | Calculated Property |
| Pvap | 137.70 | kPa | 345.68 | Calculated Property |
| Pvap | 202.65 | kPa | 357.64 | Calculated Property |
| Pvap | [7.50e-07; 3410.31] | kPa | [145.65; 500.23] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.32471e+02 | |||
| Coefficient B | -8.24837e+03 | |||
| Coefficient C | -1.81397e+01 | |||
| Coefficient D | 1.95507e-05 | |||
| Temperature range, min. | 145.65 | |||
| Temperature range, max. | 500.23 | |||
| Pvap | 7.50e-07 | kPa | 145.65 | Calculated Property |
| Pvap | 2.17e-03 | kPa | 185.05 | Calculated Property |
| Pvap | 0.22 | kPa | 224.45 | Calculated Property |
| Pvap | 4.20 | kPa | 263.84 | Calculated Property |
| Pvap | 30.21 | kPa | 303.24 | Calculated Property |
| Pvap | 123.68 | kPa | 342.64 | Calculated Property |
| Pvap | 359.27 | kPa | 382.04 | Calculated Property |
| Pvap | 846.38 | kPa | 421.43 | Calculated Property |
| Pvap | 1759.30 | kPa | 460.83 | Calculated Property |
| Pvap | 3410.31 | kPa | 500.23 | Calculated Property |
Similar Compounds
![CH3O[CH2CH2CH2O]3CH3.](data:image/png;base64,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)
Find more compounds similar to Propane, 1-ethoxy-.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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that the value is more than 2 standard deviations away from the
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