- InChI
- InChI=1S/C5H12O/c1-4-5(2,3)6/h6H,4H2,1-3H3
- InChI Key
- MSXVEPNJUHWQHW-UHFFFAOYSA-N
- Formula
- C5H12O
- SMILES
- CCC(C)(C)O
- Molecular Weight1
- 88.15
- CAS
- 75-85-4
- Other Names
-
- 1,1-Dimethyl-1-propanol
- 2-Butanol, 2-methyl-
- 2-Methyl butanol-2
- 2-ethyl-2-propanol
- 2-methyl-2-butanol
- 2-methyl-2-butanol (tert-amyl alcohol)
- 2-methylbutan-2-ol
- 3-Methyl-butanol-(3)
- 3-Methylbutan-3-ol
- C2H5C(CH3)2OH
- Dimethyl ethyl carbinol
- Ethyl dimethyl carbinol
- Methyl-2 butanol-2
- Methyl-3 butanol-3
- NSC 25498
- t-Amyl alcohol
- tert-Isoamyl alcohol
- tert-Pentanol
- tert-amyl alcohol
- tert-pentyl alcohol
- ω : Acentric Factor.
- 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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- 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).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (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 |
|---|---|---|---|
| ω | 0.5494 | Relay (1.0) Calculated Property | |
| ΔcH°liquid | -3303.10 ± 0.46 | kJ/mol | NIST |
| Cp,liquid | 251.10 | J/mol×K | Partial Molar Heat Capacities and Partial Molar Volumes of All of the Isomeric (C3 to C5) Alkanols at Infinite Dilution in Water at 298.15 K |
| μ | 1.90 | debye | KDB |
| ΔfG° | -142.76 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-329.90; -329.30] | kJ/mol |
|
| ΔfH°gas | -329.90 | kJ/mol | KDB |
| ΔfH°gas | -329.30 | kJ/mol | NIST |
| ΔfH°liquid | -379.50 ± 0.54 | kJ/mol | NIST |
| ΔfusH° | 0.90 | kJ/mol | Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols |
| ΔvapH° | [49.20; 51.50] | kJ/mol |
|
| ΔvapH° | 50.17 | kJ/mol | NIST |
| ΔvapH° | 51.50 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 50.50 | kJ/mol | NIST |
| ΔvapH° | 50.20 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 50.10 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 49.20 | kJ/mol | NIST |
| IE | [9.80; 10.16] | eV |
|
| IE | 9.80 | eV | NIST |
| IE | 10.16 ± 0.03 | eV | NIST |
| log10WS | [0.08; 0.15] |
|
|
| log10WS | 0.08 | Aq. Solubility Prediction | |
| log10WS | 0.15 | Estimated Solubility | |
| logPoct/wat | 1.167 | Crippen Calculated Property | |
| McVol | 87.180 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | [3710.00; 3710.00] | kPa |
|
| Pc | 3710.00 | kPa | KDB |
| Pc | 3710.00 ± 20.00 | kPa | NIST |
| Pc | 3710.00 ± 40.00 | kPa | NIST |
| Inp | [596.60; 662.00] |
|
|
| Inp | 597.50 | NIST | |
| Inp | 597.90 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 652.00 | NIST | |
| Inp | 644.00 | NIST | |
| Inp | 628.00 | NIST | |
| Inp | 652.00 | NIST | |
| Inp | Outlier 662.00 | NIST | |
| Inp | 642.00 | NIST | |
| Inp | 644.00 | NIST | |
| Inp | 628.00 | NIST | |
| Inp | 652.00 | NIST | |
| Inp | Outlier 662.00 | NIST | |
| Inp | 642.00 | NIST | |
| Inp | 644.00 | NIST | |
| Inp | 628.00 | NIST | |
