- InChI
- InChI=1S/C4H10O/c1-3-4-5-2/h3-4H2,1-2H3
- InChI Key
- VNKYTQGIUYNRMY-UHFFFAOYSA-N
- Formula
- C4H10O
- SMILES
- CCCOC
- Molecular Weight1
- 74.12
- CAS
- 557-17-5
- Other Names
-
- 1-METHOXY-PROPANE
- 1-Methoxypropane
- Ether, methyl propyl
- Methyl n-propyl ether
- Metopryl
- Neothyl
- Propane, 1-methoxy-
- Propyl methyl ether
- UN 2612
- n-C3H7OCH3
- «alpha»-Methoxy propane
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- ΔcH°gas : Standard gas enthalpy of combustion (kJ/mol).
- 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).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : 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).
- 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.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.2710; 0.3107] |
|
|
| ω | 0.3107 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.2770 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.2710 | KDB | |
| PAff | 814.90 | kJ/mol | NIST |
| BasG | 785.70 | kJ/mol | NIST |
| ΔcH°gas | -2765.50 ± 1.00 | kJ/mol | NIST |
| ΔcH°liquid | -2737.23 | kJ/mol | NIST |
| μ | [1.20; 1.24] | debye |
|
| μ | 1.24 | debye | ChemSep v8.3 pure component data Compiled value |
| μ | 1.20 | debye | KDB |
| ΔfG° | [-110.80; -110.00] | kJ/mol |
|
| ΔfG° | -110.80 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -110.00 | kJ/mol | KDB |
| ΔfH°gas | [-238.02; -237.70] | kJ/mol |
|
| ΔfH°gas | -237.90 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -237.90 | kJ/mol | KDB |
| ΔfH°gas | -238.02 ± 0.85 | kJ/mol | NIST |
| ΔfH°gas | -237.70 ± 1.10 | kJ/mol | NIST |
| ΔfH°liquid | -265.96 ± 0.84 | kJ/mol | NIST |
| ΔfusH° | 7.30 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [27.50; 27.94] | kJ/mol |
|
| ΔvapH° | 27.90 | kJ/mol | NIST |
| ΔvapH° | 27.57 | kJ/mol | NIST |
| ΔvapH° | 27.60 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 27.50 | kJ/mol | NIST |
| ΔvapH° | 27.94 ± 0.16 | kJ/mol | NIST |
| ΔvapH° | 27.90 ± 0.20 | kJ/mol | NIST |
| IE | [9.41; 9.73] | eV |
|
| IE | 9.41 ± 0.07 | eV | NIST |
| IE | 9.73 | eV | NIST |
| log10WS | [-0.51; -0.39] |
|
|
| log10WS | -0.51 | Aq. Solubility Prediction | |
| log10WS | -0.39 | Estimated Solubility | |
| logPoct/wat | 1.043 | Crippen Calculated Property | |
| McVol | 73.090 | ml/mol | McGowan Calculated Property |
| Pc | [3800.70; 3801.00] | kPa |
|
| Pc | 3801.00 | kPa | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Pc | 3800.70 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 3801.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 3801.00 | kPa | KDB |
| Pc | 3801.00 ± 4.00 | kPa | NIST |
| Ptriple | 2.90e-06 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [497.00; 512.00] |
|
|
| Inp | 497.00 | NIST | |
| Inp | 498.00 | NIST | |
| Inp | 499.00 | NIST | |
| Inp | 512.00 | NIST | |
| Ip | [644.00; 644.00] |
|
|
| Ip | 644.00 | NIST | |
| Ip | 644.00 | NIST | |
| S°gas | 352.00 | J/mol×K | NIST |
| S°liquid | 262.90 | J/mol×K | NIST |
| Tboil | [311.70; 312.29] | K |
|
| Tboil | 312.29 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 312.20 | K | KDB |
| Tboil | 311.70 | K | NIST |
| Tboil | 312.20 | K | NIST |
| Tboil | 311.80 ± 1.00 | K | NIST |
| Tc | [472.00; 476.30] | K |
|
| Tc | 476.20 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Tc | 472.00 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 472.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 476.25 | K | KDB |
| Tc | 476.30 | K | NIST |
| Tc | 476.25 ± 0.20 | K | NIST |
| Tfus | [123.15; 157.00] | K |
|
