- InChI
- InChI=1S/C6H14O/c1-5-7-6(2,3)4/h5H2,1-4H3
- InChI Key
- NUMQCACRALPSHD-UHFFFAOYSA-N
- Formula
- C6H14O
- SMILES
- CCOC(C)(C)C
- Molecular Weight1
- 102.17
- CAS
- 637-92-3
- Other Names
-
- 1,1-dimethylethyl ethyl ether
- 2-ethoxy-2-methylpropane
- 4,4-dimethyl-3-oxapentane
- Ether, tert-butyl ethyl
- Ethyl tert-butyl oxide
- ethyl 1,1-dimethylethyl ether
- ethyl tert-butyl ether
- t-Butyl ethyl ether
- tert-C4H9OC2H5
- tert-butyl ethyl ether
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- Csat : Molar heat capacity at saturation pressure (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).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- 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).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- 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).
- αdiff : Thermal diffusivity (m2/s).
- 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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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.2957; 0.3194] |
|
|
| ω | 0.3194 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.2957 | ChemSep v8.3 pure component data Compiled value | |
| PAff | 856.00 | kJ/mol | NIST |
| BasG | 826.90 | kJ/mol | NIST |
| μ | 1.22 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -121.70 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | [-317.80; -314.00] | kJ/mol |
|
| ΔfH°gas | -316.50 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -317.80 | kJ/mol | NIST |
| ΔfH°gas | -314.00 ± 2.00 | kJ/mol | NIST |
| ΔfH°liquid | -350.80 ± 2.60 | kJ/mol | NIST |
| ΔfusH° | 5.07 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [32.97; 33.10] | kJ/mol |
|
| ΔvapH° | 32.97 | kJ/mol | NIST |
| ΔvapH° | 33.10 ± 0.40 | kJ/mol | NIST |
| IE | 9.39 ± 0.01 | eV | NIST |
| logPoct/wat | 1.821 | Crippen Calculated Property | |
| McVol | 101.270 | ml/mol | McGowan Calculated Property |
| Pc | [2933.93; 3149.00] | kPa |
|
| Pc | 2934.00 | kPa | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Pc | 2933.93 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 3149.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 8.80e-04 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [586.00; 637.00] |
|
|
| Inp | 612.70 | NIST | |
| Inp | 612.00 | NIST | |
| Inp | Outlier 586.00 | NIST | |
| Inp | Outlier 587.00 | NIST | |
| Inp | 620.00 | NIST | |
| Inp | 624.00 | NIST | |
| Inp | 620.00 | NIST | |
| Inp | 637.00 | NIST | |
| Inp | 616.00 | NIST | |
| Inp | 615.40 | NIST | |
| Inp | 620.00 | NIST | |
| Inp | 621.00 | NIST | |
| Inp | 620.00 | NIST | |
| Inp | 612.70 | NIST | |
| Ip | [710.00; 710.00] |
|
|
| Ip | 710.00 | NIST | |
| Ip | 710.00 | NIST | |
| Tboil | [345.60; 346.30] | K |
|
| Tboil | 345.65 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 346.10 ± 0.50 | K | NIST |
| Tboil | 346.30 | K | NIST |
| Tboil | 345.60 | K | NIST |
| Tboil | 345.90 ± 0.30 | K | NIST |
| Tc | [509.40; 512.00] | K |
|
| Tc | 509.40 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Tc | 509.40 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 512.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [176.15; 179.15] | K |
|
| Tfus | 179.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 176.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 179.15 ± 0.20 | K | NIST |
| Ttriple | 179.15 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 4.17 | ChemSep v8.3 pure component data Compiled value | |
| URi | 4.74 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.382; 0.395] | m3/kmol |
|
| Vc | 0.395 | m3/kmol | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Vc | 0.394 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.382 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | [0.2720000; 0.2740000] |
|
|
| Zc | 0.2740000 | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value | |
| Zc | 0.2720000 | ChemSep v8.3 pure component data Compiled value | |
| Zra | 0.27 | ChemSep v8.3 pure component data Compiled value |
Cheméo can also estimate Log10 of Water solubility in mol/l for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.
