- InChI
- InChI=1S/C6H14O/c1-5-6(2,3)7-4/h5H2,1-4H3
- InChI Key
- HVZJRWJGKQPSFL-UHFFFAOYSA-N
- Formula
- C6H14O
- SMILES
- CCC(C)(C)OC
- Molecular Weight1
- 102.17
- CAS
- 994-05-8
- Other Names
-
- 1,1-DIMETHYLPROPYL METHYL ETHER
- 2-METHYL-2-METHOXYBUTANE
- 2-Methoxy-2-methylbutane
- Ether, methyl tert-pentyl
- Methyl 2-methyl-2-butyl ether
- Methyl tert-pentyl ether
- TERT-AMYL METHYL ETHER
- methyl 1,1-dimethylpropyl ether
- methyl tert-amyl ether
- tert-pentyl methyl ether
- 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).
- 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).
- 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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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | -4020.07 ± 0.73 | kJ/mol | NIST |
| ΔfG° | -102.52 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -306.50 ± 1.10 | kJ/mol | NIST |
| ΔfH°liquid | -341.79 ± 0.79 | kJ/mol | NIST |
| ΔfusH° | 5.07 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [33.50; 35.80] | kJ/mol |
|
| ΔvapH° | 35.30 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 34.80 | kJ/mol | NIST |
| ΔvapH° | 35.50 ± 1.00 | kJ/mol | NIST |
| ΔvapH° | 35.20 | kJ/mol | NIST |
| ΔvapH° | 35.00 | kJ/mol | NIST |
| ΔvapH° | 35.80 | kJ/mol | NIST |
| ΔvapH° | Outlier 33.50 | kJ/mol | 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 | [655.00; 678.00] |
|
|
| Inp | 672.50 | NIST | |
| Inp | 674.00 | NIST | |
| Inp | Outlier 655.00 | NIST | |
| Inp | 673.00 | NIST | |
| Inp | 668.30 | NIST | |
| Inp | 678.00 | NIST | |
| Inp | 666.00 | NIST | |
| Inp | 672.50 | NIST | |
| I | [790.00; 790.00] |
|
|
| I | 790.00 | NIST | |
| I | 790.00 | NIST | |
| Tboil | [359.20; 359.57] | K |
|
| Tboil | 359.52 | K | Vapor-L... |
| Tboil | 359.30 ± 0.30 | K | NIST |
| Tboil | 359.20 ± 0.30 | K | NIST |
| Tboil | 359.50 | K | NIST |
| Tboil | 359.57 ± 0.10 | K | NIST |
| Tc | 531.48 | K | Joback Calculated Property |
| Tfus | 182.03 | K | Joback Calculated Property |
| 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 | 222.00 | J/mol×K | 298.00 | NIST |
| η | [0.0002612; 0.0072406] | Pa×s | [182.03; 355.87] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 6.00e-3 7.00e-3 200 250 300 350 | ||||
| η | 0.0072406 | Pa×s | 182.03 | Joback Calculated Property |
| η | 0.0028457 | Pa×s | 211.00 | Joback Calculated Property |
| η | 0.0014013 | Pa×s | 239.98 | Joback Calculated Property |
| η | 0.0008039 | Pa×s | 268.95 | Joback Calculated Property |
| η | 0.0005138 | Pa×s | 297.92 | Joback Calculated Property |
| η | 0.0003555 | Pa×s | 326.90 | Joback Calculated Property |
| η | 0.0002612 | Pa×s | 355.87 | Joback Calculated Property |
