- InChI
- InChI=1S/C5H12O/c1-5(2,3)4-6/h6H,4H2,1-3H3
- InChI Key
- KPSSIOMAKSHJJG-UHFFFAOYSA-N
- Formula
- C5H12O
- SMILES
- CC(C)(C)CO
- Molecular Weight1
- 88.15
- CAS
- 75-84-3
- Other Names
-
- (CH3)3CCH2OH
- 2,2,2-Trimethylethanol
- 2,2-Dimethylpropanol
- 2,2-Dimethylpropyl alcohol
- 2,2-dimethyl-1-propanol
- 2-Methyl-isobutanol
- Neoamyl alcohol
- Neopentanol
- neopentyl alcohol
- tert-Amyl alcohol
- tert-Butylcarbinol
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- 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).
- 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).
- 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).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.5950; 0.6210] |
|
|
| ω | 0.6200 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.5950 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.6210 | KDB | |
| PAff | 795.50 | kJ/mol | NIST |
| BasG | 765.20 | kJ/mol | NIST |
| μ | 1.64 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | [-165.40; -140.00] | kJ/mol |
|
| ΔfG° | -140.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -165.40 | kJ/mol | KDB |
| ΔfH°gas | [-302.10; -293.10] | kJ/mol |
|
| ΔfH°gas | -302.10 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -293.10 | kJ/mol | KDB |
| ΔfusH° | 2.90 | kJ/mol | Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols |
| ΔvapH° | 51.80 ± 0.30 | kJ/mol | NIST |
| IE | 9.72 ± 0.05 | eV | NIST |
| log10WS | [-0.40; -0.40] |
|
|
| log10WS | -0.40 | Aq. Solubility Prediction | |
| log10WS | -0.40 | Estimated Solubility | |
| logPoct/wat | 1.025 | Crippen Calculated Property | |
| McVol | 87.180 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | [3951.68; 4078.00] | kPa |
|
| Pc | 3951.68 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 4078.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 3970.00 | kPa | KDB |
| Ptriple | 8.05 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [631.00; 657.00] |
|
|
| Inp | 633.00 | NIST | |
| Inp | 638.00 | NIST | |
| Inp | 631.00 | NIST | |
| Inp | Outlier 657.00 | NIST | |
| Inp | 633.00 | NIST | |
| Inp | 631.00 | NIST | |
| Tboil | [375.65; 387.15] | K |
|
| Tboil | 386.25 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 386.30 | K | KDB |
| Tboil | 386.70 | K | NIST |
| Tboil | 386.15 ± 2.00 | K | NIST |
| Tboil | 385.15 ± 2.00 | K | NIST |
| Tboil | 387.15 ± 2.00 | K | NIST |
| Tboil | 383.65 ± 2.00 | K | NIST |
| Tboil | 383.65 ± 2.00 | K | NIST |
| Tboil | 383.65 ± 2.00 | K | NIST |
| Tboil | 384.15 ± 2.00 | K | NIST |
| Tboil | 386.15 ± 2.00 | K | NIST |
| Tboil | 385.65 ± 1.00 | K | NIST |
| Tboil | 385.15 ± 2.00 | K | NIST |
| Tboil | 383.65 ± 2.00 | K | NIST |
| Tboil | 383.65 ± 1.50 | K | NIST |
| Tboil | 385.15 ± 3.00 | K | NIST |
| Tboil | 386.65 ± 2.00 | K | NIST |
| Tboil | Outlier 375.65 ± 2.00 | K | NIST |
| Tboil | 382.15 ± 4.00 | K | NIST |
| Tboil | 385.15 ± 2.00 | K | NIST |
| Tboil | 385.15 ± 1.50 | K | NIST |
| Tboil | 386.65 ± 0.70 | K | NIST |
| Tboil | 386.15 ± 1.00 | K | NIST |
| Tboil | 386.15 ± 2.00 | K | NIST |
| Tboil | 383.65 ± 2.00 | K | NIST |
| Tboil | 385.65 ± 1.00 | K | NIST |
| Tboil | 387.15 ± 3.00 | K | NIST |
| Tboil | 386.15 ± 1.00 | K | NIST |
| Tboil | 386.65 ± 2.00 | K | NIST |
| Tc | [549.00; 552.70] | K |
|
| Tc | 549.00 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 552.70 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 549.00 | K | KDB |
| Tfus | [323.15; 328.15] | K |
|
| Tfus | 325.65 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 328.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 327.00 | K | KDB |
