- 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
-
- 2-Ethoxy-2-methylpropane
- 4,4-dimethyl-3-oxapentane
- Ether, tert-butyl ethyl
- Ethyl tert-butyl ether
- Ethyl tert-butyl oxide
- ethyl 1,1-dimethylethyl ether
- t-Butyl ethyl ether
- tert-Butyl Ethyl ether
- tert-C4H9OC2H5
- 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).
- 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).
- 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).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- αdiff : Thermal diffusivity (m2/s).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 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 |
|---|---|---|---|
| PAff | 856.00 | kJ/mol | NIST |
| BasG | 826.90 | kJ/mol | NIST |
| ΔfG° | -102.52 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-317.80; -314.00] | kJ/mol |
|
| 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 |
| log10WS | -1.53 | Crippen Calculated Property | |
| logPoct/wat | 1.821 | Crippen Calculated Property | |
| McVol | 101.270 | ml/mol | McGowan Calculated Property |
| Pc | 3114.04 | kPa | Joback Calculated Property |
| 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 | |
| I | [710.00; 710.00] |
|
|
| I | 710.00 | NIST | |
| I | 710.00 | NIST | |
| Tboil | [345.60; 346.30] | K |
|
| 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 | 531.48 | K | Joback Calculated Property |
| Tfus | 179.15 ± 0.20 | K | NIST |
| Vc | 0.379 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [182.43; 245.69] | J/mol×K | [355.87; 531.48] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 180 190 200 210 220 230 240 250 400 450 500 | ||||
| Cp,gas | 182.43 | J/mol×K | 355.87 | Joback Calculated Property |
| Cp,gas | 194.11 | J/mol×K | 385.14 | Joback Calculated Property |
| Cp,gas | 205.32 | J/mol×K | 414.41 | Joback Calculated Property |
| Cp,gas | 216.07 | J/mol×K | 443.68 | Joback Calculated Property |
| Cp,gas | 226.37 | J/mol×K | 472.94 | Joback Calculated Property |
| Cp,gas | 236.25 | J/mol×K | 502.21 | Joback Calculated Property |
| Cp,gas | 245.69 | J/mol×K | 531.48 | Joback Calculated Property |
| Cp,liquid | 218.00 | J/mol×K | 298.00 | NIST |
| η | [0.0004780; 0.0005320] | Pa×s | [293.15; 303.15] |
|
| η | 0.0005320 | Pa×s | 293.15 | Viscosi... |
| η | 0.0005040 | Pa×s | 298.15 | Viscosi... |
| η | 0.0004780 | Pa×s | 303.15 | Viscosi... |
| ΔvapH | [29.76; 35.30] | kJ/mol | [299.00; 373.50] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 30 31 32 33 34 35 300 320 340 360 | ||||
| ΔvapH | 35.30 | kJ/mol | 299.00 | NIST |
| ΔvapH | 33.50 | kJ/mol | 315.00 | NIST |
| ΔvapH | 32.20 | kJ/mol | 325.50 | NIST |
| ΔvapH | 32.10 | kJ/mol | 326.50 | NIST |
| ΔvapH | 31.90 | kJ/mol | 329.00 | NIST |
| ΔvapH | 32.10 | kJ/mol | 329.50 | NIST |
| ΔvapH | 29.76 | kJ/mol | 345.60 | NIST |
| ΔvapH | 31.20 | kJ/mol | 373.50 | NIST |
| Pvap | [16.83; 147.90] | kPa | [298.25; 358.31] |
|
|
T(K) Vapor pressure (kPa) 20 40 60 80 100 120 140 160 300 320 340 | ||||
| Pvap | 16.83 | kPa | 298.25 | The the... |
| Pvap | 20.88 | kPa | 303.13 | The the... |
| Pvap | 25.07 | kPa | 307.44 | The the... |
| Pvap | 29.66 | kPa | 311.54 | Vapor L... |
| Pvap | 31.70 | kPa | 312.49 | Vapor L... |
| Pvap | 30.91 | kPa | 312.55 | The the... |
| Pvap | 31.90 | kPa | 312.84 | Phase e... |
| Pvap | 37.26 | kPa | 317.29 | The the... |
| Pvap | 40.20 | kPa | 318.55 | Vapor L... |
| Pvap | 40.71 | kPa | 319.61 | Vapor L... |
| Pvap | 45.18 | kPa | 322.38 | Vapor L... |
| Pvap | 45.83 | kPa | 322.74 | The the... |
| Pvap | 47.20 | kPa | 323.25 | Vapor L... |