| Inp | 625.00 | NIST | |
| Inp | 614.00 | NIST | |
| Inp | 615.00 | NIST | |
| Inp | Outlier 596.60 | NIST | |
| Inp | 628.00 | NIST | |
| Inp | 619.00 | NIST | |
| Inp | 614.00 | NIST | |
| Inp | 622.00 | NIST | |
| Inp | 614.00 | NIST | |
| Inp | 625.00 | NIST | |
| Inp | 628.00 | NIST | |
| Inp | 630.00 | NIST | |
| Inp | 619.00 | NIST | |
| Inp | 659.00 | NIST | |
| Inp | 658.00 | NIST | |
| Inp | 629.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 628.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 628.00 | NIST | |
| Inp | 628.00 | NIST | |
| Inp | 634.00 | NIST | |
| Inp | 631.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 628.00 | NIST | |
| Inp | 628.00 | NIST | |
| Inp | 636.00 | NIST | |
| Inp | 636.00 | NIST | |
| Inp | 636.00 | NIST | |
| Inp | 628.00 | NIST | |
| Inp | 631.00 | NIST | |
| Inp | 636.00 | NIST | |
| Inp | 597.50 | NIST | |
| I | [966.00; 1048.00] |
|
|
| I | 1048.00 | NIST | |
| I | 1028.00 | NIST | |
| I | 1026.00 | NIST | |
| I | 1048.00 | NIST | |
| I | 1028.00 | NIST | |
| I | 1026.00 | NIST | |
| I | 1002.00 | NIST | |
| I | 1021.00 | NIST | |
| I | 1012.00 | NIST | |
| I | 1004.00 | NIST | |
| I | 1029.00 | NIST | |
| I | 1000.00 | NIST | |
| I | 1011.00 | NIST | |
| I | 1000.00 | NIST | |
| I | 1000.00 | NIST | |
| I | 997.00 | NIST | |
| I | 1003.00 | NIST | |
| I | 1003.00 | NIST | |
| I | 975.00 | NIST | |
| I | 1008.00 | NIST | |
| I | 987.00 | NIST | |
| I | 1015.00 | NIST | |
| I | 1014.00 | NIST | |
| I | Outlier 966.00 | NIST | |
| I | 975.00 | NIST | |
| I | 1048.00 | NIST | |
| I | 1026.00 | NIST | |
| I | 1029.00 | NIST | |
| I | 987.00 | NIST | |
| I | 1011.00 | NIST | |
| S°gas | 362.80 ± 6.70 | J/mol×K | NIST |
| S°liquid | 229.30 | J/mol×K | NIST |
| Tboil | [355.35; 376.15] | K |
|
| Tboil | 375.50 | K | KDB |
| Tboil | 375.20 | K | NIST |
| Tboil | 375.00 | K | NIST |
| Tboil | 375.40 | K | NIST |
| Tboil | 375.00 ± 0.50 | K | NIST |
| Tboil | 375.40 ± 0.40 | K | NIST |
| Tboil | Outlier 355.35 ± 0.40 | K | NIST |
| Tboil | 373.15 ± 2.00 | K | NIST |
| Tboil | 374.65 ± 1.00 | K | NIST |
| Tboil | 375.40 ± 1.00 | K | NIST |
| Tboil | 375.05 ± 0.50 | K | NIST |
| Tboil | 375.45 ± 0.50 | K | NIST |
| Tboil | 374.55 ± 1.00 | K | NIST |
| Tboil | 374.85 ± 0.50 | K | NIST |
| Tboil | 374.65 ± 1.00 | K | NIST |
| Tboil | 375.15 ± 1.00 | K | NIST |
| Tboil | 375.40 ± 1.00 | K | NIST |
| Tboil | 374.95 ± 0.50 | K | NIST |
| Tboil | 375.50 ± 0.30 | K | NIST |
| Tboil | 374.65 ± 1.00 | K | NIST |
| Tboil | 375.60 ± 0.60 | K | NIST |
| Tboil | 375.20 ± 0.50 | K | NIST |
| Tboil | 375.15 ± 0.50 | K | NIST |
| Tboil | 374.65 ± 1.00 | K | NIST |
| Tboil | 373.45 ± 1.50 | K | NIST |
| Tboil | 375.50 ± 0.10 | K | NIST |
| Tboil | 375.40 ± 0.20 | K | NIST |
| Tboil | 375.20 ± 0.50 | K | NIST |
| Tboil | Outlier 355.70 ± 0.50 | K | NIST |
