- InChI
- InChI=1S/C5H12O/c1-5(2)4-6-3/h5H,4H2,1-3H3
- InChI Key
- ZYVYEJXMYBUCMN-UHFFFAOYSA-N
- Formula
- C5H12O
- SMILES
- COCC(C)C
- Molecular Weight1
- 88.15
- CAS
- 625-44-5
- Other Names
-
- 1-METHOXY-2-METHYL PROPANE
- 1-Methoxy-2-methyl-propane
- Ether, isobutyl methyl
- ISOBUTYL METHYL ETHER
- METHYL ISOBUTYL OXIDE
- Methyl isobutyl ether
- Cp,gas : Ideal gas 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).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- 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).
- Inp : Non-polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (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 |
|---|---|---|---|
| ΔfG° | -116.22 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -284.03 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 6.37 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 30.31 | kJ/mol | NIST |
| log10WS | -0.76 | Crippen Calculated Property | |
| logPoct/wat | 1.289 | Crippen Calculated Property | |
| McVol | 87.180 | ml/mol | McGowan Calculated Property |
| Pc | 3431.89 | kPa | Joback Calculated Property |
| Inp | [556.00; 574.00] |
|
|
| Inp | 556.00 | NIST | |
| Inp | 559.00 | NIST | |
| Inp | 574.00 | NIST | |
| Tboil | 331.70 | K | NIST |
| Tc | 504.03 | K | Joback Calculated Property |
| Tfus | 153.34 | K | Joback Calculated Property |
| Vc | 0.328 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [147.62; 198.08] | J/mol×K | [335.78; 504.03] |
|
| Cp,gas | 147.62 | J/mol×K | 335.78 | Joback Calculated Property |
| Cp,gas | 156.61 | J/mol×K | 363.82 | Joback Calculated Property |
| Cp,gas | 165.37 | J/mol×K | 391.86 | Joback Calculated Property |
| Cp,gas | 173.90 | J/mol×K | 419.91 | Joback Calculated Property |
| Cp,gas | 182.20 | J/mol×K | 447.95 | Joback Calculated Property |
| Cp,gas | 190.26 | J/mol×K | 475.99 | Joback Calculated Property |
| Cp,gas | 198.08 | J/mol×K | 504.03 | Joback Calculated Property |
| η | [0.0002086; 0.0058560] | Pa×s | [153.34; 335.78] |
|
| η | 0.0058560 | Pa×s | 153.34 | Joback Calculated Property |
| η | 0.0021208 | Pa×s | 183.75 | Joback Calculated Property |
| η | 0.0010248 | Pa×s | 214.15 | Joback Calculated Property |
| η | 0.0005934 | Pa×s | 244.56 | Joback Calculated Property |
| η | 0.0003877 | Pa×s | 274.97 | Joback Calculated Property |
| η | 0.0002758 | Pa×s | 305.37 | Joback Calculated Property |
| η | 0.0002086 | Pa×s | 335.78 | Joback Calculated Property |
| ΔvapH | 28.02 | kJ/mol | 331.70 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [245.76; 352.36] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.53216e+01 | |||
| Coefficient B | -3.19318e+03 | |||
| Coefficient C | -3.33630e+01 | |||
| Temperature range, min. | 245.76 | |||
| Temperature range, max. | 352.36 | |||
| Pvap | 1.33 | kPa | 245.76 | Calculated Property |
| Pvap | 2.95 | kPa | 257.60 | Calculated Property |
| Pvap | 6.03 | kPa | 269.45 | Calculated Property |
| Pvap | 11.50 | kPa | 281.29 | Calculated Property |
| Pvap | 20.69 | kPa | 293.14 | Calculated Property |
| Pvap | 35.36 | kPa | 304.98 | Calculated Property |
| Pvap | 57.78 | kPa | 316.83 | Calculated Property |
| Pvap | 90.79 | kPa | 328.67 | Calculated Property |
| Pvap | 137.76 | kPa | 340.52 | Calculated Property |
| Pvap | 202.66 | kPa | 352.36 | Calculated Property |
| Pvap | [1.30e-04; 3352.31] | kPa | [160.00; 497.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.16689e+01 | |||
| Coefficient B | -5.63276e+03 | |||
| Coefficient C | -7.00322e+00 | |||
| Coefficient D | 5.10989e-06 | |||
| Temperature range, min. | 160.00 | |||
| Temperature range, max. | 497.00 | |||
| Pvap | 1.30e-04 | kPa | 160.00 | Calculated Property |
| Pvap | 0.03 | kPa | 197.44 | Calculated Property |
| Pvap | 0.77 | kPa | 234.89 | Calculated Property |
| Pvap | 8.14 | kPa | 272.33 | Calculated Property |
| Pvap | 44.99 | kPa | 309.78 | Calculated Property |
| Pvap | 163.04 | kPa | 347.22 | Calculated Property |
| Pvap | 444.05 | kPa | 384.67 | Calculated Property |
| Pvap | 991.01 | kPa | 422.11 | Calculated Property |
| Pvap | 1918.87 | kPa | 459.56 | Calculated Property |
| Pvap | 3352.31 | kPa | 497.00 | Calculated Property |
Similar Compounds
![Propane, 1,1'-[methylenebis(oxy)]bis[2-methyl-.](data:image/png;base64,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)
Find more compounds similar to Propane, 1-methoxy-2-methyl-.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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