| Tfus | 325.32 | K | Aq. Solubility Prediction |
| Tfus | 327.00 ± 0.20 | K | NIST |
| Tfus | 325.70 ± 3.00 | K | NIST |
| Tfus | 324.45 ± 0.40 | K | NIST |
| Tfus | 323.15 ± 1.50 | K | NIST |
| Ttriple | [237.50; 328.15] | K |
|
| Ttriple | 237.50 | K | Solid binary mixtures of neopentanol with tert-Butyl chloride and carbon tetrachloride studied by thermal, X-ray and dielectric techniques |
| Ttriple | 328.15 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 4.28 | ChemSep v8.3 pure component data Compiled value | |
| URi | 4.60 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.319; 0.327] | m3/kmol |
|
| Vc | 0.319 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.327 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.324 | m3/kmol | KDB |
| Zc | [0.2813560; 0.2900000] |
|
|
| Zc | 0.2900000 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.2813560 | KDB | |
| Zra | 0.29 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔfusH | [0.17; 4.46] | kJ/mol | [146.00; 329.80] |
|
| ΔfusH | 1.96 | kJ/mol | 146.00 | NIST |
| ΔfusH | 2.90 | kJ/mol | 190.00 | NIST |
| ΔfusH | 0.17 | kJ/mol | 213.00 | NIST |
| ΔfusH | 4.46 | kJ/mol | 264.00 | NIST |
| ΔfusH | 4.06 | kJ/mol | 325.00 | NIST |
| ΔfusH | 3.50 | kJ/mol | 328.10 | NIST |
| ΔfusH | 3.87 | kJ/mol | 329.80 | NIST |
| ΔfusH | 3.73 | kJ/mol | 329.80 | NIST |
| ΔvapH | 47.50 | kJ/mol | 358.50 | NIST |
| Pvap | [20.26; 98.94] | kPa | [345.90; 384.84] |
|
| Pvap | 20.26 | kPa | 345.90 | Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1 |
| Pvap | 24.53 | kPa | 350.00 | Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1 |
| Pvap | 29.35 | kPa | 353.97 | Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1 |
| Pvap | 34.76 | kPa | 357.84 | Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1 |
| Pvap | 40.70 | kPa | 361.57 | Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1 |
| Pvap | 47.56 | kPa | 365.36 | Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1 |
| Pvap | 60.19 | kPa | 371.31 | Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1 |
| Pvap | 74.65 | kPa | 377.00 | Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1 |
| Pvap | 93.23 | kPa | 383.15 | Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1 |
| Pvap | 98.94 | kPa | 384.84 | Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1 |
| ρl | 783.00 | kg/m3 | 327.00 | KDB |
| ΔfusS | [0.79; 16.88] | J/mol×K | [146.00; 264.00] |
|
| ΔfusS | 13.43 | J/mol×K | 146.00 | NIST |
| ΔfusS | 0.79 | J/mol×K | 213.00 | NIST |
| ΔfusS | 16.88 | J/mol×K | 264.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [73.88; 349.37] | J/mol×K | [100.00; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 7.22947e+01 | |||
| Coefficient B | -5.50037e+02 | |||
| Coefficient C | 5.96041e+00 | |||
| Coefficient D | 3.92020e-05 | |||
| Coefficient E | -1.25535e-08 | |||
| Temperature range, min. | 100.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 73.88 | J/mol×K | 100.00 | Calculated Property |
| Cp,gas | 117.78 | J/mol×K | 255.56 | Calculated Property |
| Cp,gas | 175.48 | J/mol×K | 411.11 | Calculated Property |
| Cp,gas | 221.89 | J/mol×K | 566.67 | Calculated Property |
| Cp,gas | 257.34 | J/mol×K | 722.22 | Calculated Property |
| Cp,gas | 284.71 | J/mol×K | 877.78 | Calculated Property |
| Cp,gas | 306.27 | J/mol×K | 1033.33 | Calculated Property |
| Cp,gas | 323.59 | J/mol×K | 1188.89 | Calculated Property |
| Cp,gas | 337.71 | J/mol×K | 1344.44 | Calculated Property |
