- InChI
- InChI=1S/C6H14/c1-5-6(2,3)4/h5H2,1-4H3
- InChI Key
- HNRMPXKDFBEGFZ-UHFFFAOYSA-N
- Formula
- C6H14
- SMILES
- CCC(C)(C)C
- Molecular Weight1
- 86.18
- CAS
- 75-83-2
- Other Names
-
- (CH3)3CCH2CH3
- 2,2-Dimethylbutane
- NEOHEXANE
- UN 1208
- ω : Acentric Factor.
- AP : Aniline Point (K).
- 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).
- Δc,grossH : Heat of Combustion, Gross form (kJ/mol).
- Δc,netH : Heat of Combustion, Net Form (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.
- ρc : Critical density (kg/m3).
- 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).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λ : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- 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 | 0.2320 | KDB | |
| AP | 354.350 | K | KDB |
| ΔcH°liquid | -4148.50 ± 0.88 | kJ/mol | NIST |
| ΔfG° | -9.63 | kJ/mol | KDB |
| Δc,grossH | 4148.52 | kJ/mol | KDB |
| Δc,netH | 3840.410 | kJ/mol | KDB |
| ΔfH°gas | [-185.70; -185.60] | kJ/mol |
|
| ΔfH°gas | -185.70 | kJ/mol | KDB |
| ΔfH°gas | -185.60 ± 0.96 | kJ/mol | NIST |
| ΔfH°liquid | -213.40 ± 0.96 | kJ/mol | NIST |
| ΔfusH° | 3.88 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [27.68; 27.93] | kJ/mol |
|
| ΔvapH° | 27.93 | kJ/mol | NIST |
| ΔvapH° | 27.70 | kJ/mol | NIST |
| ΔvapH° | 27.68 | kJ/mol | NIST |
| IE | [9.79; 10.07] | eV |
|
| IE | 10.07 | eV | NIST |
| IE | 9.79 | eV | NIST |
| IE | 10.06 | eV | NIST |
| log10WS | [-3.55; -3.55] |
|
|
| log10WS | -3.55 | Aq. Sol... | |
| log10WS | -3.55 | Estimat... | |
| logPoct/wat | 2.442 | Crippen Calculated Property | |
| McVol | 95.400 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | [3100.00; 3107.64] | kPa |
|
| Pc | 3100.00 | kPa | KDB |
| Pc | 3100.00 ± 20.00 | kPa | NIST |
| Pc | 3102.36 ± 5.00 | kPa | NIST |
| Pc | 3102.00 ± 3.00 | kPa | NIST |
| Pc | 3107.64 ± 10.13 | kPa | NIST |
| ρc | [240.43; 241.29] | kg/m3 |
|
| ρc | 241.29 ± 1.72 | kg/m3 | NIST |
| ρc | 240.43 ± 1.72 | kg/m3 | NIST |
| Inp | [525.00; 547.90] |
|
|
| Inp | 535.60 | NIST | |
| Inp | 537.40 | NIST | |
| Inp | 540.80 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | 533.00 | NIST | |
| Inp | 534.00 | NIST | |
| Inp | 539.00 | NIST | |
| Inp | 535.30 | NIST | |
| Inp | 543.80 | NIST | |
| Inp | Outlier 547.90 | NIST | |
| Inp | 535.00 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | 538.20 | NIST | |
| Inp | 537.90 | NIST | |
| Inp | 537.90 | NIST | |
| Inp | 540.90 | NIST | |
| Inp | 534.00 | NIST | |
| Inp | 541.00 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | 535.00 | NIST | |
| Inp | 536.00 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | 535.50 | NIST | |