Temperature Dependent Properties
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 100.00 | 751.23 |
| 288.15 | 100.00 | 746.2 |
| 293.15 | 100.00 | 741.05 |
| 298.15 | 100.00 | 735.9 |
| 303.15 | 100.00 | 730.67 |
| 308.15 | 100.00 | 725.44 |
| 313.15 | 100.00 | 720.14 |
| 318.15 | 100.00 | 714.82 |
| 323.15 | 100.00 | 709.43 |
| 328.15 | 100.00 | 703.95 |
| 333.15 | 100.00 | 698.45 |
| 283.15 | 5000.00 | 756.42 |
| 288.15 | 5000.00 | 751.53 |
| 293.15 | 5000.00 | 746.6 |
| 298.15 | 5000.00 | 741.67 |
| 303.15 | 5000.00 | 736.68 |
| 308.15 | 5000.00 | 731.69 |
| 313.15 | 5000.00 | 726.68 |
| 318.15 | 5000.00 | 721.59 |
| 323.15 | 5000.00 | 716.51 |
| 328.15 | 5000.00 | 711.38 |
| 333.15 | 5000.00 | 706.19 |
| 283.15 | 10000.00 | 761.33 |
| 288.15 | 10000.00 | 756.63 |
| 293.15 | 10000.00 | 751.89 |
| 298.15 | 10000.00 | 747.14 |
| 303.15 | 10000.00 | 742.38 |
| 308.15 | 10000.00 | 737.6 |
| 313.15 | 10000.00 | 732.78 |
| 318.15 | 10000.00 | 727.94 |
| 323.15 | 10000.00 | 723.13 |
| 328.15 | 10000.00 | 718.21 |
| 333.15 | 10000.00 | 713.35 |
| 283.15 | 15000.00 | 765.98 |
| 288.15 | 15000.00 | 761.42 |
| 293.15 | 15000.00 | 756.83 |
| 298.15 | 15000.00 | 752.27 |
| 303.15 | 15000.00 | 747.69 |
| 308.15 | 15000.00 | 743.07 |
| 313.15 | 15000.00 | 738.45 |
| 318.15 | 15000.00 | 733.82 |
| 323.15 | 15000.00 | 729.2 |
| 328.15 | 15000.00 | 724.52 |
| 333.15 | 15000.00 | 719.84 |
| 283.15 | 20000.00 | 770.36 |
| 288.15 | 20000.00 | 765.93 |
| 293.15 | 20000.00 | 761.5 |
| 298.15 | 20000.00 | 757.08 |
| 303.15 | 20000.00 | 752.63 |
| 308.15 | 20000.00 | 748.18 |
| 313.15 | 20000.00 | 743.71 |
| 318.15 | 20000.00 | 739.27 |
| 323.15 | 20000.00 | 734.81 |
| 328.15 | 20000.00 | 730.3 |
| 333.15 | 20000.00 | 725.83 |
| 283.15 | 25000.00 | 774.54 |
| 288.15 | 25000.00 | 770.23 |
| 293.15 | 25000.00 | 765.92 |
| 298.15 | 25000.00 | 761.61 |
| 303.15 | 25000.00 | 757.33 |
| 308.15 | 25000.00 | 753.01 |
| 313.15 | 25000.00 | 748.69 |
| 318.15 | 25000.00 | 744.39 |
| 323.15 | 25000.00 | 740.06 |
| 328.15 | 25000.00 | 735.75 |
| 333.15 | 25000.00 | 731.42 |
| 283.15 | 30000.00 | 778.52 |
| 288.15 | 30000.00 | 774.31 |
| 293.15 | 30000.00 | 770.13 |
| 298.15 | 30000.00 | 765.96 |
| 303.15 | 30000.00 | 761.74 |
| 308.15 | 30000.00 | 757.57 |
| 313.15 | 30000.00 | 753.36 |
| 318.15 | 30000.00 | 749.2 |
| 323.15 | 30000.00 | 745.02 |
| 328.15 | 30000.00 | 740.83 |
| 333.15 | 30000.00 | 736.64 |
| 283.15 | 35000.00 | 782.33 |
| 288.15 | 35000.00 | 778.21 |
| 293.15 | 35000.00 | 774.13 |
| 298.15 | 35000.00 | 770.04 |
| 303.15 | 35000.00 | 765.95 |
| 308.15 | 35000.00 | 761.9 |
| 313.15 | 35000.00 | 757.81 |