| ΔvapH | [32.10; 36.60] | kJ/mol | [295.50; 352.50] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 32 33 34 35 36 37 300 320 340 | ||||
| ΔvapH | 35.70 ± 1.00 | kJ/mol | 295.50 | NIST |
| ΔvapH | 34.30 | kJ/mol | 326.50 | NIST |
| ΔvapH | 33.80 | kJ/mol | 332.50 | NIST |
| ΔvapH | 33.70 | kJ/mol | 333.50 | NIST |
| ΔvapH | 33.40 | kJ/mol | 338.00 | NIST |
| ΔvapH | 32.10 ± 0.50 | kJ/mol | 352.50 | NIST |
| ΔvapH | 36.60 ± 0.10 | kJ/mol | 352.50 | NIST |
| ΔvapH | 34.50 ± 0.20 | kJ/mol | 352.50 | NIST |
| Pvap | [2.69; 86.70] | kPa | [274.20; 353.15] |
|
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 280 300 320 340 | ||||
| Pvap | 2.69 | kPa | 274.20 | Determi... |
| Pvap | 3.00 | kPa | 276.20 | Determi... |
| Pvap | 3.31 | kPa | 278.20 | Determi... |
| Pvap | 3.80 | kPa | 280.20 | Determi... |
| Pvap | 4.42 | kPa | 282.80 | Determi... |
| Pvap | 4.68 | kPa | 283.80 | Determi... |
| Pvap | 5.69 | kPa | 287.80 | Determi... |
| Pvap | 7.60 | kPa | 292.90 | Determi... |
| Pvap | 9.14 | kPa | 297.80 | Determi... |
| Pvap | 12.31 | kPa | 302.80 | Determi... |
| Pvap | 14.55 | kPa | 307.80 | Determi... |
| Pvap | 86.70 | kPa | 353.15 | Thermod... |
| n0 | [1.38541; 1.38860] | [293.15; 298.15] |
|
|
|
T(K) Refractive Index 1.39 1.39 1.39 1.39 1.39 1.39 1.39 294 296 298 | ||||
| n0 | 1.38860 | 293.15 | A novel... | |
| n0 | 1.38614 | 293.15 | Isother... | |
| n0 | 1.38620 | 293.15 | Vapor-L... | |
| n0 | 1.38541 | 298.15 | Quatern... | |
| n0 | 1.38670 | 298.15 | Solubil... | |
| n0 | 1.38712 | 298.15 | Vapor L... | |
| n0 | 1.38587 | 298.15 | Isobari... | |
| n0 | 1.38736 | 298.15 | Atmosph... | |
| ρl | [736.50; 765.68] | kg/m3 | [298.15; 328.15] |
|
|
T(K) Liquid Density (kg/m3) 735 740 745 750 755 760 765 300 310 320 | ||||
| ρl | 765.60 | kg/m3 | 298.15 | Thermop... |
| ρl | 765.68 | kg/m3 | 298.15 | Binary ... |
| ρl | 756.30 | kg/m3 | 308.15 | Thermop... |
| ρl | 746.30 | kg/m3 | 318.15 | Thermop... |
| ρl | 741.40 | kg/m3 | 323.15 | Thermop... |
| ρl | 736.50 | kg/m3 | 328.15 | Thermop... |
| αdiff | [4.20e-08; 2.54e-07] | m2/s | [477.88; 522.45] |
|
|
T(K) Thermal diffusivity (m2/s) 5.00e-8 1.00e-7 1.50e-7 2.00e-7 2.50e-7 480 500 520 | ||||
| αdiff | 2.54e-07 | m2/s | 477.88 | Thermal... |
| αdiff | 2.30e-07 | m2/s | 483.74 | Thermal... |
| αdiff | 2.13e-07 | m2/s | 487.65 | Thermal... |
| αdiff | 1.90e-07 | m2/s | 493.04 | Thermal... |
| αdiff | 1.63e-07 | m2/s | 499.05 | Thermal... |
| αdiff | 1.45e-07 | m2/s | 502.72 | Thermal... |
| αdiff | 1.21e-07 | m2/s | 508.18 | Thermal... |
| αdiff | 1.05e-07 | m2/s | 511.38 | Thermal... |
| αdiff | 7.83e-08 | m2/s | 517.41 | Thermal... |
| αdiff | 4.20e-08 | m2/s | 522.45 | Thermal... |
Datasets
Speed of sound, m/s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Speed of sound, m/s - Liquid |
