- 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 ether
- Methyl isobutyl oxide
- 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).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- 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).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3078 | ChemSep v8.3 pure component data Compiled value | |
| μ | 1.41 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -107.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -266.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfusH° | 6.37 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 30.31 | kJ/mol | NIST |
| IE | 9.52 | eV | Relay (1.0) Calculated Property |
| log10WS | -1.01 | Relay (1.0) Calculated Property | |
| logPoct/wat | 1.289 | Crippen Calculated Property | |
| McVol | 87.180 | ml/mol | McGowan Calculated Property |
| Pc | 3410.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [556.00; 574.00] |
|
|
| Inp | 556.00 | NIST | |
| Inp | 559.00 | NIST | |
| Inp | 574.00 | NIST | |
| Inp | 556.00 | NIST | |
| Tboil | [331.70; 331.70] | K |
|
| Tboil | 331.70 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 331.70 | K | NIST |
| Tc | 497.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 141.51 | K | Relay (1.0) Calculated Property |
| UQi | 3.55 | ChemSep v8.3 pure component data Compiled value | |
| URi | 4.07 | ChemSep v8.3 pure component data Compiled value | |
| Vc | 0.329 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2720000 | ChemSep v8.3 pure component data Compiled value | |
| Zra | 0.27 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 28.02 | kJ/mol | 331.70 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [91.61; 319.71] | J/mol×K | [150.00; 1200.00] |
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 | 8.44800e+01 | |||
| Coefficient B | -5.73480e+02 | |||
| Coefficient C | 5.73724e+00 | |||
| Coefficient D | 3.60010e-04 | |||
| Coefficient E | -1.60260e-07 | |||
| Temperature range, min. | 150.00 | |||
| Temperature range, max. | 1200.00 | |||
| Cp,gas | 91.61 | J/mol×K | 150.00 | Calculated Property |
| Cp,gas | 123.78 | J/mol×K | 266.67 | Calculated Property |
| Cp,gas | 162.40 | J/mol×K | 383.33 | Calculated Property |
| Cp,gas | 197.80 | J/mol×K | 500.00 | Calculated Property |
| Cp,gas | 228.27 | J/mol×K | 616.67 | Calculated Property |
| Cp,gas | 254.01 | J/mol×K | 733.33 | Calculated Property |
| Cp,gas | 275.58 | J/mol×K | 850.00 | Calculated Property |
| Cp,gas | 293.46 | J/mol×K | 966.67 | Calculated Property |
| Cp,gas | 308.07 | J/mol×K | 1083.33 | Calculated Property |
| Cp,gas | 319.71 | J/mol×K | 1200.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [189.35; 217.77] | J/mol×K | [298.15; 370.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 1.56890e+02 | |||
| Coefficient B | 4.81870e+02 | |||
| Coefficient C | -3.72796e+00 | |||
| Coefficient D | 2.32920e-02 | |||
| Coefficient E | -1.52190e-05 | |||
| Temperature range, min. | 298.15 | |||
| Temperature range, max. | 370.00 | |||
| Cp,liquid | 189.35 | J/mol×K | 298.15 | Calculated Property |
| Cp,liquid | 191.71 | J/mol×K | 306.13 | Calculated Property |
| Cp,liquid | 194.26 | J/mol×K | 314.12 | Calculated Property |
| Cp,liquid | 196.99 | J/mol×K | 322.10 | Calculated Property |
| Cp,liquid | 199.92 | J/mol×K | 330.08 | Calculated Property |
| Cp,liquid | 203.06 | J/mol×K | 338.07 | Calculated Property |
| Cp,liquid | 206.40 | J/mol×K | 346.05 | Calculated Property |
| Cp,liquid | 209.97 | J/mol×K | 354.03 | Calculated Property |
| Cp,liquid | 213.75 | J/mol×K | 362.02 | Calculated Property |