| 318.15 | 35000.00 | 753.76 |
| 323.15 | 35000.00 | 749.69 |
| 328.15 | 35000.00 | 745.64 |
| 333.15 | 35000.00 | 741.54 |
| 283.15 | 40000.00 | 785.98 |
| 288.15 | 40000.00 | 781.97 |
| 293.15 | 40000.00 | 777.97 |
| 298.15 | 40000.00 | 773.96 |
| 303.15 | 40000.00 | 769.98 |
| 308.15 | 40000.00 | 766.03 |
| 313.15 | 40000.00 | 762.03 |
| 318.15 | 40000.00 | 758.08 |
| 323.15 | 40000.00 | 754.13 |
| 328.15 | 40000.00 | 750.18 |
| 333.15 | 40000.00 | 746.21 |
| 283.15 | 45000.00 | 789.49 |
| 288.15 | 45000.00 | 785.55 |
| 293.15 | 45000.00 | 781.65 |
| 298.15 | 45000.00 | 777.75 |
| 303.15 | 45000.00 | 773.86 |
| 308.15 | 45000.00 | 769.97 |
| 313.15 | 45000.00 | 766.08 |
| 318.15 | 45000.00 | 762.23 |
| 323.15 | 45000.00 | 758.36 |
| 328.15 | 45000.00 | 754.48 |
| 333.15 | 45000.00 | 750.65 |
| 283.15 | 50000.00 | 792.89 |
| 288.15 | 50000.00 | 789.02 |
| 293.15 | 50000.00 | 785.19 |
| 298.15 | 50000.00 | 781.37 |
| 303.15 | 50000.00 | 777.57 |
| 308.15 | 50000.00 | 773.76 |
| 313.15 | 50000.00 | 769.94 |
| 318.15 | 50000.00 | 766.19 |
| 323.15 | 50000.00 | 762.39 |
| 328.15 | 50000.00 | 758.63 |
| 333.15 | 50000.00 | 754.86 |
| 283.15 | 55000.00 | 796.17 |
| 288.15 | 55000.00 | 792.37 |
| 293.15 | 55000.00 | 788.63 |
| 298.15 | 55000.00 | 784.85 |
| 303.15 | 55000.00 | 781.12 |
| 308.15 | 55000.00 | 777.4 |
| 313.15 | 55000.00 | 773.66 |
| 318.15 | 55000.00 | 769.98 |
| 323.15 | 55000.00 | 766.26 |
| 328.15 | 55000.00 | 762.55 |
| 333.15 | 55000.00 | 758.88 |
| 283.15 | 60000.00 | 799.33 |
| 288.15 | 60000.00 | 795.56 |
| 293.15 | 60000.00 | 791.91 |
| 298.15 | 60000.00 | 788.21 |
| 303.15 | 60000.00 | 784.56 |
| 308.15 | 60000.00 | 780.9 |
| 313.15 | 60000.00 | 777.23 |
| 318.15 | 60000.00 | 773.61 |
| 323.15 | 60000.00 | 770.0 |
| 328.15 | 60000.00 | 766.37 |
| 333.15 | 60000.00 | 762.77 |
| 283.15 | 65000.00 | 802.42 |
| 288.15 | 65000.00 | 798.71 |
| 293.15 | 65000.00 | 795.1 |
| 298.15 | 65000.00 | 791.48 |
| 303.15 | 65000.00 | 787.89 |
| 308.15 | 65000.00 | 784.29 |
| 313.15 | 65000.00 | 780.69 |
| 318.15 | 65000.00 | 777.13 |
| 323.15 | 65000.00 | 773.58 |
| 328.15 | 65000.00 | 770.52 |
| 333.15 | 65000.00 | 766.51 |
| Reference | ||
Speed of sound, m/s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Speed of sound, m/s - Liquid |
| 293.15 | 10.00 | 1059.15 |
| 303.15 | 10.00 | 1012.95 |
| 313.15 | 10.00 | 967.71 |
| 323.15 | 20.00 | 923.32 |
| 333.15 | 40.00 | 879.69 |
| 343.15 | 60.00 | 836.71 |
| 353.15 | 90.00 | 794.25 |
| 363.15 | 130.00 | 752.18 |
| 373.15 | 180.00 | 710.37 |
| 383.15 | 250.00 | 668.66 |
| 393.15 | 340.00 | 626.87 |
| 403.15 | 440.00 | 584.83 |
| 413.15 | 570.00 | 542.3 |