| Pvap | 49.34 | kPa | 324.77 | Vapor L... |
| Pvap | 51.40 | kPa | 325.18 | Vapor L... |
| Pvap | 54.10 | kPa | 326.60 | Vapor L... |
| Pvap | 55.57 | kPa | 328.05 | Vapor L... |
| Pvap | 56.12 | kPa | 328.30 | The the... |
| Pvap | 59.00 | kPa | 329.02 | Vapor L... |
| Pvap | 60.07 | kPa | 330.26 | Vapor L... |
| Pvap | 65.30 | kPa | 331.96 | Vapor L... |
| Pvap | 64.24 | kPa | 332.17 | Vapor L... |
| Pvap | 64.28 | kPa | 332.26 | Vapor L... |
| Pvap | 67.40 | kPa | 333.28 | Vapor L... |
| Pvap | 67.49 | kPa | 333.56 | The the... |
| Pvap | 68.91 | kPa | 334.21 | Vapor L... |
| Pvap | 74.80 | kPa | 335.92 | Vapor L... |
| Pvap | 74.94 | kPa | 336.69 | Vapor L... |
| Pvap | 80.50 | kPa | 338.08 | Vapor L... |
| Pvap | 79.89 | kPa | 338.60 | Vapor L... |
| Pvap | 81.57 | kPa | 339.17 | The the... |
| Pvap | 85.80 | kPa | 340.01 | Vapor L... |
| Pvap | 84.63 | kPa | 340.37 | Vapor L... |
| Pvap | 90.10 | kPa | 341.49 | Vapor L... |
| Pvap | 91.51 | kPa | 342.76 | Vapor L... |
| Pvap | 94.30 | kPa | 342.88 | Vapor L... |
| Pvap | 93.18 | kPa | 343.23 | The the... |
| Pvap | 97.00 | kPa | 343.86 | Vapor L... |
| Pvap | 95.31 | kPa | 343.89 | The the... |
| Pvap | 97.44 | kPa | 344.57 | The the... |
| Pvap | 99.60 | kPa | 345.25 | The the... |
| Pvap | 102.80 | kPa | 345.77 | Vapor L... |
| Pvap | 101.69 | kPa | 345.92 | The the... |
| Pvap | 101.42 | kPa | 345.99 | Vapor L... |
| Pvap | 147.90 | kPa | 358.31 | Phase e... |
| n0 | [1.37300; 1.37468] | [298.00; 298.15] |
|
|
|
T(K) Refractive Index 1.37 1.37 1.37 1.37 298 298.05 298.09999999999997 298.15 | ||||
| n0 | 1.37300 | 298.00 | Vapor-L... | |
| n0 | 1.37300 | 298.15 | Vapor l... | |
| n0 | 1.37319 | 298.15 | Vapor l... | |
| n0 | 1.37300 | 298.15 | Vapor l... | |
| n0 | 1.37468 | 298.15 | Atmosph... | |
| ρl | [720.69; 741.11] | kg/m3 | [293.15; 313.15] |
|
|
T(K) Liquid Density (kg/m3) 720 725 730 735 740 295 300 305 310 | ||||
| ρl | 741.11 | kg/m3 | 293.15 | Volumet... |
| ρl | 735.85 | kg/m3 | 298.15 | Azeotro... |
| ρl | 735.59 | kg/m3 | 298.15 | Volumet... |
| ρl | 730.85 | kg/m3 | 303.15 | Volumet... |
| ρl | 725.98 | kg/m3 | 308.15 | Volumet... |
| ρl | 720.69 | kg/m3 | 313.15 | Volumet... |
| csound,fluid | [920.73; 1078.87] | m/s | [288.15; 323.15] |
|
|
T(K) Speed of sound in fluid (m/s) 950 1000 1050 290 300 310 320 | ||||
| csound,fluid | 1078.87 | m/s | 288.15 | Tempera... |
| csound,fluid | 1076.43 | m/s | 288.15 | Influen... |
| csound,fluid | 1076.43 | m/s | 288.15 | Tempera... |
| csound,fluid | 1065.09 | m/s | 290.65 | Influen... |
| csound,fluid | 1053.72 | m/s | 293.15 | Influen... |
| csound,fluid | 1042.23 | m/s | 295.65 | Influen... |
| csound,fluid | 1031.01 | m/s | 298.15 | Influen... |
| csound,fluid | 1031.01 | m/s | 298.15 | Tempera... |
| csound,fluid | 1033.23 | m/s | 298.15 | Tempera... |
| csound,fluid | 1019.76 | m/s | 300.65 | Influen... |
| csound,fluid | 1008.62 | m/s | 303.15 | Influen... |
| csound,fluid | 1010.23 | m/s | 303.15 | Tempera... |
| csound,fluid | 997.52 | m/s | 305.65 | Influen... |
| csound,fluid | 986.39 | m/s | 308.15 | Influen... |
| csound,fluid | 975.42 | m/s | 310.65 | Influen... |
| csound,fluid | 965.87 | m/s | 313.15 | Tempera... |
| csound,fluid | 964.53 | m/s | 313.15 | Influen... |
| csound,fluid | 953.54 | m/s | 315.65 | Influen... |
| csound,fluid | 942.67 | m/s | 318.15 | Influen... |
| csound,fluid | 931.73 | m/s | 320.65 | Influen... |
| csound,fluid | 920.73 | m/s | 323.15 | Influen... |
| csound,fluid | 922.48 | m/s | 323.15 | Tempera... |