| Tfus | 123.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 157.00 | K | KDB |
| Ttriple | [133.97; 133.97] | K |
|
| Ttriple | 133.97 | K | ChemSep v8.3 pure component data Compiled value |
| Ttriple | 133.97 ± 0.05 | K | NIST |
| Ttriple | 133.97 ± 0.05 | K | NIST |
| Ttriple | 133.97 ± 0.05 | K | NIST |
| UQi | 3.02 | ChemSep v8.3 pure component data Compiled value | |
| URi | 3.39 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.274; 0.274] | m3/kmol |
|
| Vc | 0.274 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.274 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.274 | m3/kmol | KDB |
| Zc | [0.2630130; 0.2650000] |
|
|
| Zc | 0.2650000 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.2630130 | KDB | |
| Zra | 0.27 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [165.30; 165.40] | J/mol×K | [298.15; 298.15] |
|
| Cp,liquid | 165.40 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 165.30 | J/mol×K | 298.15 | NIST |
| ΔfusH | [7.67; 7.67] | kJ/mol | [133.97; 134.00] |
|
| ΔfusH | 7.67 | kJ/mol | 133.97 | NIST |
| ΔfusH | 7.67 | kJ/mol | 133.97 | NIST |
| ΔfusH | 7.67 | kJ/mol | 134.00 | NIST |
| ΔfusH | 7.67 | kJ/mol | 134.00 | NIST |
| ΔvapH | [26.70; 31.00] | kJ/mol | [290.50; 438.50] |
|
| ΔvapH | 29.70 | kJ/mol | 290.50 | NIST |
| ΔvapH | 29.70 | kJ/mol | 292.50 | NIST |
| ΔvapH | 30.70 | kJ/mol | 297.00 | NIST |
| ΔvapH | 31.00 | kJ/mol | 311.70 | KDB |
| ΔvapH | 26.75 | kJ/mol | 312.20 | NIST |
| ΔvapH | 27.20 | kJ/mol | 366.00 | NIST |
| ΔvapH | 26.70 | kJ/mol | 438.50 | NIST |
| ρl | 738.00 | kg/m3 | 293.00 | KDB |
| ΔfusS | [57.25; 57.25] | J/mol×K | [133.97; 133.97] |
|
| ΔfusS | 57.25 | J/mol×K | 133.97 | NIST |
| ΔfusS | 57.25 | J/mol×K | 133.97 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [94.17; 264.06] | J/mol×K | [133.97; 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 | 9.36680e+01 | |||
| Coefficient B | -9.26820e+02 | |||
| Coefficient C | 6.28124e+00 | |||
| Coefficient D | -4.81800e-04 | |||
| Coefficient E | 1.44000e-07 | |||
| Temperature range, min. | 133.97 | |||
| Temperature range, max. | 1200.00 | |||
| Cp,gas | 94.17 | J/mol×K | 133.97 | Calculated Property |
| Cp,gas | 105.81 | J/mol×K | 252.42 | Calculated Property |
| Cp,gas | 131.13 | J/mol×K | 370.87 | Calculated Property |
| Cp,gas | 159.42 | J/mol×K | 489.31 | Calculated Property |
| Cp,gas | 185.20 | J/mol×K | 607.76 | Calculated Property |
| Cp,gas | 207.08 | J/mol×K | 726.21 | Calculated Property |
| Cp,gas | 225.27 | J/mol×K | 844.66 | Calculated Property |
| Cp,gas | 240.38 | J/mol×K | 963.10 | Calculated Property |
| Cp,gas | 253.11 | J/mol×K | 1081.55 | Calculated Property |
| Cp,gas | 264.06 | J/mol×K | 1200.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [140.83; 168.51] | J/mol×K | [133.97; 312.20] |
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 | 1.36920e+02 | |||
| Coefficient B | 4.39700e+01 | |||
| Coefficient C | -1.82136e+00 | |||
| Coefficient D | 2.49920e-02 | |||
| Coefficient E | -2.73840e-05 | |||
| Temperature range, min. | 133.97 | |||
| Temperature range, max. | 312.20 | |||
| Cp,liquid | 140.83 | J/mol×K | 133.97 | Calculated Property |
| Cp,liquid | 142.18 | J/mol×K | 153.77 | Calculated Property |
| Cp,liquid | 143.91 | J/mol×K | 173.58 | Calculated Property |
| Cp,liquid | 146.08 | J/mol×K | 193.38 | Calculated Property |
| Cp,liquid | 148.72 | J/mol×K | 213.18 | Calculated Property |
| Cp,liquid | 151.85 | J/mol×K | 232.99 | Calculated Property |
| Cp,liquid | 155.47 | J/mol×K | 252.79 | Calculated Property |
| Cp,liquid | 159.52 | J/mol×K | 272.59 | Calculated Property |