| Inp | 538.90 | NIST | |
| Inp | 537.10 | NIST | |
| Inp | 535.50 | NIST | |
| Inp | 536.70 | NIST | |
| Inp | 537.10 | NIST | |
| Inp | 537.70 | NIST | |
| Inp | 534.00 | NIST | |
| Inp | 535.00 | NIST | |
| Inp | 535.00 | NIST | |
| Inp | 536.00 | NIST | |
| Inp | 537.00 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | 533.90 | NIST | |
| Inp | 534.60 | NIST | |
| Inp | 535.40 | NIST | |
| Inp | 536.20 | NIST | |
| Inp | 537.00 | NIST | |
| Inp | 537.90 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | 537.90 | NIST | |
| Inp | 536.00 | NIST | |
| Inp | 537.00 | NIST | |
| Inp | 536.00 | NIST | |
| Inp | 540.00 | NIST | |
| Inp | 536.00 | NIST | |
| Inp | 533.00 | NIST | |
| Inp | 534.50 | NIST | |
| Inp | 536.00 | NIST | |
| Inp | 537.70 | NIST | |
| Inp | 539.40 | NIST | |
| Inp | 541.30 | NIST | |
| Inp | 542.20 | NIST | |
| Inp | 541.40 | NIST | |
| Inp | 539.60 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | 536.10 | NIST | |
| Inp | 534.60 | NIST | |
| Inp | 530.00 | NIST | |
| Inp | 536.80 | NIST | |
| Inp | 537.00 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | 540.00 | NIST | |
| Inp | 539.00 | NIST | |
| Inp | 538.60 | NIST | |
| Inp | 541.70 | NIST | |
| Inp | 536.90 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | 535.10 | NIST | |
| Inp | 537.00 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | Outlier 544.75 | NIST | |
| Inp | Outlier 545.80 | NIST | |
| Inp | Outlier 547.42 | NIST | |
| Inp | 542.16 | NIST | |
| Inp | 543.36 | NIST | |
| Inp | 537.00 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | 534.99 | NIST | |
| Inp | 530.00 | NIST | |
| Inp | 532.00 | NIST | |
| Inp | 533.00 | NIST | |
| Inp | 534.00 | NIST | |
| Inp | 536.00 | NIST | |
| Inp | 537.00 | NIST | |
| Inp | 540.00 | NIST | |
| Inp | 541.00 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | 530.00 | NIST | |
| Inp | 535.00 | NIST | |
| Inp | 539.00 | NIST | |
| Inp | 541.00 | NIST | |
| Inp | 535.00 | NIST | |
| Inp | 537.00 | NIST | |
| Inp | 539.00 | NIST | |
| Inp | 540.00 | NIST | |
| Inp | 535.00 | NIST | |
| Inp | 537.00 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | 541.00 | NIST | |
| Inp | 534.00 | NIST | |
| Inp | 535.00 | NIST | |
| Inp | 536.00 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | 537.00 | NIST | |
| Inp | 539.00 | NIST | |
| Inp | 539.00 | NIST | |
| Inp | 530.00 | NIST | |
| Inp | 529.00 | NIST | |
| Inp | 540.25 | NIST | |
| Inp | 537.00 | NIST | |
| Inp | Outlier 526.00 | NIST | |
| Inp | Outlier 526.30 | NIST | |
| Inp | 528.50 | NIST | |
| Inp | Outlier 526.78 | NIST | |