| Tboil | 375.25 ± 0.50 | K | NIST |
| Tboil | 374.75 ± 0.50 | K | NIST |
| Tboil | 374.00 ± 3.00 | K | NIST |
| Tboil | 374.15 ± 2.00 | K | NIST |
| Tboil | 375.65 ± 2.00 | K | NIST |
| Tboil | 375.05 ± 0.50 | K | NIST |
| Tboil | 375.46 ± 0.20 | K | NIST |
| Tboil | 375.65 ± 2.00 | K | NIST |
| Tboil | 375.15 ± 2.00 | K | NIST |
| Tboil | 375.65 ± 2.00 | K | NIST |
| Tboil | 373.90 ± 2.00 | K | NIST |
| Tboil | 374.96 ± 0.50 | K | NIST |
| Tboil | 374.90 ± 1.00 | K | NIST |
| Tboil | 376.15 ± 2.00 | K | NIST |
| Tc | [543.70; 545.00] | K |
|
| Tc | 543.70 | K | KDB |
| Tc | 543.70 ± 0.50 | K | NIST |
| Tc | 543.70 ± 0.70 | K | NIST |
| Tc | 545.00 | K | NIST |
| Tc | 544.90 | K | NIST |
| Tfus | [262.75; 264.30] | K |
|
| Tfus | 264.30 | K | KDB |
| Tfus | 263.45 | K | Aq. Solubility Prediction |
| Tfus | 264.20 ± 0.50 | K | NIST |
| Tfus | 263.95 ± 0.50 | K | NIST |
| Tfus | 262.75 ± 0.60 | K | NIST |
| Ttriple | [264.00; 264.00] | K |
|
| Ttriple | 264.00 ± 0.20 | K | NIST |
| Ttriple | 264.00 ± 0.20 | K | NIST |
| Vc | 0.324 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 303.15 | 101.33 | 0.0028 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.15; 3758.85] | kPa | [264.35; 545.15] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.65600e+02 | |||
| Coefficient B | -1.19501e+04 | |||
| Coefficient C | -2.20829e+01 | |||
| Coefficient D | 1.24464e-05 | |||
| Temperature range, min. | 264.35 | |||
| Temperature range, max. | 545.15 | |||
| Pvap | 0.15 | kPa | 264.35 | Calculated Property |
| Pvap | 1.87 | kPa | 295.55 | Calculated Property |
| Pvap | 12.35 | kPa | 326.75 | Calculated Property |
| Pvap | 52.10 | kPa | 357.95 | Calculated Property |
| Pvap | 159.88 | kPa | 389.15 | Calculated Property |
| Pvap | 389.54 | kPa | 420.35 | Calculated Property |
| Pvap | 801.71 | kPa | 451.55 | Calculated Property |
| Pvap | 1457.58 | kPa | 482.75 | Calculated Property |
| Pvap | 2419.52 | kPa | 513.95 | Calculated Property |
| Pvap | 3758.85 | kPa | 545.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Amylene hydrate.
Mixtures
- Amylene hydrate + Water
- Sodium nitrate + Amylene hydrate + Water
- Potassium nitrate + Amylene hydrate + Water
- p-Coumaric acid + Amylene hydrate
- Amylene hydrate + Tetrahydrofuran
- Propylamine + Amylene hydrate
- Propylamine + Amylene hydrate + Tetrahydrofuran
- Amylene hydrate + Glycerin + Water
- 2-Butene, (Z)- + Amylene hydrate
- Amylene hydrate + Dimethyl ether
- Ethyl Chloride + Amylene hydrate
- Amylene hydrate + Ethane, 1,1-difluoro-
- Furfural + Amylene hydrate
- Amylene hydrate + Heptane
- n-Butyl ether + Amylene hydrate
- Amylene hydrate + Water + Phosphoric Acid
- Amylene hydrate + 1-Propanol, 2-methyl-
- Amylene hydrate + 4-CHLOROPHTHALIC ANHYDRIDE
- Amylene hydrate + Methyl Alcohol
- 2-Propanol + Amylene hydrate
Find more mixtures with Amylene hydrate.