| 423.15 | 730.00 | 499.06 |
| 433.15 | 920.00 | 454.82 |
| 443.15 | 1150.00 | 409.25 |
| 453.15 | 1420.00 | 361.97 |
| 463.15 | 1750.00 | 312.51 |
| 473.15 | 2130.00 | 260.24 |
| 483.15 | 2570.00 | 204.36 |
| 488.15 | 2820.00 | 174.7 |
| 493.15 | 3090.00 | 143.64 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [104.95; 379.63] | J/mol×K | [179.15; 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 | 7.89150e+01 | |||
| Coefficient B | -4.87030e+02 | |||
| Coefficient C | 5.93524e+00 | |||
| Coefficient D | 2.53850e-04 | |||
| Coefficient E | -8.87900e-08 | |||
| Temperature range, min. | 179.15 | |||
| Temperature range, max. | 1200.00 | |||
| Cp,gas | 104.95 | J/mol×K | 179.15 | Calculated Property |
| Cp,gas | 155.42 | J/mol×K | 292.58 | Calculated Property |
| Cp,gas | 203.39 | J/mol×K | 406.01 | Calculated Property |
| Cp,gas | 243.85 | J/mol×K | 519.43 | Calculated Property |
| Cp,gas | 277.41 | J/mol×K | 632.86 | Calculated Property |
| Cp,gas | 305.39 | J/mol×K | 746.29 | Calculated Property |
| Cp,gas | 328.89 | J/mol×K | 859.72 | Calculated Property |
| Cp,gas | 348.73 | J/mol×K | 973.14 | Calculated Property |
| Cp,gas | 365.49 | J/mol×K | 1086.57 | Calculated Property |
| Cp,gas | 379.63 | J/mol×K | 1200.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [195.13; 255.76] | J/mol×K | [257.00; 377.00] |
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 | 1.35520e+02 | |||
| Coefficient B | 9.88070e+00 | |||
| Coefficient C | 1.78364e+00 | |||
| Coefficient D | 1.07700e-02 | |||
| Coefficient E | -7.60340e-06 | |||
| Temperature range, min. | 257.00 | |||
| Temperature range, max. | 377.00 | |||
| Cp,liquid | 195.13 | J/mol×K | 257.00 | Calculated Property |
| Cp,liquid | 200.63 | J/mol×K | 270.33 | Calculated Property |
| Cp,liquid | 206.45 | J/mol×K | 283.67 | Calculated Property |
| Cp,liquid | 212.61 | J/mol×K | 297.00 | Calculated Property |
| Cp,liquid | 219.08 | J/mol×K | 310.33 | Calculated Property |
| Cp,liquid | 225.86 | J/mol×K | 323.67 | Calculated Property |
| Cp,liquid | 232.93 | J/mol×K | 337.00 | Calculated Property |
| Cp,liquid | 240.29 | J/mol×K | 350.33 | Calculated Property |
| Cp,liquid | 247.90 | J/mol×K | 363.67 | Calculated Property |
| Cp,liquid | 255.76 | J/mol×K | 377.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0040280; 0.0001075] | Pa×s | [179.15; 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 | -1.20110e+01 | |||
| Coefficient B | 1.08980e+03 | |||
| Coefficient C | 8.10110e-02 | |||
| Coefficient D | -2.16880e-07 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 179.15 | |||
| Temperature range, max. | 450.00 | |||
