- 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-Methyl-2-butanol
- 2-Methylbutan-2-ol
- 2-ethyl-2-propanol
- 2-methyl-2-butanol (tert-amyl alcohol)
- 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
- TERT-PENTANOL
- TERT-PENTYL ALCOHOL
- t-Amyl alcohol
- tert-Amyl alcohol
- tert-Isoamyl alcohol
- 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 |
|---|---|---|---|
| ΔcH°liquid | -3303.10 ± 0.46 | kJ/mol | NIST |
| 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 Ca... |
| 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. Sol... | |
| log10WS | 0.15 | Estimat... | |
| 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 | 1011.00 | NIST | |
| I | 975.00 | NIST | |
| I | 1048.00 | NIST | |
| I | 1026.00 | NIST | |
| I | 1029.00 | NIST | |
| I | 987.00 | 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. Sol... |
| Tfus | 264.20 ± 0.50 | K | NIST |
| Tfus | 263.95 ± 0.50 | K | NIST |
| Tfus | 262.75 ± 0.60 | K | NIST |
| Ttriple | 264.00 ± 0.20 | K | NIST |
| Vc | 0.324 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [167.70; 222.80] | J/mol×K | [381.35; 576.05] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 170 180 190 200 210 220 400 450 500 550 | ||||
| Cp,gas | 167.70 ± 4.10 | J/mol×K | 381.35 | NIST |
| Cp,gas | 168.60 ± 4.10 | J/mol×K | 384.65 | NIST |
| Cp,gas | 169.40 ± 4.10 | J/mol×K | 387.45 | NIST |
| Cp,gas | 171.90 ± 4.10 | J/mol×K | 396.05 | NIST |
| Cp,gas | 172.40 ± 4.10 | J/mol×K | 398.05 | NIST |
| Cp,gas | 180.30 ± 4.10 | J/mol×K | 425.95 | NIST |
| Cp,gas | 194.30 ± 4.10 | J/mol×K | 475.25 | NIST |
| Cp,gas | 207.20 ± 4.10 | J/mol×K | 520.85 | NIST |
| Cp,gas | 222.80 ± 4.10 | J/mol×K | 576.05 | NIST |
| Cp,liquid | [244.14; 248.86] | J/mol×K | [294.40; 298.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 244 245 246 247 248 249 295 296 297 298 | ||||
| Cp,liquid | 244.14 | J/mol×K | 294.40 | NIST |
| Cp,liquid | 247.15 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 248.86 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 248.86 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 247.30 | J/mol×K | 298.15 | NIST |
| η | [0.0025042; 0.0058667] | Pa×s | [288.15; 313.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 2.50e-3 3.00e-3 3.50e-3 4.00e-3 4.50e-3 5.00e-3 5.50e-3 6.00e-3 290 300 310 | ||||
| η | 0.0058667 | Pa×s | 288.15 | Excess ... |
| η | 0.0051080 | Pa×s | 293.15 | Densiti... |
| η | 0.0034781 | Pa×s | 298.15 | Excess ... |
| η | 0.0044740 | Pa×s | 298.15 | Densiti... |
| η | 0.0039086 | Pa×s | 303.15 | Densiti... |
| η | 0.0025042 | Pa×s | 308.15 | Excess ... |