Sources
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- Crippen Method
- Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
- The influence of cation, anion and temperature on the liquid-liquid equilibrium of some pentanols-water system
- Isothermal vapor-liquid equilibrium and excess molar enthalpies of the binary mixtures furfural + methyl isobutyl ketone, + 2-butanol and + 2-methyl-2-butanol
- Measurements and correlation at different temperatures of liquid-liquid equilibria of 2-butanol or 2-methyl-2-butanol + 1,2,3-propanetriol + water ternary systems
- Henry's law constants and infinite dilution activity coefficients of cis-2-butene, dimethylether, chloroethane, and 1,1-difluoroethane in methanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tert-butanol, 1-pentanol, 2-pentanol, 3-pentanol, 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol
- Molar heat capacities for (2-methyl-2-butanol + heptane) mixtures and cyclopentanol at temperatures from (284 to 353) K
- Speed of sound, density, and heat capacity for (2-methyl-2-butanol + heptane) at pressures up to 100 MPa and temperatures from (293 to 318) K. Experimental results and theoretical investigations
- (Liquid + liquid) equilibria in ternary aqueous mixtures of phosphoric acid with organic solvents at T = 298.2 K
- Excess molar volume, viscosity, and refractive index study for the ternary mixture {2-methyl-2-butanol (1) + tetrahydrofuran (2) + propylamine (3)} at different temperatures. Application of the ERAS-model and Peng Robinson Stryjek Vera equation of state
- Solubilities of some organic solutes in 1-ethyl-3-methylimidazolium acetate. Chromatographic measurements and predictions from COSMO-RS
- Solubilities of p-coumaric and caffeic acid in ionic liquids and organic solvents
- Excess molar enthalpies of the binary systems: (Dibutyl ether + isomers of pentanol) at T = (298.15 and 308.15) K
- Temperature of maximum density for aqueous mixtures of three pentanol isomers
- Solution enthalpies of 1-bromoadamantane in monoalcohols at 298.15K
- 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
- Solubilities of 3-Chlorophthalic Anhydride and 4-Chlorophthalic Anhydride in Different Pure Solvents
- Proposal for a Viscous Test Mixture Densities, Viscosities, and Vapor Liquid Equilibrium Data of the Binary Mixture 2-Methyl-2-butanol + 2-Methyl-1-propanol
- Ternary and Binary LLE Measurements for Solvent (4- Methyl-2-pentanone and 2-Methyl-2-butanol) + Furfural + Water between 298 and 401 K
- 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
- Liquid-Liquid Extraction of Biobased Isobutanol from an Aqueous Solution
- Measurement and Correlation of Solubility of Marbofloxacin in 12 Pure Solvents from 283.15 to 328.15 K
- Henry's law constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol
- Partial Molar Heat Capacities and Partial Molar Volumes of All of the Isomeric (C3 to C5) Alkanols at Infinite Dilution in Water at 298.15 K
- Experimental and Predicted Results of Anomeric Equilibrium of Glucose in Alcohols
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
- Density, Viscosity, Excess Molar Volume, and Viscosity Deviation of Three Amyl Alcohols + Ethanol Binary Mixtures from 293.15 to 323.15 K
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
- Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of N,N-Dimethylacetamide (1) + 2-Methylbutan-2-ol (2) + Ethyl Acetate (3) at 298.15 K for the Liquid Region and at Ambient Pressure
- Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
- Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
- Vapor-Liquid Equilibria Data for Methanol + 2-Propanol+ 2-Methyl-2-butanol and Constituent Binary Systems at 101.3 kPa
- Excess Molar Enthalpies of 2-Methyl-2-butanol (1) + 1-Alkanols (C1-C5) (2) at 298.15 K
- Surface Tensions of Three Amyl Alcohol + Ethanol Binary Mixtures from (293.15 to 323.15) K
- Volumetric Properties of Highly Nonideal Binary Mixtures Containing Ethanoic Acid and Propanoic Acid with Butan-2-ol, Methyl-2-propanol, and 2-Methyl-2-butanol at Different Temperatures
- Vapor Liquid Equilibria, Excess Enthalpy, and Excess Volume of Binary Mixtures Containing an Alcohol (1-Butanol, 2-Butanol, or 2-Methyl-2-butanol) and 2-Ethoxy-2-methylbutane
- Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
- Solubility of Flavonoids in Organic Solvents
- Densities and Viscosities of Binary Liquid Mixtures of 2-Butanone with Branched Alcohols at (293.15 to 313.15) K
- Study of the Effects of Temperature and Pressure on the Thermodynamic and Acoustic Properties of Pentan-1-ol, 2-Methyl-2-butanol, and Cyclopentanol in the Pressure Range from (0.1 to 100) MPa and Temperature from (293 to 318) K
- Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
- Solubilities of Cinnamic Acid Esters in Organic Solvents
- Vapor-Liquid Equilibria in Binary Systems Formed by n-Hexane with Alcohols
- Temperature Dependence of Limiting Activity Coefficients, Henry s Law Constants, and Related Infinite Dilution Properties of Branched Pentanols in Water. Measurement, Critical Compilation, Correlation, and Recommended Data
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
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