| 293.15 | 0.00 | 1133.33 |
| 303.15 | 10.00 | 1089.4 |
| 313.15 | 10.00 | 1046.4 |
| 323.15 | 20.00 | 1004.19 |
| 333.15 | 20.00 | 962.62 |
| 343.15 | 40.00 | 921.56 |
| 353.15 | 60.00 | 880.86 |
| 363.15 | 90.00 | 840.4 |
| 373.15 | 120.00 | 800.06 |
| 383.15 | 160.00 | 759.72 |
| 393.15 | 200.00 | 719.27 |
| 403.15 | 240.00 | 678.61 |
| 413.15 | 300.00 | 637.63 |
| 423.15 | 360.00 | 596.25 |
| 433.15 | 440.00 | 554.37 |
| 443.15 | 540.00 | 511.92 |
| 453.15 | 660.00 | 468.81 |
| 463.15 | 820.00 | 424.99 |
| 473.15 | 1010.00 | 380.39 |
| 483.15 | 1240.00 | 334.95 |
| 488.15 | 1370.00 | 311.9 |
| 493.15 | 1520.00 | 288.63 |
| 498.15 | 1680.00 | 265.12 |
| 503.15 | 1860.00 | 241.38 |
| 508.15 | 2060.00 | 217.4 |
| 513.15 | 2270.00 | 193.18 |
| 518.15 | 2500.00 | 168.7 |
| 523.15 | 2760.00 | 143.98 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [267.96; 381.22] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.53756e+01 | |||
| Coefficient B | -3.42321e+03 | |||
| Coefficient C | -4.10770e+01 | |||
| Temperature range, min. | 267.96 | |||
| Temperature range, max. | 381.22 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
| Pvap | 1.33 | kPa | 267.96 | Calculated Property |
| Pvap | 2.95 | kPa | 280.54 | Calculated Property |
| Pvap | 6.01 | kPa | 293.13 | Calculated Property |
| Pvap | 11.47 | kPa | 305.71 | Calculated Property |
| Pvap | 20.64 | kPa | 318.30 | Calculated Property |
| Pvap | 35.29 | kPa | 330.88 | Calculated Property |
| Pvap | 57.69 | kPa | 343.47 | Calculated Property |
| Pvap | 90.68 | kPa | 356.05 | Calculated Property |
| Pvap | 137.68 | kPa | 368.64 | Calculated Property |
| Pvap | 202.67 | kPa | 381.22 | Calculated Property |
| Pvap | [1.62e-05; 2960.51] | kPa | [160.00; 534.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 5.94177e+01 | |||
| Coefficient B | -5.93502e+03 | |||
| Coefficient C | -6.59117e+00 | |||
| Coefficient D | 3.80421e-06 | |||
| Temperature range, min. | 160.00 | |||
| Temperature range, max. | 534.00 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 200 300 400 500 | ||||
| Pvap | 1.62e-05 | kPa | 160.00 | Calculated Property |
| Pvap | 7.85e-03 | kPa | 201.56 | Calculated Property |
| Pvap | 0.38 | kPa | 243.11 | Calculated Property |
| Pvap | 5.09 | kPa | 284.67 | Calculated Property |
| Pvap | 32.54 | kPa | 326.22 | Calculated Property |
| Pvap | 128.71 | kPa | 367.78 | Calculated Property |
| Pvap | 369.86 | kPa | 409.33 | Calculated Property |
| Pvap | 852.45 | kPa | 450.89 | Calculated Property |
| Pvap | 1680.65 | kPa | 492.44 | Calculated Property |
| Pvap | 2960.51 | kPa | 534.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Butane, 2-methoxy-2-methyl-.