| Inp | Outlier 526.81 | NIST | |
| Inp | 531.00 | NIST | |
| Inp | 528.00 | NIST | |
| Inp | 528.00 | NIST | |
| Inp | 528.00 | NIST | |
| Inp | 536.00 | NIST | |
| Inp | 537.00 | NIST | |
| Inp | 536.00 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | 541.00 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | 528.00 | NIST | |
| Inp | 535.00 | NIST | |
| Inp | 536.00 | NIST | |
| Inp | 533.00 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | 537.00 | NIST | |
| Inp | Outlier 526.00 | NIST | |
| Inp | 532.00 | NIST | |
| Inp | 536.00 | NIST | |
| Inp | 528.00 | NIST | |
| Inp | 529.00 | NIST | |
| Inp | 540.00 | NIST | |
| Inp | 537.00 | NIST | |
| Inp | 535.00 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | 540.00 | NIST | |
| Inp | 528.00 | NIST | |
| Inp | 537.00 | NIST | |
| Inp | Outlier 525.00 | NIST | |
| Inp | Outlier 525.00 | NIST | |
| Inp | 533.00 | NIST | |
| Inp | 530.00 | NIST | |
| Inp | 536.00 | NIST | |
| Inp | 542.00 | NIST | |
| Inp | 537.00 | NIST | |
| Inp | 542.00 | NIST | |
| Inp | 537.00 | NIST | |
| Inp | 528.00 | NIST | |
| Inp | 540.25 | NIST | |
| Inp | 535.60 | NIST | |
| Inp | 534.00 | NIST | |
| Inp | 535.00 | NIST | |
| Inp | 537.90 | NIST | |
| Inp | 538.00 | NIST | |
| Inp | 538.90 | NIST | |
| Inp | 537.70 | NIST | |
| Inp | 537.00 | NIST | |
| Inp | 536.20 | NIST | |
| Inp | 536.00 | NIST | |
| Inp | 533.00 | NIST | |
| Inp | 541.30 | NIST | |
| Inp | 536.10 | NIST | |
| Inp | 541.70 | NIST | |
| Inp | 543.36 | NIST | |
| Inp | 532.00 | NIST | |
| Inp | 540.00 | NIST | |
| Inp | 530.00 | NIST | |
| I | 500.00 | NIST | |
| S°gas | 358.65 ± 0.84 | J/mol×K | NIST |
| S°liquid | [269.40; 272.50] | J/mol×K |
|
| S°liquid | 272.00 | J/mol×K | NIST |
| S°liquid | 272.50 | J/mol×K | NIST |
| S°liquid | 269.40 | J/mol×K | NIST |
| Tboil | [320.65; 353.25] | K |
|
| Tboil | 322.88 | K | KDB |
| Tboil | 322.90 | K | NIST |
| Tboil | 322.90 | K | NIST |
| Tboil | 322.90 ± 0.05 | K | NIST |
| Tboil | 322.89 ± 0.15 | K | NIST |
| Tboil | 323.70 ± 1.00 | K | NIST |
| Tboil | 322.85 ± 0.30 | K | NIST |
| Tboil | 322.90 ± 1.00 | K | NIST |
| Tboil | 322.85 ± 0.10 | K | NIST |
| Tboil | 322.98 ± 0.10 | K | NIST |
| Tboil | 322.90 ± 0.30 | K | NIST |
| Tboil | 322.85 ± 0.30 | K | NIST |
| Tboil | 322.80 ± 0.30 | K | NIST |
| Tboil | 322.80 ± 0.50 | K | NIST |
| Tboil | 322.85 ± 0.30 | K | NIST |
| Tboil | 322.80 ± 0.15 | K | NIST |
| Tboil | 322.88 ± 0.05 | K | NIST |
| Tboil | 322.89 ± 0.01 | K | NIST |
| Tboil | 320.65 ± 8.00 | K | NIST |
| Tboil | 322.85 ± 0.20 | K | NIST |
| Tboil | 322.80 ± 0.30 | K | NIST |
| Tboil | 323.00 ± 0.10 | K | NIST |
| Tboil | 322.85 ± 0.60 | K | NIST |