| η | 0.0033871 | Pa×s | 308.15 | Densiti... |
| η | 0.0029086 | Pa×s | 313.15 | Densiti... |
| ΔfusH | [0.17; 4.46] | kJ/mol | [146.00; 264.00] |
|
|
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 0 1 2 3 4 150 200 250 | ||||
| ΔfusH | 1.96 | kJ/mol | 146.00 | NIST |
| ΔfusH | 2.00 | kJ/mol | 192.50 | NIST |
| ΔfusH | 0.17 | kJ/mol | 213.00 | NIST |
| ΔfusH | 2.24 | kJ/mol | 262.70 | NIST |
| ΔfusH | 4.46 | kJ/mol | 264.00 | NIST |
| ΔfusH | 4.46 | kJ/mol | 264.00 | NIST |
| ΔvapH | [39.04; 52.80] | kJ/mol | [313.00; 375.40] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 40 45 50 320 340 360 | ||||
| ΔvapH | 48.40 ± 0.20 | kJ/mol | 313.00 | NIST |
| ΔvapH | 49.00 | kJ/mol | 327.50 | NIST |
| ΔvapH | 46.40 ± 0.20 | kJ/mol | 328.00 | NIST |
| ΔvapH | 48.50 | kJ/mol | 331.00 | NIST |
| ΔvapH | 52.80 | kJ/mol | 336.50 | NIST |
| ΔvapH | 51.20 | kJ/mol | 338.00 | NIST |
| ΔvapH | 47.30 | kJ/mol | 341.50 | NIST |
| ΔvapH | 44.20 ± 0.10 | kJ/mol | 343.00 | NIST |
| ΔvapH | 45.80 | kJ/mol | 349.50 | NIST |
| ΔvapH | 42.00 ± 0.10 | kJ/mol | 358.00 | NIST |
| ΔvapH | 40.30 ± 0.10 | kJ/mol | 368.00 | NIST |
| ΔvapH | 39.04 | kJ/mol | 375.40 | NIST |
| ν | [0.0000021; 0.0000051] | m2/s | [293.15; 323.15] |
|
|
T(K) Kinematic viscosity (m2/s) 2.00e-6 2.50e-6 3.00e-6 3.50e-6 4.00e-6 4.50e-6 5.00e-6 300 310 320 | ||||
| ν | 0.0000051 | m2/s | 293.15 | Density... |
| ν | 0.0000045 | m2/s | 298.15 | Density... |
| ν | 0.0000039 | m2/s | 303.15 | Density... |
| ν | 0.0000034 | m2/s | 308.15 | Density... |
| ν | 0.0000029 | m2/s | 313.15 | Density... |
| ν | 0.0000025 | m2/s | 318.15 | Density... |
| ν | 0.0000021 | m2/s | 323.15 | Density... |
| Pvap | [2.81; 102.61] | kPa | [303.29; 375.53] |
|
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 320 340 360 | ||||
| Pvap | 2.81 | kPa | 303.29 | Vapor-L... |
| Pvap | 2.85 | kPa | 303.47 | Vapor-L... |
| Pvap | 3.16 | kPa | 304.67 | Vapor-L... |
| Pvap | 3.40 | kPa | 305.75 | Vapor-L... |
| Pvap | 3.43 | kPa | 305.90 | Vapor-L... |
| Pvap | 4.08 | kPa | 308.35 | Vapor-L... |
| Pvap | 4.31 | kPa | 309.12 | Vapor-L... |
| Pvap | 4.55 | kPa | 309.86 | Vapor-L... |
| Pvap | 4.80 | kPa | 310.61 | Vapor-L... |
| Pvap | 5.15 | kPa | 311.64 | Vapor-L... |
| Pvap | 5.43 | kPa | 312.47 | Vapor-L... |
| Pvap | 5.69 | kPa | 313.15 | Vapor-L... |
| Pvap | 5.77 | kPa | 313.38 | Vapor-L... |
| Pvap | 6.08 | kPa | 314.17 | Vapor-L... |
| Pvap | 6.59 | kPa | 315.44 | Vapor-L... |
| Pvap | 7.31 | kPa | 317.09 | Vapor-L... |
| Pvap | 7.99 | kPa | 318.64 | Vapor-L... |
| Pvap | 8.36 | kPa | 319.37 | Vapor-L... |
| Pvap | 8.61 | kPa | 319.86 | Vapor-L... |
| Pvap | 8.84 | kPa | 320.32 | Vapor-L... |
| Pvap | 9.36 | kPa | 321.32 | Vapor-L... |
| Pvap | 9.99 | kPa | 322.44 | Vapor-L... |
| Pvap | 10.41 | kPa | 323.15 | Vapor-L... |
| Pvap | 10.41 | kPa | 323.15 | Vapor-L... |
| Pvap | 10.49 | kPa | 323.27 | Vapor-L... |
| Pvap | 11.03 | kPa | 324.11 | Vapor-L... |
| Pvap | 11.51 | kPa | 324.91 | Vapor-L... |
| Pvap | 12.03 | kPa | 325.71 | Vapor-L... |
| Pvap | 12.55 | kPa | 326.45 | Vapor-L... |
| Pvap | 13.05 | kPa | 327.18 | Vapor-L... |
| Pvap | 13.36 | kPa | 327.62 | Vapor-L... |
| Pvap | 13.97 | kPa | 328.41 | Vapor-L... |
| Pvap | 14.65 | kPa | 329.33 | Vapor-L... |
| Pvap | 15.31 | kPa | 330.15 | Vapor-L... |
| Pvap | 15.97 | kPa | 330.98 | Vapor-L... |
| Pvap | 16.67 | kPa | 331.80 | Vapor-L... |
| Pvap | 17.29 | kPa | 332.46 | Vapor-L... |
| Pvap | 17.87 | kPa | 333.15 | Vapor-L... |
| Pvap | 17.87 | kPa | 333.15 | Vapor-L... |
| Pvap | 17.99 | kPa | 333.26 | Vapor-L... |
| Pvap | 18.65 | kPa | 333.99 | Vapor-L... |
| Pvap | 19.32 | kPa | 334.69 | Vapor-L... |
| Pvap | 20.03 | kPa | 335.45 | Vapor-L... |
| Pvap | 19.33 | kPa | 335.75 | Vapor p... |
| Pvap | 19.84 | kPa | 336.04 | Vapor L... |
| Pvap | 20.67 | kPa | 336.05 | Vapor-L... |
| Pvap | 21.31 | kPa | 336.68 | Vapor-L... |
| Pvap | 21.96 | kPa | 337.31 | Vapor-L... |
| Pvap | 22.63 | kPa | 337.97 | Vapor-L... |
| Pvap | 22.87 | kPa | 338.15 | Vapor-L... |
| Pvap | 23.47 | kPa | 338.69 | Vapor-L... |
| Pvap | 22.66 | kPa | 339.03 | Vapor p... |
| Pvap | 23.97 | kPa | 339.15 | Vapor-L... |
| Pvap | 24.67 | kPa | 339.68 | Vapor-L... |
| Pvap | 25.35 | kPa | 340.31 | Vapor-L... |
| Pvap | 26.00 | kPa | 340.83 | Vapor-L... |
| Pvap | 26.67 | kPa | 341.39 | Vapor-L... |
| Pvap | 27.33 | kPa | 341.90 | Vapor-L... |
| Pvap | 26.00 | kPa | 341.93 | Vapor p... |
| Pvap | 27.97 | kPa | 342.40 | Vapor-L... |
| Pvap | 28.67 | kPa | 342.92 | Vapor-L... |
| Pvap | 28.95 | kPa | 343.15 | Vapor-L... |
| Pvap | 29.31 | kPa | 343.42 | Vapor-L... |
| Pvap | 30.01 | kPa | 343.94 | Vapor-L... |
| Pvap | 30.67 | kPa | 344.47 | Vapor-L... |
| Pvap | 29.33 | kPa | 344.54 | Vapor p... |
| Pvap | 29.94 | kPa | 344.75 | Vapor L... |
| Pvap | 31.35 | kPa | 344.91 | Vapor-L... |
| Pvap | 32.07 | kPa | 345.39 | Vapor-L... |
| Pvap | 32.67 | kPa | 345.78 | Vapor-L... |
| Pvap | 33.48 | kPa | 346.35 | Vapor-L... |
| Pvap | 32.66 | kPa | 346.91 | Vapor p... |
| Pvap | 34.67 | kPa | 347.18 | Vapor-L... |
| Pvap | 35.32 | kPa | 347.57 | Vapor-L... |
| Pvap | 36.07 | kPa | 348.07 | Vapor-L... |
| Pvap | 36.71 | kPa | 348.49 | Vapor-L... |
| Pvap | 37.36 | kPa | 348.88 | Vapor-L... |
| Pvap | 36.00 | kPa | 349.10 | Vapor p... |
| Pvap | 38.01 | kPa | 349.27 | Vapor-L... |
| Pvap | 38.64 | kPa | 349.64 | Vapor-L... |
| Pvap | 39.32 | kPa | 350.08 | Vapor-L... |
| Pvap | 39.96 | kPa | 350.49 | Vapor-L... |
| Pvap | 40.64 | kPa | 350.83 | Vapor-L... |
| Pvap | 41.31 | kPa | 351.20 | Vapor-L... |
| Pvap | 39.96 | kPa | 351.29 | Vapor L... |
| Pvap | 40.00 | kPa | 351.52 | Vapor p... |
| Pvap | 42.08 | kPa | 351.67 | Vapor-L... |
| Pvap | 42.65 | kPa | 351.95 | Vapor-L... |
| Pvap | 43.35 | kPa | 352.30 | Vapor-L... |
| Pvap | 44.00 | kPa | 352.73 | Vapor-L... |
| Pvap | 44.65 | kPa | 353.02 | Vapor-L... |
| Pvap | 44.87 | kPa | 353.15 | Vapor-L... |
| Pvap | 45.35 | kPa | 353.44 | Vapor-L... |
| Pvap | 45.97 | kPa | 353.73 | Vapor-L... |
| Pvap | 44.00 | kPa | 353.75 | Vapor p... |
| Pvap | 46.63 | kPa | 354.10 | Vapor-L... |
| Pvap | 47.28 | kPa | 354.41 | Vapor-L... |
| Pvap | 47.95 | kPa | 354.72 | Vapor-L... |
| Pvap | 48.65 | kPa | 355.11 | Vapor-L... |
| Pvap | 49.31 | kPa | 355.43 | Vapor-L... |
| Pvap | 49.95 | kPa | 355.74 | Vapor-L... |
| Pvap | 48.00 | kPa | 355.83 | Vapor p... |
| Pvap | 50.75 | kPa | 356.09 | Vapor-L... |
| Pvap | 51.36 | kPa | 356.45 | Vapor-L... |
| Pvap | 49.95 | kPa | 356.60 | Vapor L... |
| Pvap | 52.00 | kPa | 356.69 | Vapor-L... |
| Pvap | 52.61 | kPa | 356.99 | Vapor-L... |
| Pvap | 53.32 | kPa | 357.35 | Vapor-L... |
| Pvap | 54.03 | kPa | 357.67 | Vapor-L... |
| Pvap | 52.00 | kPa | 357.78 | Vapor p... |
| Pvap | 54.67 | kPa | 357.96 | Vapor-L... |
| Pvap | 55.35 | kPa | 358.25 | Vapor-L... |
| Pvap | 55.95 | kPa | 358.47 | Vapor-L... |
| Pvap | 56.63 | kPa | 358.85 | Vapor-L... |
| Pvap | 57.33 | kPa | 359.15 | Vapor-L... |
| Pvap | 58.00 | kPa | 359.48 | Vapor-L... |
| Pvap | 58.59 | kPa | 359.68 | Vapor-L... |
| Pvap | 56.66 | kPa | 359.90 | Vapor p... |
| Pvap | 59.27 | kPa | 360.01 | Vapor-L... |
| Pvap | 59.95 | kPa | 360.21 | Vapor-L... |
| Pvap | 60.59 | kPa | 360.53 | Vapor-L... |
| Pvap | 61.27 | kPa | 360.83 | Vapor-L... |
| Pvap | 61.99 | kPa | 361.11 | Vapor-L... |
| Pvap | 60.05 | kPa | 361.18 | Vapor L... |
| Pvap | 62.61 | kPa | 361.40 | Vapor-L... |
| Pvap | 63.35 | kPa | 361.72 | Vapor-L... |
| Pvap | 61.33 | kPa | 361.88 | Vapor p... |
| Pvap | 64.04 | kPa | 362.01 | Vapor-L... |
| Pvap | 64.67 | kPa | 362.24 | Vapor-L... |
| Pvap | 65.35 | kPa | 362.54 | Vapor-L... |
| Pvap | 66.00 | kPa | 362.84 | Vapor-L... |
| Pvap | 66.71 | kPa | 363.07 | Vapor-L... |
| Pvap | 67.92 | kPa | 363.56 | Vapor-L... |
| Pvap | 66.66 | kPa | 364.01 | Vapor p... |
| Pvap | 69.21 | kPa | 364.15 | Vapor-L... |
| Pvap | 70.64 | kPa | 364.62 | Vapor-L... |
| Pvap | 71.99 | kPa | 365.21 | Vapor-L... |
| Pvap | 70.74 | kPa | 365.40 | Vapor L... |
| Pvap | 73.37 | kPa | 365.73 | Vapor-L... |
| Pvap | 71.99 | kPa | 366.01 | Vapor p... |
| Pvap | 74.75 | kPa | 366.16 | Vapor-L... |
| Pvap | 76.05 | kPa | 366.67 | Vapor-L... |
| Pvap | 77.28 | kPa | 367.11 | Vapor-L... |
| Pvap | 78.63 | kPa | 367.53 | Vapor-L... |
| Pvap | 77.33 | kPa | 367.90 | Vapor p... |
| Pvap | 79.97 | kPa | 368.02 | Vapor-L... |
| Pvap | 78.27 | kPa | 368.07 | Vapor L... |
| Pvap | 78.09 | kPa | 368.16 | Vapor L... |
| Pvap | 81.28 | kPa | 368.44 | Vapor-L... |
| Pvap | 80.20 | kPa | 368.75 | Vapor L... |
| Pvap | 82.53 | kPa | 368.83 | Vapor-L... |
| Pvap | 83.93 | kPa | 369.31 | Vapor-L... |
| Pvap | 82.66 | kPa | 369.69 | Vapor p... |
| Pvap | 85.28 | kPa | 369.73 | Vapor-L... |
| Pvap | 86.63 | kPa | 370.15 | Vapor-L... |
| Pvap | 87.97 | kPa | 370.56 | Vapor-L... |
| Pvap | 89.39 | kPa | 370.99 | Vapor-L... |
| Pvap | 90.76 | kPa | 371.39 | Vapor-L... |
| Pvap | 91.99 | kPa | 371.77 | Vapor-L... |
| Pvap | 89.33 | kPa | 371.80 | Vapor p... |
| Pvap | 90.23 | kPa | 371.97 | Vapor L... |
| Pvap | 93.31 | kPa | 372.16 | Vapor-L... |
| Pvap | 94.67 | kPa | 372.56 | Vapor-L... |
| Pvap | 95.99 | kPa | 372.95 | Vapor-L... |
| Pvap | 97.39 | kPa | 373.34 | Vapor-L... |
| Pvap | 98.71 | kPa | 373.73 | Vapor-L... |
| Pvap | 95.99 | kPa | 373.79 | Vapor p... |
| Pvap | 98.66 | kPa | 374.56 | Vapor p... |
| Pvap | 100.74 | kPa | 375.14 | Vapor L... |
| Pvap | 101.88 | kPa | 375.38 | Vapor L... |
| Pvap | 102.61 | kPa | 375.53 | Vapor L... |
| n0 | [1.40160; 1.40250] | [293.15; 298.15] |
|
|
|
T(K) Refractive Index 1.4 1.4 1.4 1.4 1.4 294 296 298 | ||||
| n0 | 1.40160 | 293.15 | Volumet... | |
| n0 | 1.40250 | 298.15 | Molar h... | |
| n0 | 1.40220 | 298.15 | sotherm... | |
| n0 | 1.40219 | 298.15 | Ternary... | |
| n0 | 1.40180 | 298.15 | Vapor-L... | |
| n0 | 1.40190 | 298.15 | Excess ... | |
| n0 | 1.40248 | 298.15 | Vapor L... | |
| ρl | [795.16; 826.70] | kg/m3 | [273.65; 308.15] |
|
|
T(K) Liquid Density (kg/m3) 795 800 805 810 815 820 825 280 290 300 | ||||
| ρl | 826.70 | kg/m3 | 273.65 | Tempera... |
| ρl | 826.30 | kg/m3 | 274.15 | Tempera... |
| ρl | 825.80 | kg/m3 | 274.65 | Tempera... |
| ρl | 825.40 | kg/m3 | 275.15 | Tempera... |
| ρl | 824.90 | kg/m3 | 275.65 | Tempera... |
| ρl | 824.50 | kg/m3 | 276.15 | Tempera... |
| ρl | 824.00 | kg/m3 | 276.65 | Tempera... |
| ρl | 823.50 | kg/m3 | 277.15 | Tempera... |