| Cp,liquid | 217.77 | J/mol×K | 370.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0053756; 0.0001218] | Pa×s | [150.00; 450.00] |
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 | -6.50490e+00 | |||
| Coefficient B | 7.76050e+02 | |||
| Coefficient C | -7.90510e-01 | |||
| Coefficient D | 2.94690e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 150.00 | |||
| Temperature range, max. | 450.00 | |||
| η | 0.0053756 | Pa×s | 150.00 | Calculated Property |
| η | 0.0018502 | Pa×s | 183.33 | Calculated Property |
| η | 0.0008793 | Pa×s | 216.67 | Calculated Property |
| η | 0.0005099 | Pa×s | 250.00 | Calculated Property |
| η | 0.0003378 | Pa×s | 283.33 | Calculated Property |
| η | 0.0002460 | Pa×s | 316.67 | Calculated Property |
| η | 0.0001921 | Pa×s | 350.00 | Calculated Property |
| η | 0.0001585 | Pa×s | 383.33 | Calculated Property |
| η | 0.0001365 | Pa×s | 416.67 | Calculated Property |
| η | 0.0001218 | Pa×s | 450.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [37.65; 0.00] | kJ/mol | [150.00; 497.00] |
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 | 4.28100e+01 | |||
| Coefficient B | 3.44360e-01 | |||
| Coefficient C | 5.08120e-02 | |||
| Coefficient D | -2.91680e-02 | |||
| Coefficient E | 1.45270e-02 | |||
| Critical temperature, Tc (K) | 4.97000e+02 | |||
| Temperature range, min. | 150.00 | |||
| Temperature range, max. | 497.00 | |||
| ΔvapH | 37.65 | kJ/mol | 150.00 | Calculated Property |
| ΔvapH | 36.05 | kJ/mol | 188.56 | Calculated Property |
| ΔvapH | 34.30 | kJ/mol | 227.11 | Calculated Property |
| ΔvapH | 32.37 | kJ/mol | 265.67 | Calculated Property |
| ΔvapH | 30.22 | kJ/mol | 304.22 | Calculated Property |
| ΔvapH | 27.76 | kJ/mol | 342.78 | Calculated Property |
| ΔvapH | 24.86 | kJ/mol | 381.33 | Calculated Property |
| ΔvapH | 21.28 | kJ/mol | 419.89 | Calculated Property |
| ΔvapH | 16.30 | kJ/mol | 458.44 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 497.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [245.76; 352.36] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| 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 | [2.11e-05; 3377.65] | kPa | [150.00; 497.00] |
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 | 6.09319e+01 | |||
| Coefficient B | -5.58477e+03 | |||
| Coefficient C | -6.90156e+00 | |||
| Coefficient D | 5.17779e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 150.00 | |||
| Temperature range, max. | 497.00 | |||
| Pvap | 2.11e-05 | kPa | 150.00 | Calculated Property |
| Pvap | 9.44e-03 | kPa | 188.56 | Calculated Property |
| Pvap | 0.43 | kPa | 227.11 | Calculated Property |
| Pvap | 5.75 | kPa | 265.67 | Calculated Property |
| Pvap | 36.31 | kPa | 304.22 | Calculated Property |
| Pvap | 142.97 | kPa | 342.78 | Calculated Property |
| Pvap | 411.09 | kPa | 381.33 | Calculated Property |
| Pvap | 952.25 | kPa | 419.89 | Calculated Property |
| Pvap | 1894.04 | kPa | 458.44 | Calculated Property |
| Pvap | 3377.65 | kPa | 497.00 | Calculated Property |
| Pvap | [1.30e-04; 3352.31] | kPa | [160.00; 497.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 6.16689e+01 | |||
| Coefficient B | -5.63276e+03 | |||
| Coefficient C | -7.00322e+00 | |||
| Coefficient D | 5.10989e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| 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 |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [859.40; 267.27] | kg/m3 | [150.00; 497.00] |
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 | 7.36161e+01 | |||
| Coefficient B | 2.75440e-01 | |||
| Coefficient C | 4.97000e+02 | |||
| Coefficient D | 2.75250e-01 | |||
| Temperature range, min. | 150.00 | |||
| Temperature range, max. | 497.00 | |||
| ρl | 859.40 | kg/m3 | 150.00 | Calculated Property |
| ρl | 827.97 | kg/m3 | 188.56 | Calculated Property |
| ρl | 794.86 | kg/m3 | 227.11 | Calculated Property |
| ρl | 759.67 | kg/m3 | 265.67 | Calculated Property |
| ρl | 721.81 | kg/m3 | 304.22 | Calculated Property |
| ρl | 680.33 | kg/m3 | 342.78 | Calculated Property |
| ρl | 633.62 | kg/m3 | 381.33 | Calculated Property |
| ρl | 578.41 | kg/m3 | 419.89 | Calculated Property |
| ρl | 505.82 | kg/m3 | 458.44 | Calculated Property |
| ρl | 267.27 | kg/m3 | 497.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 2.05e-05] | N/m | [150.00; 493.88] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K | |||
| Coefficient A | -1.09650e-02 | |||
| Coefficient B | 3.63670e+01 | |||
| Coefficient C | -3.31440e+00 | |||
| Coefficient D | 7.17930e-04 | |||
| Coefficient E | -6.66210e-06 | |||
| Comment | Range stopped where the equation turns negative; ChemSep gives it to 497 K. | |||
| Temperature range, min. | 150.00 | |||
| Temperature range, max. | 493.88 | |||
| γ | 0.03 | N/m | 150.00 | Calculated Property |
| γ | 0.03 | N/m | 188.21 | Calculated Property |
| γ | 0.02 | N/m | 226.42 | Calculated Property |
| γ | 0.02 | N/m | 264.63 | Calculated Property |
| γ | 0.02 | N/m | 302.83 | Calculated Property |
| γ | 0.01 | N/m | 341.04 | Calculated Property |
| γ | 0.01 | N/m | 379.25 | Calculated Property |
| γ | 0.01 | N/m | 417.46 | Calculated Property |
| γ | 0.00 | N/m | 455.67 | Calculated Property |
| γ | 2.05e-05 | N/m | 493.88 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.01; 0.09] | W/m×K | [180.00; 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 | 1.60880e-04 | |||
| Coefficient B | 9.72310e-01 | |||
| Coefficient C | 4.71480e+02 | |||
| Coefficient D | 3.02810e+04 | |||
| Temperature range, min. | 180.00 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.01 | W/m×K | 180.00 | Calculated Property |
| λgas | 0.01 | W/m×K | 271.11 | Calculated Property |
| λgas | 0.02 | W/m×K | 362.22 | Calculated Property |
| λgas | 0.03 | W/m×K | 453.33 | Calculated Property |
| λgas | 0.04 | W/m×K | 544.44 | Calculated Property |
| λgas | 0.05 | W/m×K | 635.56 | Calculated Property |
| λgas | 0.06 | W/m×K | 726.67 | Calculated Property |
| λgas | 0.07 | W/m×K | 817.78 | Calculated Property |
| λgas | 0.08 | W/m×K | 908.89 | Calculated Property |
| λgas | 0.09 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.17; 0.10] | W/m×K | [150.00; 390.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K | |||
| Coefficient A | -1.66400e-01 | |||
| Coefficient B | 6.17730e+00 | |||
| Coefficient C | -1.03080e+00 | |||
| Coefficient D | -4.39400e-04 | |||
| Coefficient E | -9.92130e-07 | |||
| Temperature range, min. | 150.00 | |||
| Temperature range, max. | 390.00 | |||
| λliquid | 0.17 | W/m×K | 150.00 | Calculated Property |
| λliquid | 0.17 | W/m×K | 176.67 | Calculated Property |
| λliquid | 0.16 | W/m×K | 203.33 | Calculated Property |
| λliquid | 0.15 | W/m×K | 230.00 | Calculated Property |
| λliquid | 0.14 | W/m×K | 256.67 | Calculated Property |
| λliquid | 0.13 | W/m×K | 283.33 | Calculated Property |
| λliquid | 0.12 | W/m×K | 310.00 | Calculated Property |
| λliquid | 0.11 | W/m×K | 336.67 | Calculated Property |
| λliquid | 0.10 | W/m×K | 363.33 | Calculated Property |
| λliquid | 0.10 | W/m×K | 390.00 | 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
- 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
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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