| η | 0.0040280 | Pa×s | 179.15 | Calculated Property |
| η | 0.0016962 | Pa×s | 209.24 | Calculated Property |
| η | 0.0008882 | Pa×s | 239.34 | Calculated Property |
| η | 0.0005375 | Pa×s | 269.43 | Calculated Property |
| η | 0.0003597 | Pa×s | 299.53 | Calculated Property |
| η | 0.0002590 | Pa×s | 329.62 | Calculated Property |
| η | 0.0001969 | Pa×s | 359.72 | Calculated Property |
| η | 0.0001561 | Pa×s | 389.81 | Calculated Property |
| η | 0.0001279 | Pa×s | 419.91 | Calculated Property |
| η | 0.0001075 | Pa×s | 450.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [39.07; 11.38] | kJ/mol | [179.15; 496.38] |
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 | 4.58250e+01 | |||
| Coefficient B | 3.49787e-01 | |||
| Coefficient C | 1.37025e-01 | |||
| Coefficient D | -3.01886e-01 | |||
| Coefficient E | 2.19717e-01 | |||
| Critical temperature, Tc (K) | 5.12000e+02 | |||
| Temperature range, min. | 179.15 | |||
| Temperature range, max. | 496.38 | |||
| ΔvapH | 39.07 | kJ/mol | 179.15 | Calculated Property |
| ΔvapH | 37.48 | kJ/mol | 214.40 | Calculated Property |
| ΔvapH | 35.77 | kJ/mol | 249.65 | Calculated Property |
| ΔvapH | 33.91 | kJ/mol | 284.89 | Calculated Property |
| ΔvapH | 31.83 | kJ/mol | 320.14 | Calculated Property |
| ΔvapH | 29.46 | kJ/mol | 355.39 | Calculated Property |
| ΔvapH | 26.66 | kJ/mol | 390.64 | Calculated Property |
| ΔvapH | 23.22 | kJ/mol | 425.88 | Calculated Property |
| ΔvapH | 18.67 | kJ/mol | 461.13 | Calculated Property |
| ΔvapH | 11.38 | kJ/mol | 496.38 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [257.16; 367.48] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.53227e+01 | |||
| Coefficient B | -3.30527e+03 | |||
| Coefficient C | -3.73240e+01 | |||
| Temperature range, min. | 257.16 | |||
| Temperature range, max. | 367.48 | |||
| Pvap | 1.33 | kPa | 257.16 | Calculated Property |
| Pvap | 2.95 | kPa | 269.42 | Calculated Property |
| Pvap | 6.03 | kPa | 281.68 | Calculated Property |
| Pvap | 11.50 | kPa | 293.93 | Calculated Property |
| Pvap | 20.69 | kPa | 306.19 | Calculated Property |
| Pvap | 35.36 | kPa | 318.45 | Calculated Property |
| Pvap | 57.78 | kPa | 330.71 | Calculated Property |
| Pvap | 90.79 | kPa | 342.96 | Calculated Property |
| Pvap | 137.76 | kPa | 355.22 | Calculated Property |
| Pvap | 202.66 | kPa | 367.48 | Calculated Property |
| Pvap | [9.15e-04; 3269.76] | kPa | [179.15; 512.00] |
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 | 5.30144e+01 | |||
| Coefficient B | -5.56417e+03 | |||
| Coefficient C | -5.60132e+00 | |||
| Coefficient D | 3.38929e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 514 K. | |||