| Tboil | 322.85 ± 0.70 | K | NIST |
| Tboil | 323.00 ± 0.10 | K | NIST |
| Tboil | 322.86 ± 0.10 | K | NIST |
| Tboil | Outlier 353.25 ± 0.30 | K | NIST |
| Tboil | 322.85 ± 0.40 | K | NIST |
| Tboil | 322.95 ± 0.20 | K | NIST |
| Tboil | 322.85 ± 0.50 | K | NIST |
| Tboil | 322.75 ± 0.30 | K | NIST |
| Tboil | 322.85 ± 0.50 | K | NIST |
| Tboil | 322.75 ± 0.30 | K | NIST |
| Tboil | 322.85 ± 0.60 | K | NIST |
| Tboil | 322.88 ± 0.05 | K | NIST |
| Tboil | 322.95 ± 0.20 | K | NIST |
| Tboil | 322.87 ± 0.10 | K | NIST |
| Tboil | 322.85 ± 0.50 | K | NIST |
| Tboil | 322.85 ± 0.20 | K | NIST |
| Tboil | 322.95 ± 0.20 | K | NIST |
| Tboil | 322.75 ± 0.50 | K | NIST |
| Tboil | 322.85 ± 0.20 | K | NIST |
| Tboil | 322.85 ± 0.50 | K | NIST |
| Tboil | 322.90 ± 0.20 | K | NIST |
| Tboil | 322.96 ± 0.10 | K | NIST |
| Tboil | 325.65 ± 2.00 | K | NIST |
| Tboil | 325.65 ± 0.50 | K | NIST |
| Tboil | 322.90 ± 0.50 | K | NIST |
| Tboil | 322.00 ± 1.00 | K | NIST |
| Tboil | 322.15 ± 1.50 | K | NIST |
| Tboil | 322.85 ± 0.50 | K | NIST |
| Tboil | 322.85 ± 1.00 | K | NIST |
| Tboil | 322.88 ± 0.10 | K | NIST |
| Tboil | 322.40 ± 0.20 | K | NIST |
| Tboil | 322.80 ± 1.00 | K | NIST |
| Tc | [488.70; 489.40] | K |
|
| Tc | 489.00 | K | KDB |
| Tc | 489.40 | K | The Cri... |
| Tc | 489.00 ± 0.30 | K | NIST |
| Tc | 488.70 | K | NIST |
| Tc | 489.25 ± 0.10 | K | NIST |
| Tc | 489.24 ± 0.20 | K | NIST |
| Tc | 488.70 ± 0.30 | K | NIST |
| Tc | 488.73 ± 0.20 | K | NIST |
| Tc | 489.35 ± 0.50 | K | NIST |
| Tfus | [163.14; 260.51] | K |
|
| Tfus | 174.00 | K | KDB |
| Tfus | 173.40 | K | Aq. Sol... |
| Tfus | 172.85 ± 0.70 | K | NIST |
| Tfus | 173.65 ± 0.15 | K | NIST |
| Tfus | 163.85 ± 6.00 | K | NIST |
| Tfus | 163.14 ± 0.08 | K | NIST |
| Tfus | 173.26 ± 0.06 | K | NIST |
| Tfus | 173.28 ± 0.04 | K | NIST |
| Tfus | 172.90 ± 0.60 | K | NIST |
| Tfus | 173.18 ± 0.07 | K | NIST |
| Tfus | 173.24 ± 0.04 | K | NIST |
| Tfus | 174.29 ± 0.10 | K | NIST |
| Tfus | 173.09 ± 0.05 | K | NIST |
| Tfus | Outlier 236.66 ± 0.15 | K | NIST |
| Tfus | Outlier 260.51 | K | NIST |
| Tfus | 173.15 ± 0.01 | K | NIST |
| Tfus | 173.18 ± 0.15 | K | NIST |
| Tfus | 173.42 ± 0.06 | K | NIST |
| Tfus | 173.39 ± 0.25 | K | NIST |
| Tfus | 170.74 ± 0.10 | K | NIST |
| Tfus | 173.18 ± 0.15 | K | NIST |
| Tfus | 173.42 ± 0.06 | K | NIST |
| Tfus | 173.09 ± 0.05 | K | NIST |
| Tfus | 171.15 ± 2.00 | K | NIST |
| Tfus | 174.95 ± 1.00 | K | NIST |
| Tfus | 172.65 ± 0.40 | K | NIST |
| Tfus | 172.65 ± 0.20 | K | NIST |
| Tfus | 172.13 ± 0.15 | K | NIST |
| Tfus | 174.95 ± 0.50 | K | NIST |
| Tfus | 175.00 ± 0.30 | K | NIST |
| