- InChI
- InChI=1S/C5H12O/c1-5(2,3)6-4/h1-4H3
- InChI Key
- BZLVMXJERCGZMT-UHFFFAOYSA-N
- Formula
- C5H12O
- SMILES
- COC(C)(C)C
- Molecular Weight1
- 88.15
- CAS
- 1634-04-4
- Other Names
-
- 1,1-Dimethylethyl methyl ether
- 1,1-dimethyl-1-methoxyethane
- 2-METHOXY-2-METHYLPROPANE
- 2-Methyl-2-methoxypropane
- 3,3-dimethyl-2-oxabutane
- Driveron
- Ether, tert-butyl methyl
- METHYL-1,1-DIMETHYLETHYL ETHER
- MTBE
- Methyl 1,1-dimethylethyl ether
- Methyl t-butyl ether
- Methyl tert-butyl ether
- TERT-BUTYL METHYL ETHER
- UN 2398
- methyl tert-butyl ether (MTBE)
- t-Butyl methyl ether
- tert-C4H9OCH3
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (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).
- ν : Kinematic viscosity (m2/s).
- 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.
- 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).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- αdiff : Thermal diffusivity (m2/s).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.2690 | KDB | |
| PAff | 841.60 | kJ/mol | NIST |
| BasG | 812.40 | kJ/mol | NIST |
| ΔcH°liquid | [-3368.97; -3359.70] | kJ/mol |
|
| ΔcH°liquid | -3368.97 | kJ/mol | NIST |
| ΔcH°liquid | -3359.70 ± 6.50 | kJ/mol | NIST |
| μ | 1.20 | debye | KDB |
| η | 0.0003610 | Pa×s | Densiti... |
| ΔfG° | -125.50 | kJ/mol | KDB |
| ΔfH°gas | [-293.10; -282.20] | kJ/mol |
|
| ΔfH°gas | -293.10 | kJ/mol | KDB |
| ΔfH°gas | -285.00 | kJ/mol | NIST |
| ΔfH°gas | -283.20 ± 1.30 | kJ/mol | NIST |
| ΔfH°gas | -282.20 ± 1.90 | kJ/mol | NIST |
| ΔfH°liquid | [-322.90; -313.60] | kJ/mol |
|
| ΔfH°liquid | -315.40 | kJ/mol | NIST |
| ΔfH°liquid | -313.60 ± 1.30 | kJ/mol | NIST |
| ΔfH°liquid | -322.90 ± 5.00 | kJ/mol | NIST |
| ΔfusH° | 2.48 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 27.84 | kJ/mol | Joback Calculated Property |
| IE | [9.24; 9.48] | eV |
|
| IE | 9.24 | eV | NIST |
| IE | 9.48 | eV | NIST |
| IE | 9.41 | eV | NIST |
| log10WS | [-0.24; -0.24] |
|
|
| log10WS | -0.24 | Aq. Sol... | |
| log10WS | -0.24 | Estimat... | |
| logPoct/wat | 1.431 | Crippen Calculated Property | |
| McVol | 87.180 | ml/mol | McGowan Calculated Property |
| Pc | [3397.00; 3430.00] | kPa |
|
| Pc | 3430.00 | kPa | KDB |
| Pc | 3397.00 ± 8.00 | kPa | NIST |
| Pc | 3430.00 ± 10.00 | kPa | NIST |
| Inp | [544.00; 570.12] |
|
|
| Inp | 563.70 | NIST | |
| Inp | 562.70 | NIST | |
| Inp | 562.00 | NIST | |
| Inp | Outlier 544.00 | NIST | |
| Inp | 549.00 | NIST | |
| Inp | 570.12 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 566.00 | NIST | |
| Inp | 566.00 | NIST | |
| Inp | 567.00 | NIST | |
| Inp | 554.50 | NIST | |
| Inp | 558.00 | NIST | |
| Inp | 563.00 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 560.00 | NIST | |
| Inp | 556.00 | NIST | |
| Inp | 556.00 | NIST | |
| Inp | 556.00 | NIST | |
| Inp | 560.00 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 563.00 | NIST | |
| Inp | 556.00 | NIST | |
| I | [666.00; 688.00] |
|
|
| I | 666.00 | NIST | |
| I | 688.00 | NIST | |
| S°gas | 357.80 | J/mol×K | NIST |
| S°liquid | 265.30 | J/mol×K | NIST |
| Tboil | [328.25; 328.30] | K |
|
| Tboil | 328.30 | K | KDB |
| Tboil | 328.25 | K | Vapor-L... |
| Tc | [496.40; 497.10] | K |
|
| Tc | 497.10 | K | KDB |
| Tc | 497.00 | K | Measure... |
| Tc | 496.40 ± 0.30 | K | NIST |
| Tc | 497.10 | K | NIST |
| Tc | 497.10 ± 0.20 | K | NIST |
| Tfus | [164.25; 164.50] | K |
|
| Tfus | 164.50 | K | KDB |
| Tfus | 164.25 | K | Aq. Sol... |
| Tfus | 164.50 ± 0.20 | K | NIST |
| Ttriple | 164.56 ± 0.07 | K | NIST |
| Vc | 0.323 | m3/kmol | KDB |
| Zc | 0.2676350 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [147.83; 203.44] | J/mol×K | [332.99; 508.60] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 150 160 170 180 190 200 350 400 450 500 | ||||
| Cp,gas | 147.83 | J/mol×K | 332.99 | Joback Calculated Property |
| Cp,gas | 158.08 | J/mol×K | 362.26 | Joback Calculated Property |
| Cp,gas | 167.93 | J/mol×K | 391.53 | Joback Calculated Property |
| Cp,gas | 177.38 | J/mol×K | 420.79 | Joback Calculated Property |
| Cp,gas | 186.44 | J/mol×K | 450.06 | Joback Calculated Property |
| Cp,gas | 195.13 | J/mol×K | 479.33 | Joback Calculated Property |
| Cp,gas | 203.44 | J/mol×K | 508.60 | Joback Calculated Property |
| Cp,liquid | [187.50; 188.00] | J/mol×K | [298.00; 298.15] |
|
| Cp,liquid | 188.00 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 187.50 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 187.80 | J/mol×K | 298.15 | NIST |
| η | [0.0002780; 0.0004430] | Pa×s | [273.15; 313.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 3.00e-4 3.50e-4 4.00e-4 4.50e-4 280 290 300 310 | ||||
| η | 0.0003900 | Pa×s | 273.15 | Density... |
| η | 0.0004430 | Pa×s | 273.15 | Densiti... |
| η | 0.0004170 | Pa×s | 278.15 | Densiti... |
| η | 0.0003920 | Pa×s | 283.15 | Densiti... |
| η | 0.0003600 | Pa×s | 283.15 | Density... |
| η | 0.0003897 | Pa×s | 283.15 | Experim... |
| η | 0.0003640 | Pa×s | 288.15 | Experim... |
| η | 0.0003700 | Pa×s | 288.15 | Densiti... |
| η | 0.0003482 | Pa×s | 293.15 | Experim... |
| η | 0.0003330 | Pa×s | 293.15 | Density... |
| η | 0.0003327 | Pa×s | 298.15 | Experim... |
| η | 0.0003190 | Pa×s | 298.15 | Density... |
| η | 0.0003040 | Pa×s | 303.15 | Density... |
| η | 0.0003152 | Pa×s | 303.15 | Experim... |
| η | 0.0002994 | Pa×s | 308.15 | Experim... |
| η | 0.0002846 | Pa×s | 313.15 | Experim... |
| η | 0.0002780 | Pa×s | 313.15 | Density... |
| ΔfusH | [7.60; 7.60] | kJ/mol | [164.56; 164.60] |
|
| ΔfusH | 7.60 | kJ/mol | 164.56 | NIST |
| ΔfusH | 7.60 | kJ/mol | 164.60 | NIST |
| ΔfusH | 7.60 | kJ/mol | 164.60 | NIST |
| ΔvapH | [27.90; 31.20] | kJ/mol | [306.50; 355.50] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 28 28.5 29 29.5 30 30.5 31 31.5 320 340 | ||||
| ΔvapH | 30.40 | kJ/mol | 306.50 | NIST |
| ΔvapH | 30.00 | kJ/mol | 310.00 | NIST |
| ΔvapH | 29.90 | kJ/mol | 314.00 | NIST |
| ΔvapH | 30.20 | kJ/mol | 319.00 | NIST |
| ΔvapH | 27.90 | kJ/mol | 328.00 | NIST |
| ΔvapH | 27.94 | kJ/mol | 328.30 | NIST |
| ΔvapH | 29.60 | kJ/mol | 340.00 | NIST |
| ΔvapH | 31.20 | kJ/mol | 355.50 | NIST |
| ν | [0.0000004; 0.0000005] | m2/s | [283.15; 313.15] |
|
| ν | 0.0000005 | m2/s | 283.15 | Kinemat... |
| ν | 0.0000005 | m2/s | 298.15 | Kinemat... |
| ν | 0.0000004 | m2/s | 313.15 | Kinemat... |
| Pvap | [6.24; 221.79] | kPa | [263.15; 354.82] |
|
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 280 300 320 340 | ||||
| Pvap | 6.24 | kPa | 263.15 | Isother... |
| Pvap | 6.25 | kPa | 263.15 | Thermod... |
| Pvap | 6.40 | kPa | 263.53 | Isother... |
| Pvap | 10.67 | kPa | 273.15 | Isother... |
| Pvap | 10.64 | kPa | 273.15 | Thermod... |
| Pvap | 10.80 | kPa | 273.34 | Isother... |
| Pvap | 11.59 | kPa | 274.90 | Isother... |
| Pvap | 11.59 | kPa | 274.91 | Isother... |
| Pvap | 17.41 | kPa | 283.15 | Isother... |
| Pvap | 17.31 | kPa | 283.15 | Thermod... |
| Pvap | 17.60 | kPa | 283.27 | Isother... |
| Pvap | 17.79 | kPa | 283.60 | A milli... |
| Pvap | 18.55 | kPa | 284.82 | Isother... |
| Pvap | 22.07 | kPa | 288.60 | A milli... |
| Pvap | 27.06 | kPa | 293.15 | Thermod... |
| Pvap | 27.25 | kPa | 293.15 | Isother... |
| Pvap | 27.40 | kPa | 293.25 | Isother... |
| Pvap | 27.43 | kPa | 293.50 | A milli... |
| Pvap | 28.78 | kPa | 294.80 | Isother... |
| Pvap | 28.78 | kPa | 294.80 | Isother... |
| Pvap | 28.78 | kPa | 294.81 | Isother... |
| Pvap | 33.39 | kPa | 298.15 | Thermod... |
| Pvap | 33.72 | kPa | 298.40 | A milli... |
| Pvap | 41.16 | kPa | 303.15 | Isother... |
| Pvap | 40.86 | kPa | 303.15 | Thermod... |
| Pvap | 41.20 | kPa | 303.22 | Isother... |
| Pvap | 41.10 | kPa | 303.30 | A milli... |
| Pvap | 43.26 | kPa | 304.79 | Isother... |
| Pvap | 43.24 | kPa | 304.79 | Isother... |
| Pvap | 49.80 | kPa | 308.20 | A milli... |
| Pvap | 59.90 | kPa | 313.10 | A milli... |
| Pvap | 60.22 | kPa | 313.15 | Isother... |
| Pvap | 59.81 | kPa | 313.15 | Thermod... |
| Pvap | 62.40 | kPa | 313.20 | Isother... |
| Pvap | 60.30 | kPa | 313.24 | Isother... |
| Pvap | 62.95 | kPa | 314.75 | Isother... |
| Pvap | 62.97 | kPa | 314.76 | Isother... |
| Pvap | 62.97 | kPa | 314.76 | Isother... |
| Pvap | 71.61 | kPa | 318.10 | A milli... |
| Pvap | 85.01 | kPa | 323.00 | A milli... |
| Pvap | 85.15 | kPa | 323.15 | Thermod... |
| Pvap | 85.65 | kPa | 323.15 | Isother... |
| Pvap | 85.80 | kPa | 323.21 | Isother... |
| Pvap | 89.66 | kPa | 324.90 | Isother... |
| Pvap | 89.69 | kPa | 324.90 | Isother... |
| Pvap | 100.34 | kPa | 327.90 | A milli... |
| Pvap | 117.70 | kPa | 332.90 | A milli... |
| Pvap | 118.27 | kPa | 333.15 | Thermod... |
| Pvap | 118.78 | kPa | 333.15 | Isother... |
| Pvap | 120.40 | kPa | 333.15 | Thermod... |
| Pvap | 119.20 | kPa | 333.19 | Isother... |
| Pvap | 124.02 | kPa | 334.85 | Isother... |
| Pvap | 137.39 | kPa | 337.80 | A milli... |
| Pvap | 160.66 | kPa | 343.15 | Thermod... |
| Pvap | 167.14 | kPa | 344.84 | Isother... |
| Pvap | 167.57 | kPa | 344.85 | Isother... |
| Pvap | 221.79 | kPa | 354.82 | Isother... |
| Pvap | 221.39 | kPa | 354.82 | Isother... |
| n0 | [1.36594; 1.36980] | [293.15; 298.20] |
|
|
|
T(K) Refractive Index 1.37 1.37 1.37 1.37 1.37 294 296 298 | ||||
| n0 | 1.36900 | 293.15 | (Vapor ... | |
| n0 | 1.36890 | 293.15 | A novel... | |
| n0 | 1.36980 | 293.15 | Vapor-L... | |
| n0 | 1.36766 | 298.15 | Phase e... | |
| n0 | 1.36648 | 298.15 | Volumet... | |
| n0 | 1.36648 | 298.15 | Volumet... | |
| n0 | 1.36610 | 298.15 | sotherm... | |
| n0 | 1.36594 | 298.15 | Quatern... | |
| n0 | 1.36628 | 298.15 | Isobari... | |
| n0 | 1.36600 | 298.15 | Solubil... | |
| n0 | 1.36764 | 298.15 | Atmosph... | |
| n0 | 1.36766 | 298.15 | Vapor-L... | |
| n0 | 1.36632 | 298.20 | Vapor-L... | |
| ρl | [713.96; 761.34] | kg/m3 | [273.15; 318.15] |
|
|
T(K) Liquid Density (kg/m3) 710 720 730 740 750 760 280 290 300 310 | ||||
| ρl | 761.30 | kg/m3 | 273.15 | Physico... |
| ρl | 761.34 | kg/m3 | 273.15 | Densiti... |
| ρl | 756.14 | kg/m3 | 278.15 | Densiti... |
| ρl | 751.02 | kg/m3 | 283.15 | Densiti... |
| ρl | 745.90 | kg/m3 | 288.15 | Physico... |
| ρl | 745.85 | kg/m3 | 288.15 | Densiti... |
| ρl | 740.65 | kg/m3 | 293.15 | Densiti... |
| ρl | 739.80 | kg/m3 | 293.15 | Measure... |
| ρl | 739.45 | kg/m3 | 293.20 | Liquid-... |
| ρl | 735.40 | kg/m3 | 298.15 | Phase e... |
| ρl | 734.10 | kg/m3 | 298.15 | Solubil... |
| ρl | 735.69 | kg/m3 | 298.15 | Excess ... |
| ρl | 735.36 | kg/m3 | 298.15 | Densiti... |
| ρl | 735.69 | kg/m3 | 298.15 | Excess ... |
| ρl | 735.00 | kg/m3 | 298.15 | Physico... |
| ρl | 735.99 | kg/m3 | 298.15 | Excess ... |
| ρl | 735.35 | kg/m3 | 298.15 | Mixing ... |
| ρl | 735.48 | kg/m3 | 298.15 | Excess ... |
| ρl | 740.60 | kg/m3 | 298.15 | Vapor-L... |
| ρl | 735.21 | kg/m3 | 298.15 | Excess ... |
| ρl | 735.99 | kg/m3 | 298.15 | Excess ... |
| ρl | 735.99 | kg/m3 | 298.15 | Excess ... |
| ρl | 735.40 | kg/m3 | 298.15 | Densiti... |
| ρl | 737.80 | kg/m3 | 298.20 | Phase e... |
| ρl | 730.10 | kg/m3 | 303.15 | Densiti... |
| ρl | 724.60 | kg/m3 | 308.15 | Physico... |
| ρl | 724.85 | kg/m3 | 308.15 | Densiti... |
| ρl | 724.82 | kg/m3 | 308.15 | Densiti... |
| ρl | 719.42 | kg/m3 | 313.15 | Densiti... |
| ρl | 718.08 | kg/m3 | 313.20 | Liquid-... |
| ρl | 713.96 | kg/m3 | 318.15 | Densiti... |
| ΔfusS | 46.18 | J/mol×K | 164.56 | NIST |
| csound,fluid | [103.70; 1086.92] | m/s | [288.15; 493.06] |
|
|
T(K) Speed of sound in fluid (m/s) 200 400 600 800 1000 300 350 400 450 | ||||
| csound,fluid | 1086.92 | m/s | 288.15 | Mixing ... |
| csound,fluid | 1082.11 | m/s | 288.15 | Influen... |
| csound,fluid | 1086.62 | m/s | 288.15 | Mixing ... |
| csound,fluid | 1082.40 | m/s | 288.15 | Excess ... |
| csound,fluid | 1083.38 | m/s | 288.15 | Influen... |
| csound,fluid | 1083.38 | m/s | 288.15 | Influen... |
| csound,fluid | 1071.61 | m/s | 290.65 | Influen... |
| csound,fluid | 1070.62 | m/s | 290.65 | Influen... |
| csound,fluid | 1071.61 | m/s | 290.65 | Influen... |
| csound,fluid | 1060.05 | m/s | 293.15 | Influen... |
| csound,fluid | 1060.05 | m/s | 293.15 | Influen... |
| csound,fluid | 1063.43 | m/s | 293.15 | Mixing ... |
| csound,fluid | 1059.10 | m/s | 293.15 | Influen... |
| csound,fluid | 1059.40 | m/s | 293.15 | Excess ... |
| csound,fluid | 1047.83 | m/s | 295.65 | Influen... |
| csound,fluid | 1048.48 | m/s | 295.65 | Influen... |
| csound,fluid | 1048.48 | m/s | 295.65 | Influen... |
| csound,fluid | 1036.63 | m/s | 298.15 | Influen... |
| csound,fluid | 1036.10 | m/s | 298.15 | Excess ... |
| csound,fluid | 1036.94 | m/s | 298.15 | Influen... |
| csound,fluid | 1040.35 | m/s | 298.15 | Mixing ... |
| csound,fluid | 1036.94 | m/s | 298.15 | Influen... |
| csound,fluid | 1025.38 | m/s | 300.65 | Influen... |
| csound,fluid | 1025.42 | m/s | 300.65 | Influen... |
| csound,fluid | 1025.42 | m/s | 300.65 | Influen... |
| csound,fluid | 1024.33 | m/s | 301.65 | Influen... |
| csound,fluid | 1017.42 | m/s | 303.15 | Mixing ... |
| csound,fluid | 1014.04 | m/s | 303.15 | Influen... |
| csound,fluid | 1013.90 | m/s | 303.15 | Influen... |
| csound,fluid | 1013.00 | m/s | 303.15 | Excess ... |
| csound,fluid | 1012.81 | m/s | 303.15 | Influen... |
| csound,fluid | 1013.90 | m/s | 303.15 | Influen... |
| csound,fluid | 1024.70 | m/s | 303.19 | Speed o... |
| csound,fluid | 1001.35 | m/s | 305.65 | Influen... |
| csound,fluid | 1002.41 | m/s | 305.65 | Influen... |
| csound,fluid | 1002.70 | m/s | 305.65 | Influen... |
| csound,fluid | 1002.41 | m/s | 305.65 | Influen... |
| csound,fluid | 991.34 | m/s | 308.15 | Influen... |
| csound,fluid | 990.99 | m/s | 308.15 | Influen... |
| csound,fluid | 990.10 | m/s | 308.15 | Excess ... |
| csound,fluid | 989.90 | m/s | 308.15 | Influen... |
| csound,fluid | 990.99 | m/s | 308.15 | Influen... |
| csound,fluid | 994.68 | m/s | 308.15 | Mixing ... |
| csound,fluid | 988.60 | m/s | 308.16 | Speed o... |
| csound,fluid | 979.62 | m/s | 310.65 | Influen... |
| csound,fluid | 980.00 | m/s | 310.65 | Influen... |
| csound,fluid | 978.47 | m/s | 310.65 | Influen... |
| csound,fluid | 979.62 | m/s | 310.65 | Influen... |
| csound,fluid | 960.40 | m/s | 313.08 | Speed o... |
| csound,fluid | 967.03 | m/s | 313.15 | Influen... |
| csound,fluid | 968.16 | m/s | 313.15 | Influen... |
| csound,fluid | 968.63 | m/s | 313.15 | Influen... |
| csound,fluid | 968.16 | m/s | 313.15 | Influen... |
| csound,fluid | 956.80 | m/s | 315.65 | Influen... |
| csound,fluid | 956.80 | m/s | 315.65 | Influen... |
| csound,fluid | 955.73 | m/s | 315.65 | Influen... |
| csound,fluid | 957.31 | m/s | 315.65 | Influen... |
| csound,fluid | 946.03 | m/s | 318.15 | Influen... |
| csound,fluid | 944.34 | m/s | 318.15 | Influen... |
| csound,fluid | 945.54 | m/s | 318.15 | Influen... |
| csound,fluid | 945.54 | m/s | 318.15 | Influen... |
| csound,fluid | 942.70 | m/s | 318.19 | Speed o... |
| csound,fluid | 934.24 | m/s | 320.65 | Influen... |
| csound,fluid | 934.24 | m/s | 320.65 | Influen... |
| csound,fluid | 933.01 | m/s | 320.65 | Influen... |
| csound,fluid | 934.76 | m/s | 320.65 | Influen... |
| csound,fluid | 912.40 | m/s | 323.07 | Speed o... |
| csound,fluid | 922.97 | m/s | 323.15 | Influen... |
| csound,fluid | 922.97 | m/s | 323.15 | Influen... |
| csound,fluid | 923.46 | m/s | 323.15 | Influen... |
| csound,fluid | 921.93 | m/s | 323.15 | Influen... |
| csound,fluid | 904.70 | m/s | 328.21 | Speed o... |
| csound,fluid | 876.80 | m/s | 333.13 | Speed o... |
| csound,fluid | 855.10 | m/s | 338.07 | Speed o... |
| csound,fluid | 826.30 | m/s | 343.12 | Speed o... |
| csound,fluid | 797.50 | m/s | 348.24 | Speed o... |
| csound,fluid | 781.50 | m/s | 353.11 | Speed o... |
| csound,fluid | 748.60 | m/s | 358.22 | Speed o... |
| csound,fluid | 727.10 | m/s | 363.16 | Speed o... |
| csound,fluid | 707.10 | m/s | 368.17 | Speed o... |
| csound,fluid | 698.90 | m/s | 373.05 | Speed o... |
| csound,fluid | 668.30 | m/s | 378.05 | Speed o... |
| csound,fluid | 646.40 | m/s | 383.08 | Speed o... |
| csound,fluid | 627.50 | m/s | 388.11 | Speed o... |
| csound,fluid | 609.10 | m/s | 393.16 | Speed o... |
| csound,fluid | 580.10 | m/s | 398.11 | Speed o... |
| csound,fluid | 558.00 | m/s | 403.24 | Speed o... |
| csound,fluid | 537.60 | m/s | 408.23 | Speed o... |
| csound,fluid | 515.80 | m/s | 413.20 | Speed o... |
| csound,fluid | 494.40 | m/s | 418.24 | Speed o... |
| csound,fluid | 476.00 | m/s | 423.15 | Speed o... |
| csound,fluid | 453.80 | m/s | 428.24 | Speed o... |
| csound,fluid | 430.30 | m/s | 433.05 | Speed o... |
| csound,fluid | 405.80 | m/s | 438.19 | Speed o... |
| csound,fluid | 387.30 | m/s | 443.09 | Speed o... |
| csound,fluid | 360.30 | m/s | 448.23 | Speed o... |
| csound,fluid | 339.50 | m/s | 453.10 | Speed o... |
| csound,fluid | 313.60 | m/s | 458.19 | Speed o... |
| csound,fluid | 287.10 | m/s | 463.23 | Speed o... |
| csound,fluid | 265.00 | m/s | 468.18 | Speed o... |
| csound,fluid | 236.50 | m/s | 473.17 | Speed o... |
| csound,fluid | 206.10 | m/s | 478.08 | Speed o... |
| csound,fluid | 177.70 | m/s | 483.20 | Speed o... |
| csound,fluid | 142.80 | m/s | 488.11 | Speed o... |
| csound,fluid | 103.70 | m/s | 493.06 | Speed o... |
| γ | [0.01; 0.02] | N/m | [243.08; 393.13] |
|
|
T(K) Surface Tension (N/m) 0.01 0.02 0.02 0.03 250 300 350 | ||||
| γ | 0.02 | N/m | 243.08 | Surface... |
| γ | 0.02 | N/m | 248.01 | Surface... |
| γ | 0.02 | N/m | 253.11 | Surface... |
| γ | 0.02 | N/m | 258.13 | Surface... |
| γ | 0.02 | N/m | 263.10 | Surface... |
| γ | 0.02 | N/m | 268.13 | Surface... |
| γ | 0.02 | N/m | 273.16 | Surface... |
| γ | 0.02 | N/m | 278.11 | Surface... |
| γ | 0.02 | N/m | 283.12 | Surface... |
| γ | 0.02 | N/m | 288.13 | Surface... |
| γ | 0.02 | N/m | 293.07 | Surface... |
| γ | 0.02 | N/m | 298.08 | Surface... |
| γ | 0.02 | N/m | 303.11 | Surface... |
| γ | 0.02 | N/m | 308.15 | Surface... |
| γ | 0.02 | N/m | 313.16 | Surface... |
| γ | 0.02 | N/m | 318.11 | Surface... |
| γ | 0.02 | N/m | 323.16 | Surface... |
| γ | 0.01 | N/m | 328.14 | Surface... |
| γ | 0.01 | N/m | 333.15 | Surface... |
| γ | 0.01 | N/m | 338.16 | Surface... |
| γ | 0.01 | N/m | 343.13 | Surface... |
| γ | 0.01 | N/m | 348.13 | Surface... |
| γ | 0.01 | N/m | 353.13 | Surface... |
| γ | 0.01 | N/m | 358.15 | Surface... |
| γ | 0.01 | N/m | 363.13 | Surface... |
| γ | 0.01 | N/m | 368.13 | Surface... |
| γ | 0.01 | N/m | 373.12 | Surface... |
| γ | 0.01 | N/m | 378.12 | Surface... |
| γ | 0.01 | N/m | 383.12 | Surface... |
| γ | 0.01 | N/m | 388.14 | Surface... |
| γ | 0.01 | N/m | 393.13 | Surface... |
| αdiff | [2.73e-08; 6.40e-08] | m2/s | [303.15; 493.15] |
|
|
T(K) Thermal diffusivity (m2/s) 3.00e-8 4.00e-8 5.00e-8 6.00e-8 300 350 400 450 | ||||
| αdiff | 6.40e-08 | m2/s | 303.15 | Thermal... |
| αdiff | 6.17e-08 | m2/s | 313.15 | Thermal... |
| αdiff | 5.87e-08 | m2/s | 323.15 | Thermal... |
| αdiff | 5.70e-08 | m2/s | 333.15 | Thermal... |
| αdiff | 5.42e-08 | m2/s | 343.15 | Thermal... |
| αdiff | 5.26e-08 | m2/s | 353.15 | Thermal... |
| αdiff | 5.05e-08 | m2/s | 363.15 | Thermal... |
| αdiff | 4.83e-08 | m2/s | 373.15 | Thermal... |
| αdiff | 4.72e-08 | m2/s | 383.15 | Thermal... |
| αdiff | 4.64e-08 | m2/s | 393.15 | Thermal... |
| αdiff | 4.55e-08 | m2/s | 403.15 | Thermal... |
| αdiff | 4.48e-08 | m2/s | 413.15 | Thermal... |
| αdiff | 4.38e-08 | m2/s | 423.15 | Thermal... |
| αdiff | 4.31e-08 | m2/s | 433.15 | Thermal... |
| αdiff | 4.18e-08 | m2/s | 443.15 | Thermal... |
| αdiff | 4.05e-08 | m2/s | 453.15 | Thermal... |
| αdiff | 3.91e-08 | m2/s | 458.15 | Thermal... |
| αdiff | 3.86e-08 | m2/s | 463.15 | Thermal... |
| αdiff | 3.66e-08 | m2/s | 468.15 | Thermal... |
| αdiff | 3.55e-08 | m2/s | 473.15 | Thermal... |
| αdiff | 3.47e-08 | m2/s | 475.15 | Thermal... |
| αdiff | 3.36e-08 | m2/s | 477.15 | Thermal... |
| αdiff | 3.36e-08 | m2/s | 479.15 | Thermal... |
| αdiff | 3.30e-08 | m2/s | 481.15 | Thermal... |
| αdiff | 3.22e-08 | m2/s | 483.15 | Thermal... |
| αdiff | 3.07e-08 | m2/s | 485.15 | Thermal... |
| αdiff | 3.02e-08 | m2/s | 487.15 | Thermal... |
| αdiff | 2.95e-08 | m2/s | 489.15 | Thermal... |
| αdiff | 2.81e-08 | m2/s | 491.15 | Thermal... |
| αdiff | 2.73e-08 | m2/s | 493.15 | Thermal... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 100.00 | 750.94 |
| 288.15 | 100.00 | 745.79 |
| 293.15 | 100.00 | 740.59 |
| 298.15 | 100.00 | 735.34 |
| 303.15 | 100.00 | 730.04 |
| 308.15 | 100.00 | 724.69 |
| 313.15 | 100.00 | 719.29 |
| 318.15 | 100.00 | 713.84 |
| 323.15 | 100.00 | 708.45 |
| 283.15 | 5000.00 | 756.29 |
| 288.15 | 5000.00 | 751.33 |
| 293.15 | 5000.00 | 746.34 |
| 298.15 | 5000.00 | 741.32 |
| 303.15 | 5000.00 | 736.27 |
| 308.15 | 5000.00 | 731.19 |
| 313.15 | 5000.00 | 726.07 |
| 318.15 | 5000.00 | 720.92 |
| 323.15 | 5000.00 | 715.73 |
| 283.15 | 10000.00 | 761.29 |
| 288.15 | 10000.00 | 756.52 |
| 293.15 | 10000.00 | 751.7 |
| 298.15 | 10000.00 | 746.89 |
| 303.15 | 10000.00 | 742.05 |
| 308.15 | 10000.00 | 737.18 |
| 313.15 | 10000.00 | 732.27 |
| 318.15 | 10000.00 | 727.36 |
| 323.15 | 10000.00 | 722.39 |
| 283.15 | 15000.00 | 765.93 |
| 288.15 | 15000.00 | 761.32 |
| 293.15 | 15000.00 | 756.68 |
| 298.15 | 15000.00 | 752.04 |
| 303.15 | 15000.00 | 747.37 |
| 308.15 | 15000.00 | 742.69 |
| 313.15 | 15000.00 | 737.97 |
| 318.15 | 15000.00 | 733.26 |
| 323.15 | 15000.00 | 728.51 |
| 283.15 | 20000.00 | 770.32 |
| 288.15 | 20000.00 | 765.86 |
| 293.15 | 20000.00 | 761.35 |
| 298.15 | 20000.00 | 756.85 |
| 303.15 | 20000.00 | 752.37 |
| 308.15 | 20000.00 | 747.84 |
| 313.15 | 20000.00 | 743.29 |
| 318.15 | 20000.00 | 738.74 |
| 323.15 | 20000.00 | 734.2 |
| 283.15 | 25000.00 | 774.48 |
| 288.15 | 25000.00 | 770.15 |
| 293.15 | 25000.00 | 765.77 |
| 298.15 | 25000.00 | 761.42 |
| 303.15 | 25000.00 | 757.05 |
| 308.15 | 25000.00 | 752.67 |
| 313.15 | 25000.00 | 748.27 |
| 318.15 | 25000.00 | 743.91 |
| 323.15 | 25000.00 | 739.51 |
| 283.15 | 30000.00 | 778.47 |
| 288.15 | 30000.00 | 774.24 |
| 293.15 | 30000.00 | 770.01 |
| 298.15 | 30000.00 | 765.75 |
| 303.15 | 30000.00 | 761.51 |
| 308.15 | 30000.00 | 757.26 |
| 313.15 | 30000.00 | 752.99 |
| 318.15 | 30000.00 | 748.75 |
| 323.15 | 30000.00 | 744.49 |
| 283.15 | 35000.00 | 782.29 |
| 288.15 | 35000.00 | 778.15 |
| 293.15 | 35000.00 | 774.0 |
| 298.15 | 35000.00 | 769.88 |
| 303.15 | 35000.00 | 765.74 |
| 308.15 | 35000.00 | 761.6 |
| 313.15 | 35000.00 | 757.46 |
| 318.15 | 35000.00 | 753.35 |
| 323.15 | 35000.00 | 749.2 |
| 283.15 | 40000.00 | 785.94 |
| 288.15 | 40000.00 | 781.89 |
| 293.15 | 40000.00 | 777.85 |
| 298.15 | 40000.00 | 773.81 |
| 303.15 | 40000.00 | 769.79 |
| 308.15 | 40000.00 | 765.75 |
| 313.15 | 40000.00 | 761.71 |
| 318.15 | 40000.00 | 757.7 |
| 323.15 | 40000.00 | 753.67 |
| 283.15 | 45000.00 | 789.45 |
| 288.15 | 45000.00 | 785.49 |
| 293.15 | 45000.00 | 781.54 |
| 298.15 | 45000.00 | 777.6 |
| 303.15 | 45000.00 | 773.65 |
| 308.15 | 45000.00 | 769.71 |
| 313.15 | 45000.00 | 765.77 |
| 318.15 | 45000.00 | 761.86 |
| 323.15 | 45000.00 | 757.92 |
| 283.15 | 50000.00 | 792.86 |
| 288.15 | 50000.00 | 788.97 |
| 293.15 | 50000.00 | 785.09 |
| 298.15 | 50000.00 | 781.23 |
| 303.15 | 50000.00 | 777.36 |
| 308.15 | 50000.00 | 773.49 |
| 313.15 | 50000.00 | 769.65 |
| 318.15 | 50000.00 | 765.83 |
| 323.15 | 50000.00 | 761.98 |
| 283.15 | 55000.00 | 796.13 |
| 288.15 | 55000.00 | 792.3 |
| 293.15 | 55000.00 | 788.51 |