| Temperature range, min. | 179.15 | |||
| Temperature range, max. | 512.00 | |||
| Pvap | 9.15e-04 | kPa | 179.15 | Calculated Property |
| Pvap | 0.07 | kPa | 216.13 | Calculated Property |
| Pvap | 1.29 | kPa | 253.12 | Calculated Property |
| Pvap | 10.58 | kPa | 290.10 | Calculated Property |
| Pvap | 51.04 | kPa | 327.08 | Calculated Property |
| Pvap | 171.97 | kPa | 364.07 | Calculated Property |
| Pvap | 450.65 | kPa | 401.05 | Calculated Property |
| Pvap | 985.53 | kPa | 438.03 | Calculated Property |
| Pvap | 1886.72 | kPa | 475.02 | Calculated Property |
| Pvap | 3269.76 | kPa | 512.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [849.87; 428.17] | kg/m3 | [179.15; 496.38] |
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 | 7.59905e+01 | |||
| Coefficient B | 2.76190e-01 | |||
| Coefficient C | 5.12000e+02 | |||
| Coefficient D | 3.06020e-01 | |||
| Temperature range, min. | 179.15 | |||
| Temperature range, max. | 496.38 | |||
| ρl | 849.87 | kg/m3 | 179.15 | Calculated Property |
| ρl | 818.19 | kg/m3 | 214.40 | Calculated Property |
| ρl | 785.14 | kg/m3 | 249.65 | Calculated Property |
| ρl | 750.37 | kg/m3 | 284.89 | Calculated Property |
| ρl | 713.44 | kg/m3 | 320.14 | Calculated Property |
| ρl | 673.65 | kg/m3 | 355.39 | Calculated Property |
| ρl | 629.86 | kg/m3 | 390.64 | Calculated Property |
| ρl | 579.95 | kg/m3 | 425.88 | Calculated Property |
| ρl | 519.05 | kg/m3 | 461.13 | Calculated Property |
| ρl | 428.17 | kg/m3 | 496.38 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 5.54e-04] | N/m | [179.15; 496.38] |
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 | -9.75340e-03 | |||
| Coefficient B | 5.91450e+01 | |||
| Coefficient C | -3.43190e+00 | |||
| Coefficient D | 1.37270e-03 | |||
| Coefficient E | -7.88810e-06 | |||
| Temperature range, min. | 179.15 | |||
| Temperature range, max. | 496.38 | |||
| γ | 0.03 | N/m | 179.15 | Calculated Property |
| γ | 0.03 | N/m | 214.40 | Calculated Property |
| γ | 0.03 | N/m | 249.65 | Calculated Property |
| γ | 0.02 | N/m | 284.89 | Calculated Property |
| γ | 0.02 | N/m | 320.14 | Calculated Property |
| γ | 0.01 | N/m | 355.39 | Calculated Property |
| γ | 0.01 | N/m | 390.64 | Calculated Property |
| γ | 0.01 | N/m | 425.88 | Calculated Property |
| γ | 0.00 | N/m | 461.13 | Calculated Property |
| γ | 5.54e-04 | N/m | 496.38 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.01; 0.09] | W/m×K | [179.15; 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 | 5.87880e-05 | |||
| Coefficient B | 1.09070e+00 | |||
| Coefficient C | 2.35700e+02 | |||
| Coefficient D | 3.31500e+04 | |||