| Cp,liquid | 163.91 | J/mol×K | 292.40 | Calculated Property |
| Cp,liquid | 168.51 | J/mol×K | 312.20 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0063942; 0.0002124] | Pa×s | [133.97; 312.20] |
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 | -1.13010e+01 | |||
| Coefficient B | 8.02090e+02 | |||
| Coefficient C | 5.49380e-02 | |||
| Coefficient D | -4.18440e-07 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 133.97 | |||
| Temperature range, max. | 312.20 | |||
| η | 0.0063942 | Pa×s | 133.97 | Calculated Property |
| η | 0.0029729 | Pa×s | 153.77 | Calculated Property |
| η | 0.0016461 | Pa×s | 173.58 | Calculated Property |
| η | 0.0010285 | Pa×s | 193.38 | Calculated Property |
| η | 0.0007010 | Pa×s | 213.18 | Calculated Property |
| η | 0.0005097 | Pa×s | 232.99 | Calculated Property |
| η | 0.0003894 | Pa×s | 252.79 | Calculated Property |
| η | 0.0003092 | Pa×s | 272.59 | Calculated Property |
| η | 0.0002531 | Pa×s | 292.40 | Calculated Property |
| η | 0.0002124 | Pa×s | 312.20 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [37.25; 12.15] | kJ/mol | [133.97; 458.24] |
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 | 4.42528e+01 | |||
| Coefficient B | 5.86164e-01 | |||
| Coefficient C | -3.78014e-01 | |||
| Coefficient D | 5.82618e-01 | |||
| Coefficient E | -4.40041e-01 | |||
| Critical temperature, Tc (K) | 4.72000e+02 | |||
| Temperature range, min. | 133.97 | |||
| Temperature range, max. | 458.24 | |||
| ΔvapH | 37.25 | kJ/mol | 133.97 | Calculated Property |
| ΔvapH | 35.32 | kJ/mol | 170.00 | Calculated Property |
| ΔvapH | 33.30 | kJ/mol | 206.03 | Calculated Property |
| ΔvapH | 31.20 | kJ/mol | 242.06 | Calculated Property |
| ΔvapH | 28.98 | kJ/mol | 278.09 | Calculated Property |
| ΔvapH | 26.65 | kJ/mol | 314.12 | Calculated Property |
| ΔvapH | 24.17 | kJ/mol | 350.15 | Calculated Property |
| ΔvapH | 21.41 | kJ/mol | 386.18 | Calculated Property |
| ΔvapH | 18.03 | kJ/mol | 422.21 | Calculated Property |
| ΔvapH | 12.15 | kJ/mol | 458.24 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [236.43; 331.31] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.33135e+01 | |||
| Coefficient B | -1.96855e+03 | |||
| Coefficient C | -8.53040e+01 | |||
| Temperature range, min. | 236.43 | |||
| Temperature range, max. | 331.31 | |||
| Pvap | 1.33 | kPa | 236.43 | Calculated Property |
| Pvap | 3.12 | kPa | 246.97 | Calculated Property |
| Pvap | 6.57 | kPa | 257.51 | Calculated Property |
| Pvap | 12.70 | kPa | 268.06 | Calculated Property |
| Pvap | 22.86 | kPa | 278.60 | Calculated Property |
| Pvap | 38.71 | kPa | 289.14 | Calculated Property |
| Pvap | 62.24 | kPa | 299.68 | Calculated Property |
| Pvap | 95.71 | kPa | 310.23 | Calculated Property |
| Pvap | 141.63 | kPa | 320.77 | Calculated Property |
| Pvap | 202.64 | kPa | 331.31 | Calculated Property |
| Pvap | [5.89e-06; 3454.35] | kPa | [133.97; 472.00] |
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 | 5.29049e+01 | |||
| Coefficient B | -4.96863e+03 | |||
| Coefficient C | -5.70304e+00 | |||
| Coefficient D | 3.96217e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 476.25 K. | |||
| Temperature range, min. | 133.97 | |||
| Temperature range, max. | 472.00 | |||
| Pvap | 5.89e-06 | kPa | 133.97 | Calculated Property |
| Pvap | 5.06e-03 | kPa | 171.53 | Calculated Property |
| Pvap | 0.32 | kPa | 209.09 | Calculated Property |
| Pvap | 4.90 | kPa | 246.65 | Calculated Property |
| Pvap | 33.85 | kPa | 284.21 | Calculated Property |
| Pvap | 140.47 | kPa | 321.76 | Calculated Property |
| Pvap | 416.05 | kPa | 359.32 | Calculated Property |
| Pvap | 977.45 | kPa | 396.88 | Calculated Property |
| Pvap | 1949.47 | kPa | 434.44 | Calculated Property |
| Pvap | 3454.35 | kPa | 472.00 | Calculated Property |
| Pvap | [7.89; 3813.44] | kPa | [254.15; 476.20] |
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 | 7.97043e+01 | |||
| Coefficient B | -5.82130e+03 | |||
| Coefficient C | -1.00118e+01 | |||
| Coefficient D | 1.10139e-05 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 254.15 | |||
| Temperature range, max. | 476.20 | |||
| Pvap | 7.89 | kPa | 254.15 | Calculated Property |
| Pvap | 27.39 | kPa | 278.82 | Calculated Property |
| Pvap | 74.95 | kPa | 303.49 | Calculated Property |
| Pvap | 172.09 | kPa | 328.17 | Calculated Property |
| Pvap | 346.44 | kPa | 352.84 | Calculated Property |
| Pvap | 631.28 | kPa | 377.51 | Calculated Property |
| Pvap | 1066.09 | kPa | 402.18 | Calculated Property |
| Pvap | 1698.61 | kPa | 426.86 | Calculated Property |
| Pvap | 2588.57 | kPa | 451.53 | Calculated Property |
| Pvap | 3813.44 | kPa | 476.20 | Calculated Property |
| Pvap | [19.92; 102.65] | kPa | [272.60; 312.49] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.30960e+01 | |||
| Coefficient B | -2.08059e+03 | |||
| Coefficient C | -6.66910e+01 | |||
| Reference | Bingham, 1910 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 272.60 | |||
| Temperature range, max. | 312.49 | |||
| Pvap | 19.92 | kPa | 272.60 | Calculated Property |
| Pvap | 24.64 | kPa | 277.03 | Calculated Property |
| Pvap | 30.22 | kPa | 281.46 | Calculated Property |
| Pvap | 36.76 | kPa | 285.90 | Calculated Property |
| Pvap | 44.37 | kPa | 290.33 | Calculated Property |
| Pvap | 53.16 | kPa | 294.76 | Calculated Property |
| Pvap | 63.26 | kPa | 299.19 | Calculated Property |
| Pvap | 74.79 | kPa | 303.63 | Calculated Property |
| Pvap | 87.88 | kPa | 308.06 | Calculated Property |
| Pvap | 102.65 | kPa | 312.49 | Calculated Property |
| Pvap | [19.92; 102.65] | kPa | [272.60; 312.49] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.30960e+01 | |||
| Coefficient B | -2.08059e+03 | |||
| Coefficient C | -6.66910e+01 | |||
| Reference | Bingham, 1910, 2 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 272.60 | |||
| Temperature range, max. | 312.49 | |||
| Pvap | 19.92 | kPa | 272.60 | Calculated Property |
| Pvap | 24.64 | kPa | 277.03 | Calculated Property |
| Pvap | 30.22 | kPa | 281.46 | Calculated Property |
| Pvap | 36.76 | kPa | 285.90 | Calculated Property |
| Pvap | 44.37 | kPa | 290.33 | Calculated Property |
| Pvap | 53.16 | kPa | 294.76 | Calculated Property |
| Pvap | 63.26 | kPa | 299.19 | Calculated Property |
| Pvap | 74.79 | kPa | 303.63 | Calculated Property |
| Pvap | 87.88 | kPa | 308.06 | Calculated Property |
| Pvap | 102.65 | kPa | 312.49 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [893.16; 437.82] | kg/m3 | [133.97; 458.24] |
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 | 8.46988e+01 | |||
| Coefficient B | 2.89270e-01 | |||
| Coefficient C | 4.72000e+02 | |||
| Coefficient D | 3.18500e-01 | |||
| Temperature range, min. | 133.97 | |||
| Temperature range, max. | 458.24 | |||
| ρl | 893.16 | kg/m3 | 133.97 | Calculated Property |
| ρl | 858.72 | kg/m3 | 170.00 | Calculated Property |
| ρl | 822.85 | kg/m3 | 206.03 | Calculated Property |
| ρl | 785.22 | kg/m3 | 242.06 | Calculated Property |
| ρl | 745.34 | kg/m3 | 278.09 | Calculated Property |
| ρl | 702.49 | kg/m3 | 314.12 | Calculated Property |
| ρl | 655.45 | kg/m3 | 350.15 | Calculated Property |
| ρl | 601.97 | kg/m3 | 386.18 | Calculated Property |
| ρl | 536.71 | kg/m3 | 422.21 | Calculated Property |
| ρl | 437.82 | kg/m3 | 458.24 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 4.44e-04] | N/m | [133.97; 458.24] |
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 | -1.26510e-02 | |||
| Coefficient B | 2.09900e+01 | |||
| Coefficient C | -2.90430e+00 | |||
| Coefficient D | -4.95860e-04 | |||
| Coefficient E | -5.95190e-06 | |||
| Temperature range, min. | 133.97 | |||
| Temperature range, max. | 458.24 | |||
| γ | 0.04 | N/m | 133.97 | Calculated Property |
| γ | 0.04 | N/m | 170.00 | Calculated Property |
| γ | 0.03 | N/m | 206.03 | Calculated Property |
| γ | 0.02 | N/m | 242.06 | Calculated Property |
| γ | 0.02 | N/m | 278.09 | Calculated Property |
| γ | 0.02 | N/m | 314.12 | Calculated Property |
| γ | 0.01 | N/m | 350.15 | Calculated Property |
| γ | 0.01 | N/m | 386.18 | Calculated Property |
| γ | 0.00 | N/m | 422.21 | Calculated Property |
| γ | 4.44e-04 | N/m | 458.24 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.00; 0.09] | W/m×K | [133.97; 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 | 1.07180e-02 | |||
| Coefficient B | 4.85000e-01 | |||
| Coefficient C | 2.08390e+03 | |||
| Coefficient D | 2.83110e+05 | |||
| Temperature range, min. | 133.97 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.00 | W/m×K | 133.97 | Calculated Property |
| λgas | 0.01 | W/m×K | 230.20 | Calculated Property |
| λgas | 0.02 | W/m×K | 326.42 | Calculated Property |
| λgas | 0.03 | W/m×K | 422.65 | Calculated Property |
| λgas | 0.04 | W/m×K | 518.87 | Calculated Property |
| λgas | 0.05 | W/m×K | 615.10 | Calculated Property |
| λgas | 0.06 | W/m×K | 711.32 | Calculated Property |
| λgas | 0.07 | W/m×K | 807.55 | Calculated Property |
| λgas | 0.08 | W/m×K | 903.77 | Calculated Property |
| λgas | 0.09 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.20; 0.09] | W/m×K | [123.15; 423.15] |
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 | -7.97880e-03 | |||
| Coefficient B | 3.90010e+00 | |||
| Coefficient C | -1.42240e+00 | |||
| Coefficient D | -1.06930e-03 | |||
| Coefficient E | -2.53150e-06 | |||
| Temperature range, min. | 123.15 | |||
| Temperature range, max. | 423.15 | |||
| λliquid | 0.20 | W/m×K | 123.15 | Calculated Property |
| λliquid | 0.19 | W/m×K | 156.48 | Calculated Property |
| λliquid | 0.18 | W/m×K | 189.82 | Calculated Property |
| λliquid | 0.16 | W/m×K | 223.15 | Calculated Property |
| λliquid | 0.15 | W/m×K | 256.48 | Calculated Property |
| λliquid | 0.14 | W/m×K | 289.82 | Calculated Property |
| λliquid | 0.12 | W/m×K | 323.15 | Calculated Property |
| λliquid | 0.11 | W/m×K | 356.48 | Calculated Property |
| λliquid | 0.10 | W/m×K | 389.82 | Calculated Property |
| λliquid | 0.09 | W/m×K | 423.15 | Calculated Property |
Similar Compounds
![CH3O[CH2CH2CH2O]3CH3.](data:image/png;base64,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)
Find more compounds similar to Methyl propyl ether.
Sources
- KDB Vapor Pressure Data
- IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 ChEDL chemicals 1.5.2, from Kudchadker, A. P.; Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 7. Oxygen Compounds Other Than Alkanols and Cycloalkanols. J. Chem. Eng. Data 2001, 46, 457-479.
- 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.
- 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
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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