Mixtures
- Butane, 2-methoxy-2-methyl- + 2-Pyrrolidinone, 1-methyl-
- n-Hexane + Butane, 2-methoxy-2-methyl-
- Butane, 2-methoxy-2-methyl- + Methyl Alcohol
- n-Hexane + Butane, 2-methoxy-2-methyl- + Methyl Alcohol
- Butane, 2-methoxy-2-methyl- + Ethanol
- Butane, 2-methoxy-2-methyl- + Water
- Butane, 2-methoxy-2-methyl- + Furfural + Water
- Butane, 2-methoxy-2-methyl- + Acetic acid + Water
- Butane, 2-methoxy-2-methyl- + Benzene, 1,3-dimethyl-
- Butane, 2-methoxy-2-methyl- + 1H-Imidazole
- Butane, 2-methoxy-2-methyl- + 1H-Imidazole, 2-methyl-
- Butane, 2-methoxy-2-methyl- + 1H-Imidazole, 1,2-dimethyl-
- Butane, 2-methoxy-2-methyl- + «beta» Carotene
- Butane, 2-methoxy-2-methyl- + Cyclohexane + «beta» Carotene
- n-Hexane + Butane, 2-methoxy-2-methyl- + «beta» Carotene
- Toluene + Butane, 2-methoxy-2-methyl- + «beta» Carotene
- Toluene + Butane, 2-methoxy-2-methyl-
- Butane, 2-methoxy-2-methyl- + Heptane
- Butane, 2-methoxy-2-methyl- + Methyl Alcohol + Water
- Butane, 2-methoxy-2-methyl- + Ethanol + Water
Find more mixtures with Butane, 2-methoxy-2-methyl-.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- (Solid + liquid) phase equilibria of binary mixtures containing N-methyl-2-pyrrolidinone and ethers at atmospheric pressure
- 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?
- Vapour liquid equilibrium of octane enhancing additives in gasolines 7: Total pressure data and gE for the ternary mixture tert-amyl methyl ether (TAME), methanol and hexane at 313.15K
- Infinite dilution activity coefficient measurements by inert gas stripping method
- Isothermal vapor liquid equilibrium at 333.15K, excess molar volumes and refractive indices at 298.15K for mixtures of tert-amyl methyl ether + ethanol + 2,2,4-trimethylpentane
- Measurement and theoretical prediction of the vapor-liquid equilibrium, densities and interfacial tensions of the system hexane + 2-methoxy-2-methylbutane
- Liquid-liquid equilibria for ternary mixtures of methyl tert-amyl ether + methanol (or ethanol) + imidazolium-based ionic liquids at 298.15 K
- Volumetric behavior of the ternary system benzene-2-methoxy-2-methylbutane-2,2,4-trimethylpentane and all binary sub-systems at temperature range (298.15 - 318.15) K
- A novel static analytical apparatus for phase equilibrium measurements
- 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
- 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
- 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)
- (Liquid + liquid) phase equilibria of 1-alkyl-3-methylimidazolium methylsulfate with alcohols, or ethers, or ketones
- Activity coefficients at infinite dilution measurements for organic solutes and water in 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 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
- 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
- Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
- 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
- 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-methylbutane + Furfural + Acetic Acid + Water at Temperatures between 298 and 341 K
- 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
- Thermophysical Study of Binary Systems of tert-Amyl Methyl Ether with n-Hexane and m-Xylene
- Solubility of Imidazoles in Ethers
- Determination of Ambient Temperature Vapor Pressures and Vaporization Enthalpies of Branched Ethers
- Oxygenated Gasoline Additives: Saturated Heat Capacities between (277 and 355) K
- Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with tert-Butyl Methyl Ether and with tert-Amyl Methyl Ether
- 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 Equilibrium in the Binary Systems 2-Butanol + tert-Amyl Methyl Ether, 2-Butanol + Heptane, and Heptane + tert-Amyl Methyl Ether
- Vapor Liquid Equilibria and Interfacial Tensions of the System Ethanol + 2-Methoxy-2-methylbutane
- Binary Liquid-Liquid Equilibrium (LLE) for Methyl tert-Amyl Ether (TAME) + Water from (288.15 to 313.15) K and Ternary LLE for Systems of TAME + C1-C4 Alcohols + Water at 298.15 K
- 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
- Isothermal Vapor-Liquid Equilibria in the Two Binary and the Ternary Systems Composed of tert-Amyl Methyl Ether, tert-Butanol, and Isooctane
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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