| Temperature range, min. | 179.15 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.01 | W/m×K | 179.15 | Calculated Property |
| λgas | 0.01 | W/m×K | 270.36 | Calculated Property |
| λgas | 0.02 | W/m×K | 361.56 | Calculated Property |
| λgas | 0.03 | W/m×K | 452.77 | Calculated Property |
| λgas | 0.04 | W/m×K | 543.97 | Calculated Property |
| λgas | 0.05 | W/m×K | 635.18 | Calculated Property |
| λgas | 0.06 | W/m×K | 726.38 | Calculated Property |
| λgas | 0.07 | W/m×K | 817.59 | Calculated Property |
| λgas | 0.08 | W/m×K | 908.79 | Calculated Property |
| λgas | 0.09 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.15; 0.09] | W/m×K | [179.15; 404.20] |
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 | -1.31600e-01 | |||
| Coefficient B | 1.17160e+01 | |||
| Coefficient C | -1.24780e+00 | |||
| Coefficient D | -2.46720e-04 | |||
| Coefficient E | -1.25190e-06 | |||
| Temperature range, min. | 179.15 | |||
| Temperature range, max. | 404.20 | |||
| λliquid | 0.15 | W/m×K | 179.15 | Calculated Property |
| λliquid | 0.14 | W/m×K | 204.16 | Calculated Property |
| λliquid | 0.14 | W/m×K | 229.16 | Calculated Property |
| λliquid | 0.13 | W/m×K | 254.17 | Calculated Property |
| λliquid | 0.12 | W/m×K | 279.17 | Calculated Property |
| λliquid | 0.11 | W/m×K | 304.18 | Calculated Property |
| λliquid | 0.11 | W/m×K | 329.18 | Calculated Property |
| λliquid | 0.10 | W/m×K | 354.19 | Calculated Property |
| λliquid | 0.09 | W/m×K | 379.19 | Calculated Property |
| λliquid | 0.09 | W/m×K | 404.20 | Calculated Property |
Similar Compounds
Find more compounds similar to Propane, 2-ethoxy-2-methyl-.
Mixtures
- Propane, 2-ethoxy-2-methyl- + Water
- Ethanol, 2-methoxy- + Propane, 2-ethoxy-2-methyl-
- Ethanol, 2-(2-methoxyethoxy)- + Propane, 2-ethoxy-2-methyl-
- Propane, 2-ethoxy-2-methyl- + Ethanol, 2-[2-(2-methoxyethoxy)ethoxy]-
- Propanenitrile + Propane, 2-ethoxy-2-methyl-
- Propane, 2-ethoxy-2-methyl- + Heptane
- 1-Hexene + Propane, 2-ethoxy-2-methyl-
- 1-Hexene + Propane, 2-ethoxy-2-methyl- + Heptane
- Thiophene + Propane, 2-ethoxy-2-methyl-
- Propane, 2-ethoxy-2-methyl- + o-Xylene
- Benzene, 1,3-dimethyl- + Propane, 2-ethoxy-2-methyl-
- p-Xylene + Propane, 2-ethoxy-2-methyl-
- Benzene + Propane, 2-ethoxy-2-methyl-
- Toluene + Propane, 2-ethoxy-2-methyl-
- Propane, 2-ethoxy-2-methyl- + Benzene, ethyl-
- Propane, 2-ethoxy-2-methyl- + Pentane, 2,2,4-trimethyl-
- 2-Propanol, 2-methyl- + Propane, 2-ethoxy-2-methyl-
- Ethanol + Propane, 2-ethoxy-2-methyl-
- Propane, 2-ethoxy-2-methyl- + Cyclohexane
- 1-Propanol + Propane, 2-ethoxy-2-methyl-
Find more mixtures with Propane, 2-ethoxy-2-methyl-.