| 298.15 | 55000.00 | 784.71 |
| 303.15 | 55000.00 | 780.95 |
| 308.15 | 55000.00 | 777.14 |
| 313.15 | 55000.00 | 773.39 |
| 318.15 | 55000.00 | 769.63 |
| 323.15 | 55000.00 | 765.85 |
| 283.15 | 60000.00 | 799.29 |
| 288.15 | 60000.00 | 795.55 |
| 293.15 | 60000.00 | 791.81 |
| 298.15 | 60000.00 | 788.1 |
| 303.15 | 60000.00 | 784.37 |
| 308.15 | 60000.00 | 780.65 |
| 313.15 | 60000.00 | 776.97 |
| 318.15 | 60000.00 | 773.29 |
| 323.15 | 60000.00 | 769.61 |
| 283.15 | 65000.00 | 802.37 |
| 288.15 | 65000.00 | 798.67 |
| 293.15 | 65000.00 | 795.0 |
| 298.15 | 65000.00 | 791.36 |
| 303.15 | 65000.00 | 787.7 |
| 308.15 | 65000.00 | 784.04 |
| 313.15 | 65000.00 | 780.41 |
| 318.15 | 65000.00 | 776.82 |
| 323.15 | 65000.00 | 773.22 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [243.08; 348.65] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.53357e+01 | |||
| Coefficient B | -3.16987e+03 | |||
| Coefficient C | -3.24310e+01 | |||
| Temperature range, min. | 243.08 | |||
| Temperature range, max. | 348.65 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 350 | ||||
| Pvap | 1.33 | kPa | 243.08 | Calculated Property |
| Pvap | 2.95 | kPa | 254.81 | Calculated Property |
| Pvap | 6.02 | kPa | 266.54 | Calculated Property |
| Pvap | 11.49 | kPa | 278.27 | Calculated Property |
| Pvap | 20.67 | kPa | 290.00 | Calculated Property |
| Pvap | 35.34 | kPa | 301.73 | Calculated Property |
| Pvap | 57.76 | kPa | 313.46 | Calculated Property |
| Pvap | 90.75 | kPa | 325.19 | Calculated Property |
| Pvap | 137.73 | kPa | 336.92 | Calculated Property |
| Pvap | 202.64 | kPa | 348.65 | Calculated Property |
| Pvap | [5.51e-04; 3384.37] | kPa | [164.55; 497.10] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.49173e+01 | |||
| Coefficient B | -5.55710e+03 | |||
| Coefficient C | -7.60854e+00 | |||
| Coefficient D | 6.59025e-06 | |||
| Temperature range, min. | 164.55 | |||
| Temperature range, max. | 497.10 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 200 300 400 500 | ||||
| Pvap | 5.51e-04 | kPa | 164.55 | Calculated Property |
| Pvap | 0.06 | kPa | 201.50 | Calculated Property |
| Pvap | 1.40 | kPa | 238.45 | Calculated Property |
| Pvap | 12.09 | kPa | 275.40 | Calculated Property |
| Pvap | 58.24 | kPa | 312.35 | Calculated Property |
| Pvap | 191.91 | kPa | 349.30 | Calculated Property |
| Pvap | 489.32 | kPa | 386.25 | Calculated Property |
| Pvap | 1044.38 | kPa | 423.20 | Calculated Property |
| Pvap | 1966.13 | kPa | 460.15 | Calculated Property |
| Pvap | 3384.37 | kPa | 497.10 | Calculated Property |
Similar Compounds
Find more compounds similar to Propane, 2-methoxy-2-methyl-.
Mixtures
- Benzene + Propane, 2-methoxy-2-methyl-
- Toluene + Propane, 2-methoxy-2-methyl-
- Propane, 2-methoxy-2-methyl- + Ethylbenzene
- Propane, 2-methoxy-2-methyl- + Pentane, 2,2,4-trimethyl-
- 2-Propanol, 2-methyl- + Propane, 2-methoxy-2-methyl-
- Propane, 2-methoxy-2-methyl- + Pentane, 3-methyl-
- n-Hexane + Propane, 2-methoxy-2-methyl-
- Propane, 2-methoxy-2-methyl- + Heptane
- Butane, 1-chloro- + Propane, 2-methoxy-2-methyl-
- Propane, 2-methoxy-2-methyl- + Butane, 2-chloro-
- Propane, 1-chloro-2-methyl- + Propane, 2-methoxy-2-methyl-
- 2-Pyrrolidinone, 1-methyl- + Propane, 2-methoxy-2-methyl-
- Propane, 2-methoxy-2-methyl- + 1-Hexyne
- Propane, 2-methoxy-2-methyl- + 2-Hexyne
- Propane, 2-methoxy-2-methyl- + o-Xylene
- Benzene, 1,3-dimethyl- + Propane, 2-methoxy-2-methyl-
- p-Xylene + Propane, 2-methoxy-2-methyl-
- Propane, 2-methoxy-2-methyl- + Ethane, 1,2-dichloro-
- Propane, 2-methoxy-2-methyl- + Cyclohexane
- Propane, 2-methoxy-2-methyl- + Acetone
Find more mixtures with Propane, 2-methoxy-2-methyl-.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
- Kinematic Viscosities for Ether + Alkane Mixtures: Experimental Results and UNIFAC-VISCO Parameters
- Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
- (Solid + liquid) phase equilibria of binary mixtures containing N-methyl-2-pyrrolidinone and ethers at atmospheric pressure
- Phase equilibria for binary systems of octane boosters with 2,2,4-trimethylpentane
- Determination of excess molar enthalpies of the ternary system methyl tert-butyl ether + 1-pentanol + nonane at 298.15K Analysis and comparison with predicted values of the UNIFAC model and some empirical methods
- Liquid-liquid equilibrium data of water with neohexane, methylcyclohexane, tert-butyl methyl ether, n-heptane and vapor -liquid-liquid equilibrium with methane
- Thermodynamics of binary mixtures containing N-methyl-2-pyrrolidinone VLE measurements for systems with ethers Comparison with the Mod. UNIFAC (Do) and DISQUAC models Predictions for VLE, GE m, HEm and SLE?