| ρl | 823.10 | kg/m3 | 277.65 | Tempera... |
| ρl | 822.60 | kg/m3 | 278.15 | Tempera... |
| ρl | 822.20 | kg/m3 | 278.65 | Tempera... |
| ρl | 821.70 | kg/m3 | 279.15 | Tempera... |
| ρl | 821.30 | kg/m3 | 279.65 | Tempera... |
| ρl | 820.80 | kg/m3 | 280.15 | Tempera... |
| ρl | 820.30 | kg/m3 | 280.65 | Tempera... |
| ρl | 819.90 | kg/m3 | 281.15 | Tempera... |
| ρl | 819.40 | kg/m3 | 281.65 | Tempera... |
| ρl | 819.00 | kg/m3 | 282.15 | Tempera... |
| ρl | 809.00 | kg/m3 | 293.00 | KDB |
| ρl | 804.31 | kg/m3 | 298.15 | Excess ... |
| ρl | 804.21 | kg/m3 | 298.15 | Measure... |
| ρl | 804.28 | kg/m3 | 298.15 | Proposa... |
| ρl | 795.16 | kg/m3 | 308.15 | Excess ... |
| ΔfusS | [0.78; 16.88] | J/mol×K | [146.00; 264.00] |
|
| ΔfusS | 13.44 | J/mol×K | 146.00 | NIST |
| ΔfusS | 0.78 | J/mol×K | 213.00 | NIST |
| ΔfusS | 16.88 | J/mol×K | 264.00 | NIST |
| csound,fluid | 1177.79 | m/s | 298.15 | Study o... |
| γ | [0.02; 0.02] | N/m | [293.15; 323.15] |
|
|
T(K) Surface Tension (N/m) 0.02 0.02 0.02 0.02 0.02 0.02 300 310 320 | ||||
| γ | 0.02 | N/m | 293.15 | Surface... |
| γ | 0.02 | N/m | 298.15 | Surface... |
| γ | 0.02 | N/m | 303.15 | Surface... |
| γ | 0.02 | N/m | 308.15 | Surface... |
| γ | 0.02 | N/m | 313.15 | Surface... |
| γ | 0.02 | N/m | 318.15 | Surface... |
| γ | 0.02 | N/m | 323.15 | Surface... |
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 Vap...
|
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 300 400 500 | ||||
| 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 + Glycerin + Water
- Amylene hydrate + Heptane
- Amylene hydrate + Tetrahydrofuran
- Propylamine + Amylene hydrate
- Propylamine + Amylene hydrate + Tetrahydrofuran
- p-Coumaric acid + Amylene hydrate
- n-Butyl ether + Amylene hydrate
- Amylene hydrate + Water
- Amylene hydrate + Propane, 2-methoxy-2-methyl-
- Amylene hydrate + 1,3-Isobenzofurandione, 5-chloro-
- Amylene hydrate + 1-Propanol, 2-methyl-
- Furfural + Amylene hydrate + Water
- Ethanol + Amylene hydrate
- Amylene hydrate + N,N-Dimethylacetamide
- Amylene hydrate + Ethyl Acetate
- Amylene hydrate + N,N-Dimethylacetamide + Ethyl Acetate
- Amylene hydrate + Methyl Alcohol
- Isopropyl Alcohol + Amylene hydrate
- Isopropyl Alcohol + Amylene hydrate + Methyl Alcohol
- 1-Propanol + Amylene hydrate
Find more mixtures with Amylene hydrate.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- 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
- 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
- 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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