| Cp,gas | 349.37 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [250.72; 315.78] | J/mol×K | [294.40; 386.25] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 1.24850e+02 | |||
| Coefficient B | 3.68960e+02 | |||
| Coefficient C | -1.99836e+00 | |||
| Coefficient D | 2.74720e-02 | |||
| Coefficient E | -2.89300e-05 | |||
| Temperature range, min. | 294.40 | |||
| Temperature range, max. | 386.25 | |||
| Cp,liquid | 250.72 | J/mol×K | 294.40 | Calculated Property |
| Cp,liquid | 258.71 | J/mol×K | 304.61 | Calculated Property |
| Cp,liquid | 266.73 | J/mol×K | 314.81 | Calculated Property |
| Cp,liquid | 274.70 | J/mol×K | 325.02 | Calculated Property |
| Cp,liquid | 282.52 | J/mol×K | 335.22 | Calculated Property |
| Cp,liquid | 290.09 | J/mol×K | 345.43 | Calculated Property |
| Cp,liquid | 297.31 | J/mol×K | 355.63 | Calculated Property |
| Cp,liquid | 304.06 | J/mol×K | 365.84 | Calculated Property |
| Cp,liquid | 310.25 | J/mol×K | 376.04 | Calculated Property |
| Cp,liquid | 315.78 | J/mol×K | 386.25 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0020150; 0.0003872] | Pa×s | [328.15; 386.25] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.26930e+01 | |||
| Coefficient B | 3.44680e+03 | |||
| Coefficient C | -7.14560e-01 | |||
| Coefficient D | 1.13220e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 328.15 | |||
| Temperature range, max. | 386.25 | |||
| η | 0.0020150 | Pa×s | 328.15 | Calculated Property |
| η | 0.0016305 | Pa×s | 334.61 | Calculated Property |
| η | 0.0013300 | Pa×s | 341.06 | Calculated Property |
| η | 0.0010932 | Pa×s | 347.52 | Calculated Property |
| η | 0.0009050 | Pa×s | 353.97 | Calculated Property |
| η | 0.0007543 | Pa×s | 360.43 | Calculated Property |
| η | 0.0006328 | Pa×s | 366.88 | Calculated Property |
| η | 0.0005342 | Pa×s | 373.34 | Calculated Property |
| η | 0.0004535 | Pa×s | 379.79 | Calculated Property |
| η | 0.0003872 | Pa×s | 386.25 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [53.26; 0.00] | kJ/mol | [274.20; 552.70] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 4.52240e+01 | |||
| Coefficient B | -1.24350e+00 | |||
| Coefficient C | 2.13800e+00 | |||
| Coefficient D | 1.39880e-01 | |||
| Coefficient E | -7.39890e-01 | |||
| Critical temperature, Tc (K) | 5.52700e+02 | |||
| Temperature range, min. | 274.20 | |||
| Temperature range, max. | 552.70 | |||
| ΔvapH | 53.26 | kJ/mol | 274.20 | Calculated Property |
| ΔvapH | 50.81 | kJ/mol | 305.14 | Calculated Property |
| ΔvapH | 47.75 | kJ/mol | 336.09 | Calculated Property |
| ΔvapH | 44.19 | kJ/mol | 367.03 | Calculated Property |
| ΔvapH | 40.21 | kJ/mol | 397.98 | Calculated Property |
| ΔvapH | 35.91 | kJ/mol | 428.92 | Calculated Property |
| ΔvapH | 31.31 | kJ/mol | 459.87 | Calculated Property |
| ΔvapH | 26.32 | kJ/mol | 490.81 | Calculated Property |
| ΔvapH | 20.35 | kJ/mol | 521.76 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 552.70 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [299.49; 405.81] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.49592e+01 | |||
| Coefficient B | -2.99573e+03 | |||
| Coefficient C | -9.53010e+01 | |||
| Temperature range, min. | 299.49 | |||
| Temperature range, max. | 405.81 | |||
| Pvap | 1.33 | kPa | 299.49 | Calculated Property |
| Pvap | 2.97 | kPa | 311.30 | Calculated Property |
| Pvap | 6.11 | kPa | 323.12 | Calculated Property |
| Pvap | 11.68 | kPa | 334.93 | Calculated Property |
| Pvap | 21.01 | kPa | 346.74 | Calculated Property |
| Pvap | 35.86 | kPa | 358.56 | Calculated Property |
| Pvap | 58.46 | kPa | 370.37 | Calculated Property |
| Pvap | 91.54 | kPa | 382.18 | Calculated Property |
| Pvap | 138.35 | kPa | 394.00 | Calculated Property |
| Pvap | 202.63 | kPa | 405.81 | Calculated Property |
| Pvap | [1.30; 4078.00] | kPa | [298.15; 522.23] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.85561e+02 | |||
| Coefficient B | -1.24136e+04 | |||
| Coefficient C | -2.55993e+01 | |||
| Coefficient D | 2.46643e-05 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | Range stopped where the equation exceeds Pc; ChemSep gives it to 552.7 K. | |||
| Temperature range, min. | 298.15 | |||
| Temperature range, max. | 522.23 | |||
| Pvap | 1.30 | kPa | 298.15 | Calculated Property |
| Pvap | 6.05 | kPa | 323.05 | Calculated Property |
| Pvap | 21.35 | kPa | 347.94 | Calculated Property |
| Pvap | 61.38 | kPa | 372.84 | Calculated Property |
| Pvap | 151.36 | kPa | 397.74 | Calculated Property |
| Pvap | 332.86 | kPa | 422.64 | Calculated Property |
| Pvap | 672.37 | kPa | 447.53 | Calculated Property |
| Pvap | 1276.13 | kPa | 472.43 | Calculated Property |
| Pvap | 2316.43 | kPa | 497.33 | Calculated Property |
| Pvap | 4078.00 | kPa | 522.23 | Calculated Property |
| Pvap | [1.26; 3792.12] | kPa | [298.15; 550.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.64736e+02 | |||
| Coefficient B | -1.20851e+04 | |||
| Coefficient C | -2.19703e+01 | |||
| Coefficient D | 1.35835e-05 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 298.15 | |||
| Temperature range, max. | 550.00 | |||
| Pvap | 1.26 | kPa | 298.15 | Calculated Property |
| Pvap | 7.21 | kPa | 326.13 | Calculated Property |
| Pvap | 28.61 | kPa | 354.12 | Calculated Property |
| Pvap | 86.67 | kPa | 382.10 | Calculated Property |
| Pvap | 214.57 | kPa | 410.08 | Calculated Property |
| Pvap | 456.34 | kPa | 438.07 | Calculated Property |
| Pvap | 865.15 | kPa | 466.05 | Calculated Property |
| Pvap | 1503.48 | kPa | 494.03 | Calculated Property |
| Pvap | 2446.90 | kPa | 522.02 | Calculated Property |
| Pvap | 3792.12 | kPa | 550.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [702.36; 269.74] | kg/m3 | [328.15; 552.70] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 7.82236e+01 | |||
| Coefficient B | 2.90000e-01 | |||
| Coefficient C | 5.52700e+02 | |||
| Coefficient D | 2.85710e-01 | |||
| Temperature range, min. | 328.15 | |||
| Temperature range, max. | 552.70 | |||
| ρl | 702.36 | kg/m3 | 328.15 | Calculated Property |
| ρl | 680.47 | kg/m3 | 353.10 | Calculated Property |
| ρl | 657.30 | kg/m3 | 378.05 | Calculated Property |
| ρl | 632.55 | kg/m3 | 403.00 | Calculated Property |
| ρl | 605.77 | kg/m3 | 427.95 | Calculated Property |
| ρl | 576.24 | kg/m3 | 452.90 | Calculated Property |
| ρl | 542.74 | kg/m3 | 477.85 | Calculated Property |
| ρl | 502.78 | kg/m3 | 502.80 | Calculated Property |
| ρl | 449.56 | kg/m3 | 527.75 | Calculated Property |
| ρl | 269.74 | kg/m3 | 552.70 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.01; 1.02e-05] | N/m | [327.15; 552.25] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K | |||
| Coefficient A | -4.15790e-03 | |||
| Coefficient B | 9.05490e+02 | |||
| Coefficient C | -1.11290e+01 | |||
| Coefficient D | 2.24900e-02 | |||
| Coefficient E | -2.75790e-05 | |||
| Comment | Range stopped where the equation turns negative; ChemSep gives it to 552.7 K. | |||
| Temperature range, min. | 327.15 | |||
| Temperature range, max. | 552.25 | |||
| γ | 0.01 | N/m | 327.15 | Calculated Property |
| γ | 0.01 | N/m | 352.16 | Calculated Property |
| γ | 0.01 | N/m | 377.17 | Calculated Property |
| γ | 0.01 | N/m | 402.18 | Calculated Property |
| γ | 0.01 | N/m | 427.19 | Calculated Property |
| γ | 0.01 | N/m | 452.20 | Calculated Property |
| γ | 0.00 | N/m | 477.22 | Calculated Property |
| γ | 0.00 | N/m | 502.23 | Calculated Property |
| γ | 0.00 | N/m | 527.24 | Calculated Property |
| γ | 1.02e-05 | N/m | 552.25 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.01; 0.12] | W/m×K | [274.00; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | 1.28420e-07 | |||
| Coefficient B | 1.97730e+00 | |||
| Coefficient C | -6.19330e+01 | |||
| Coefficient D | 2.94600e+03 | |||
| Temperature range, min. | 274.00 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.01 | W/m×K | 274.00 | Calculated Property |
| λgas | 0.02 | W/m×K | 354.67 | Calculated Property |
| λgas | 0.02 | W/m×K | 435.33 | Calculated Property |
| λgas | 0.03 | W/m×K | 516.00 | Calculated Property |
| λgas | 0.04 | W/m×K | 596.67 | Calculated Property |
| λgas | 0.06 | W/m×K | 677.33 | Calculated Property |
| λgas | 0.07 | W/m×K | 758.00 | Calculated Property |
| λgas | 0.08 | W/m×K | 838.67 | Calculated Property |
| λgas | 0.10 | W/m×K | 919.33 | Calculated Property |
| λgas | 0.12 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.17; 0.09] | W/m×K | [165.00; 435.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K | |||
| Coefficient A | -1.16020e-01 | |||
| Coefficient B | 1.04160e+01 | |||
| Coefficient C | -1.22700e+00 | |||
| Coefficient D | -3.33550e-04 | |||
| Coefficient E | -1.13000e-06 | |||
| Temperature range, min. | 165.00 | |||
| Temperature range, max. | 435.00 | |||
| λliquid | 0.17 | W/m×K | 165.00 | Calculated Property |
| λliquid | 0.16 | W/m×K | 195.00 | Calculated Property |
| λliquid | 0.15 | W/m×K | 225.00 | Calculated Property |
| λliquid | 0.14 | W/m×K | 255.00 | Calculated Property |
| λliquid | 0.14 | W/m×K | 285.00 | Calculated Property |
| λliquid | 0.13 | W/m×K | 315.00 | Calculated Property |
| λliquid | 0.12 | W/m×K | 345.00 | Calculated Property |
| λliquid | 0.11 | W/m×K | 375.00 | Calculated Property |
| λliquid | 0.10 | W/m×K | 405.00 | Calculated Property |
| λliquid | 0.09 | W/m×K | 435.00 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Propanol, 2,2-dimethyl-.
Mixtures
- 1-Propanol, 2,2-dimethyl- + Propane, 2-chloro-2-methyl-
- 1-Propanol, 2,2-dimethyl- + Carbon Tetrachloride
- 1-Propanol, 2,2-dimethyl- + 2-Butanone, 3,3-dimethyl-
- 1-Propanol, 2,2-dimethyl- + Propane, 2-methoxy-2-methyl-
- 1-Propanol, 2,2-dimethyl- + Propane, 2-methoxy-2-methyl- + 2-Butanone, 3,3-dimethyl-
- 1-Propanol, 2,2-dimethyl- + Water
- Carbon dioxide + 1-Propanol, 2,2-dimethyl-
Sources
- KDB Vapor Pressure Data
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- Crippen Method
- 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
- Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
- Solid binary mixtures of neopentanol with tert-Butyl chloride and carbon tetrachloride studied by thermal, X-ray and dielectric techniques
- 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
- Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
- Partial Molar Volumes of Selected Aliphatic Alcohols at Infinite Dilution in Water at Temperatures T = (278 to 573) K and Pressures up to 30 MPa
- Partial Molar Isentropic Compressions and Partial Molar Volumes of Selected Branched Aliphatic Alcohols at Infinite Dilution in Water at Temperatures from T = (278 to 318) K and Atmospheric Pressure
- Vapor Liquid Equilibria of CO2 + C1 C5 Alcohols from the Experiment and the COSMO-SAC Model
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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