- Infinite dilution activity coefficient measurements by inert gas stripping method
- Thermodynamics of isomeric hexynes +MTBE binary mixtures
- (Liquid + liquid) equilibria for the quaternary system water + methyl tert-butyl ether + ethanol + benzene at 303.15K
- Liquid liquid equilibria for the MTBE+water + salts systems at 298.15K
- Influence of temperature on thermodynamics of ethers + xylenes
- Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
- Study of the effect of increasing the chain length of the alkane in excess molar enthalpies of mixtures containing methyl tert-butyl ether, 1-propanol, alkane
- Phase equilibria and interfacial tensions in the systems methyl tert-butyl ether + acetone + cyclohexane, methyl tert-butyl ether + acetone and methyl tert-butyl ether + cyclohexane
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
- Isothermal vapour liquid equilibria in the binary and ternary systems composed of tert-butyl methyl ether, 3,3-dimethyl-2-butanone and 2,2-dimethyl-1-propanol
- Activity coefficients at infinite dilution measurements for organic solutes and water in the 1-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium bis(trifluoromethylsulfonyl)-imide ionic liquids The cation influence
- Study on the effect of increasing the chain length of the alkanol in excess molar enthalpies of mixtures containing 2-methoxy-2-methylpropane, 1-alkanol, decane
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Solubility of caprolactam in different organic solvents
- A novel static analytical apparatus for phase equilibrium measurements
- Liquid liquid equilibria at 298.15 K for ternary mixtures of methyl tert-butyl ether + methanol (or ethanol) + imidazolium-based ionic liquids at atmospheric pressure
- 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.
- Phase equilibria of (water + propionic acid or butyric acid + 2-methoxy- 2-methylpropane) ternary systems at 298.2 K and 323.2 K
- 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
- Determination and modeling for solid-liquid phase equilibrium of ternary caprolactam + cyclohexanone oxime + methyl tert-butyl ether system
- A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
- 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
- Liquid-liquid equilibrium measurement and thermodynamics modeling for the systems water + thioglycolic acid + isopropyl ether/methyl tert-butyl ether at 298.15 and 308.15 K
- Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
- Liquid-liquid equilibrium data and thermophysical properties for ternary systems composed of water, acetic acid and different solvents
- Excess molar enthalpies of the ternary mixtures: methyl tert-butyl ether +2-methylpentane + (n-decane or n-dodecane) at the temperature 298.15 K
- Excess molar enthalpies of the ternary mixtures: (methyl tert-butyl ether or 2-methyltetrahydrofuran + cyclohexane + 2,2,4- trimethylpentane} at the temperature 298.15 K
- Densities and derived thermodynamic properties of the binary systems of 1,1-dimethylethyl methyl ether with allyl methacrylate, butyl methacrylate, methacrylic acid, and vinyl acetate at T = (298.15 and 308.15) K
- Excess molar enthalpies of the ternary mixtures: {tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether + n-dodecane} at the temperature 298.15 K
- Quaternary (liquid + liquid) equilibria for (water + 1,1-dimethylethyl methyl ether + diisopropyl ether + toluene) at the temperature 298.15 K
- Quaternary (liquid + liquid) equilibria for (water + 2-propanol + 1,1-dimethylethyl methyl ether + diisopropyl ether) at the temperature 298.15 K
- Excess molar enthalpies of the ternary mixtures: (tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether + n-octane) at the temperature 298.15 K
- (Liquid + liquid) phase equilibria of 1-alkyl-3-methylimidazolium methylsulfate with alcohols, or ethers, or ketones
- Excess molar enthalpies of the ternary mixtures (1-hexene + tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether) at the temperature 298.15K.
- Excess enthalpy, density, and speed of sound determination for the ternary mixture (methyl tert-butyl ether + 1-butanol + n-hexane)
- (Vapor + liquid) equilibrium of the binary mixtures formed by acetonitrile with selected compounds at 95.5 kPa
- 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 measurements for organic solutes and water in the ionic liquid triethylsulphonium bis(trifluoromethylsulfonyl)imide
- Measurements of activity coefficients at infinite dilution of aliphatic and aromatic hydrocarbons, alcohols, thiophene, tetrahydrofuran, MTBE, and water in ionic liquid [BMIM][SCN] using GLC
- Volumetric behaviour of binary liquid systems composed of toluene, isooctane, and methyl tert-butyl ether at temperatures from (298.15 to 328.15) K
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
- Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
- Volumetric behaviour of the ternary liquid system composed of methyl tert-butyl ether, toluene, and isooctane at temperatures from (298.15 to 328.15) K: Experimental data and correlation
- Measurements of activity coefficients at infinite dilution of organic solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
- Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
- Volumetric and viscometric properties of binary mixtures of {methyl tert-butyl ether (MTBE) + alcohol} at several temperatures and p = 0.1 MPa: Experimental results and application of the ERAS model
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
- Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
- Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
- 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
- Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
- 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
- Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
- Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
- Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
- 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
- Measurement of critical temperatures and critical pressures for binary mixtures of methyl tert-butyl ether (MTBE) + alcohol and MTBE + alkane
- 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
- Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
- Experimental and theoretical excess molar enthalpies of ternary and binary mixtures containing 2-Methoxy-2-Methylpropane, 1-propanol, heptane
- 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
- Contribution to study of the thermodynamics properties of mixtures containing 2-methoxy-2-methylpropane, alkanol, alkane
- Measurement and correlation of critical properties for binary mixtures and ternary mixtures containing gasoline additives
- Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
- Solubility and solution thermodynamics of sorbic acid in eight pure organic solvents
- 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