| csound,fluid | 920.73 | m/s | 323.15 | Tempera... |
| csound,fluid | 922.08 | m/s | 323.15 | Tempera... |
| αdiff | [2.27e-08; 5.67e-08] | m2/s | [293.13; 496.24] |
|
|
T(K) Thermal diffusivity (m2/s) 2.00e-8 3.00e-8 4.00e-8 5.00e-8 6.00e-8 300 400 500 | ||||
| αdiff | 5.67e-08 | m2/s | 293.13 | Thermal... |
| αdiff | 5.45e-08 | m2/s | 303.09 | Thermal... |
| αdiff | 5.16e-08 | m2/s | 313.21 | Thermal... |
| αdiff | 4.96e-08 | m2/s | 323.18 | Thermal... |
| αdiff | 4.79e-08 | m2/s | 333.18 | Thermal... |
| αdiff | 4.70e-08 | m2/s | 338.25 | Thermal... |
| αdiff | 4.64e-08 | m2/s | 343.17 | Thermal... |
| αdiff | 4.55e-08 | m2/s | 348.15 | Thermal... |
| αdiff | 4.49e-08 | m2/s | 353.08 | Thermal... |
| αdiff | 4.43e-08 | m2/s | 358.19 | Thermal... |
| αdiff | 4.38e-08 | m2/s | 363.10 | Thermal... |
| αdiff | 4.33e-08 | m2/s | 368.12 | Thermal... |
| αdiff | 4.30e-08 | m2/s | 373.11 | Thermal... |
| αdiff | 4.26e-08 | m2/s | 378.18 | Thermal... |
| αdiff | 4.20e-08 | m2/s | 383.14 | Thermal... |
| αdiff | 4.17e-08 | m2/s | 388.07 | Thermal... |
| αdiff | 4.15e-08 | m2/s | 393.06 | Thermal... |
| αdiff | 4.10e-08 | m2/s | 398.17 | Thermal... |
| αdiff | 4.08e-08 | m2/s | 403.22 | Thermal... |
| αdiff | 4.02e-08 | m2/s | 408.16 | Thermal... |
| αdiff | 4.00e-08 | m2/s | 413.10 | Thermal... |
| αdiff | 3.97e-08 | m2/s | 418.18 | Thermal... |
| αdiff | 3.95e-08 | m2/s | 423.09 | Thermal... |
| αdiff | 3.90e-08 | m2/s | 428.08 | Thermal... |
| αdiff | 3.85e-08 | m2/s | 433.18 | Thermal... |
| αdiff | 3.82e-08 | m2/s | 438.17 | Thermal... |
| αdiff | 3.77e-08 | m2/s | 443.06 | Thermal... |
| αdiff | 3.74e-08 | m2/s | 448.18 | Thermal... |
| αdiff | 3.68e-08 | m2/s | 453.18 | Thermal... |
| αdiff | 3.61e-08 | m2/s | 458.10 | Thermal... |
| αdiff | 3.53e-08 | m2/s | 463.19 | Thermal... |
| αdiff | 3.50e-08 | m2/s | 466.12 | Thermal... |
| αdiff | 3.45e-08 | m2/s | 469.18 | Thermal... |
| αdiff | 3.39e-08 | m2/s | 472.09 | Thermal... |
| αdiff | 3.33e-08 | m2/s | 475.06 | Thermal... |
| αdiff | 3.25e-08 | m2/s | 478.15 | Thermal... |
| αdiff | 3.16e-08 | m2/s | 481.24 | Thermal... |
| αdiff | 3.05e-08 | m2/s | 484.23 | Thermal... |
| αdiff | 2.95e-08 | m2/s | 487.17 | Thermal... |
| αdiff | 2.77e-08 | m2/s | 490.09 | Thermal... |
| αdiff | 2.63e-08 | m2/s | 493.14 | Thermal... |
| αdiff | 2.27e-08 | m2/s | 496.24 | Thermal... |
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 |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [257.16; 367.48] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
| 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 |
Similar Compounds
Find more compounds similar to Propane, 2-ethoxy-2-methyl-.
Mixtures
- Propane, 2-ethoxy-2-methyl- + Diethyl sulfide
- 1-Propanol + Propane, 2-ethoxy-2-methyl-
- Thiophene + 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
- Propane, 2-ethoxy-2-methyl- + o-Xylene
- Benzene, 1,3-dimethyl- + Propane, 2-ethoxy-2-methyl-
- p-Xylene + Propane, 2-ethoxy-2-methyl-
- Propanenitrile + Propane, 2-ethoxy-2-methyl-
- 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]-
- Propane, 2-ethoxy-2-methyl- + Ethanol, 2-ethoxy-
- Ethanol, 2-(2-ethoxyethoxy)- + Propane, 2-ethoxy-2-methyl-
- Propane, 2-ethoxy-2-methyl- + Ethanol, 2-[2-(2-ethoxyethoxy)ethoxy]-
- Benzene + Propane, 2-ethoxy-2-methyl-
- Toluene + Propane, 2-ethoxy-2-methyl-
- Propane, 2-ethoxy-2-methyl- + Ethylbenzene
Find more mixtures with Propane, 2-ethoxy-2-methyl-.
Sources
- 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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