Sources
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- 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
- Crippen Method
- Infinite dilution activity coefficient measurements by inert gas stripping method
- Vapor liquid equilibrium for binary system of diethyl sulfide + cyclohexane at 353.15 and 343.15 K and diethyl sulfide + 2-ethoxy-2-methylpropane at 343.15 and 333.15 K
- Vapor liquid equilibrium, densities, and interfacial tensions for the system ethyl 1,1-dimethylethyl ether (ETBE) + propan-1-ol
- Vapor liquid equilibrium for binary system of thiophene + 2,2,4-trimethylpentane at 343.15 and 353.15K and thiophene + 2-ethoxy-2-methylpropane at 333.15 and 343.15K
- Thermodynamics of fuels with a biosynthetic component (III): Vapor liquid equilibrium data for the ternary mixture ethyl 1, 1-dimethylethyl ether, n-heptane and 1-hexene at T = 313.15K
- Influence of temperature on thermodynamics of ethers + xylenes
- Phase equilibrium measurements for systems containing propanenitrile with tert-butyl ethyl ether and C4-hydrocarbons
- Azeotrope breaking for the system ethyl tert-butyl ether (ETBE) + ethanol at 313.15 K and excess properties at 298.15 K for mixtures of ETBE and ethanol with phosphonium-based ionic liquids
- Atmospheric densities and interfacial tensions for 1- alkanol (1-butanol to 1-octanol) + water and ether (MTBE, ETBE, DIPE, TAME and THP) + water demixed mixtures.
- Speed of sound measurement in ethyl tert-butyl ether and tert-amyl methyl ether by Brillouin light scattering
- Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
- Experimental and modeled volumetric behavior of linear and branched ethers
- High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
- Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
- Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
- New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
- Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
- Volumetric properties of binary mixtures of alkoxyethanols with ethyl tert-butyl ether at various temperatures
- Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
- The thermodynamics of vaporization of ethyl tert-butyl ether, isobutyl tert-butyl ether, and di-isopropyl ether
- Viscosities of binary mixtures of some n-ethoxyethanols with ethyl tert-butyl ether at T = (293.15, 298.15, and 303.15) K
- Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
- Thermodynamics of fuels with a bio-synthetic component (IV): (Vapor + liquid) equilibrium data for the ternary mixture (ethyl 1,1-dimethylethyl ether + 1-hexene + toluene) at T = 313.15 K
- Thermodynamics of biofuels: Excess enthalpies for binary mixtures involving ethyl 1,1-dimethylethyl ether and hydrocarbons at different temperatures using a new flow calorimeter
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
- Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
- Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
- Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
- The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
- Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
- Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
- A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
- Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
- Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
- Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
- Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
- The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
- Thermodynamic Analysis of the Experimental Equilibria for the Liquid-Phase Etherification of Isobutene with C1 to C4 Linear Primary Alcohols
- Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
- Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
- Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
- Vapor Liquid Equilibrium for Binary System of 2-Propanol + 2-Ethoxy-2-methylpropane and Ethyl Ethanoate + 2-Ethoxy-2-methylpropane at 333 K and 2-Propanone + 2-Ethoxy-2-methylpropane at 323 K
- Volumetric and Viscosity Study for the Mixtures of 2-Ethoxy-2-methylpropane, Ethanol, and 1-Ethyl-3-methylimidazolium Ethyl Sulfate Ionic Liquid
- Thermodynamics of Fuels with a Biosynthetic Component: Vapor-Liquid Equilibrium Data for Binary and Ternary Mixtures Containing Ethyl 1,1-Dimethylethyl Ether, n-Heptane, and Toluene at T ) 313.15 K
- Vapor-Liquid Equilibrium for Dimethyl Disulfide + Butane, + trans-But-2-ene, + 2-Methylpropane, + 2-Methylpropene, + Ethanol, and 2-Ethoxy-2-methylpropane
- Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
- Thermodynamics of Fuels with a Biosynthetic Component. II. Vapor Liquid Equilibrium Data for Binary and Ternary Mixtures Containing Ethyl 1,1-Dimethylethyl Ether, 1-Hexene, and Cyclohexane at T = 313.15 K
- Phase Equilibria of (1-Ethyl-3-methylimidazolium Ethylsulfate + Hydrocarbon, + Ketone, and + Ether) Binary Systems
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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