- Volumetric behavior of the ternary system (methyl tert-butyl ether + methylbenzene + butan-1-ol) and its binary sub-system (methyl tert-butyl ether + butan-1-ol) within the temperature range (298.15 to 328.15) K
- 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
- Solubility measurement and correlation of the form A of ibrutinib in organic solvents from 278.15 to 323.15 K
- 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
- Liquid-liquid equilibrium for ternary systems of water + 2,2,3,3-tetrafluoro-1-propanol + isopropyl ether/tert-butyl methyl ether at 298.2, 308.2 K
- The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
- Liquid-liquid equilibria for azeotropic mixture of methyl tert-butyl ether and methanol with ionic liquids at different temperatures
- Liquid-liquid equilibrium study for ternary systems of water + propargyl alcohol + solvents at 308.2 K: Measurement and thermodynamic modelling
- Excess molar enthalpies of the ternary mixtures: methyl tert-butyl ether + 3-methylpentane + (n-decane or n-dodecane) at 298.15K
- Isothermal vapor-liquid equilibrium of binary and ternary systems of anisole, hexane, and toluene and ternary system of methyl tert-butyl ether, hexane, and toluene
- sothermal and Isobaric Vapor-Liquid Equilibrium and Excess Molar Enthalpy of the Binary Mixtures of 2-Methoxy-2-methylpropane + 2-Methyl-2-butanol or + 2-Butanol
- Solubility of Amorphous Clopidogrel Hydrogen Sulfate in Different Pure Solvents
- Solubility of Agomelatine Crystal Form I and Form II in Pure Solvents and (Isopropanol + Water) Mixtures
- Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
- Quaternary, Ternary, and Binary LLE Measurements for 2-Methoxy-2-methylpropane + Furfural + Acetic Acid + Water at Temperatures between 298 and 307 K
- Speed of Sound Measurements of 2-Methoxy-2-methylpropane in the Temperature Range of 293.15 and 673.15 K and for Pressures up to 10 MPa
- Liquid-Liquid Equilibria of Ionic Liquids-Water-Acetic Acid Mixtures
- Measurements and Thermodynamic Models for the Separation of 2-Methoxyethanol and Water Azeotropic Mixtures via Different Solvents
- Solid-Liquid Phase Equilibrium and Thermodynamic Properties of Olaparib in Selected Organic Solvents and (Tetrahydrofuran + MTBE, Acetonitrile + Isopropyl Alcohol) Binary Solvent Mixtures
- Solubility Measurement and Thermodynamic Modeling of N-(4-Methylphenyl-Z-3-chloro-2-(phenylthio)propenamide in 12 Pure Solvents at Temperatures Ranging from 278.15 to 318.15 K
- Physicochemical Properties of LiFSI Solutions II: LiFSI with Water, MTBE, and Anisole
- Vapor-Liquid Equilibrium Measurements of Ether Alcohol Blends for Investigation on Reformulated Gas
- Solubility Measurement and Correlation of Probenecid in 12 Pure Organic Solvents and Thermodynamic Properties of Mixing of Solutions
- Measurement and Correlation of the Solubility of Dienogest in Twelve Pure and Water + Methanol Binary Solvents at Temperatures from 273.15 to 318.15 K
- Solubility of Imidazoles in Ethers
- Mixing Properties for the Ternary Mixture Methyl tert-Butyl Ether + 1-Butanol + Decane at 298.15 K
- Vapor-Liquid Equilibria for the Binary Systems of Dimethoxymethane with Some Fuel Oxygenates
- Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
- Excess Molar Volumes and Surface Tensions of Xylene with Isopropyl Ether or Methyl tert-Butyl Ether at 298.15 K
- Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with tert-Butyl Methyl Ether and with tert-Amyl Methyl Ether
- Liquid-Liquid Equilibrium of MTBE + Ethanol + Water and MTBE + 1-Hexanol + Water over the Temperature Range of 288.15 to 308.15 K
- Experimental and Predicted Excess Molar Enthalpies of the Ternary System tert-Butyl Methyl Ether + 1-Pentanol + Decane at 298.15 K
- Vapor-Liquid Equilibrium Measurements of MTBE and TAME with Toluene
- Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique
- Vapor-Liquid Equilibria for the Ternary Systems of Methyl tert-Butyl Ether + Methanol + Methylcyclohexane and Methyl tert-Butyl Ether + Methanol + n-Heptane and Constituent Binary Systems at 313.15 K
- Liquid-Liquid Equilibria for the Ternary Systems Water + 3-Methyl-2-cyclopentenone with Ethyl Acetate or Methyl tert-Butyl Ether at 293.2 K
- Densities and Viscosities for the Ternary Systems of Methyl tert-Butyl Ether + Methanol + Benzene and Methyl tert-Butyl Ether + Methanol + Toluene and Their Sub-binary Systems at 298.15 K
- Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
- Phase Equilibrium Properties of Binary and Ternary Mixtures Containing 1,1-Dimethylethyl Methyl Ether, 1-Propanol, and Hexane at T ) 313.15 K
- Liquid-Liquid Equilibria of the Ternary System Water + Acetic Acid + Methyl tert-Butyl Ether
- Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
- Solubility of Artemisinin in Different Single and Binary Solvent Mixtures Between (284.15 and 323.15) K and NRTL Interaction Parameters
- Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
- Density, Viscosity, Vapor-Liquid Equilibrium, and Excess Molar Enthalpy of [Chloroform + Methyl tert-Butyl Ether]
- Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
- Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
- Excess Molar Enthalpies of Ternary and Binary Mixtures Containing 2-Methoxy-2-Methylpropane, Ethanol, and Nonane
- Excess Volumes of Ternary Mixtures 2,2,4-Trimethylpentane + Diisopropyl Ether or Methyl tert-Butyl Ether + Methanol, Ethanol, or 1-Propanol at 298.15 K
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Liquid Liquid Equilibria for the Ternary System 2-Methoxy-2-methylpropane + Phenol + Water
- Measurements of Liquid Liquid Equilibria for the Quaternary System 2-Methoxy-2-methylpropane + Phenol + Hydroquinone + Water at 313.15 K
- Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa
- Experimental Determination and Correlation of Liquid Liquid Equilibria for the Ternary System 2-Methoxy-2-methylpropane + o-Cresol + Water at 298.15 K and 313.15 K
- Densities and Viscosities of MTBE + Heptane or Octane at p ) 0.1 MPa from (273.15 to 363.15) K
- Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
- Phase Equilibria of (1-Ethyl-3-methylimidazolium Ethylsulfate + Hydrocarbon, + Ketone, and + Ether) Binary Systems
- Excess Enthalpy, Density, and Speed of Sound for the Ternary Mixture Methyl tert-Butyl Ether (1) + Butan-1-ol (2) + Octane (3)
- Measurement and Correlation of Liquid-Liquid Equilibrium Data for Water + Acetic Acid + Methyl tert-Butyl Ether + NaCl
- Excess Molar Enthalpies of Ternary and Binary Mixtures Containing 2-Methoxy-2-methylpropane, 1-Propanol, and Nonane
- Isobaric Vapor-Liquid Equilibria at 101.32 kPa and Densities, Speeds of Sound, and Refractive Indices at 298.15 K for MTBE or DIPE or TAME + 1-Propanol Binary Systems
- Vapor-Liquid Equilibria and Interfacial Tensions of the System Ethanol + 2-Methoxy-2-methylpropane
- Mixing Properties for Binary Liquid Mixtures of Methyl tert-Butyl Ether with Propylamine and Dipropylamine at Temperatures from (288.15 to 308.15) K
- Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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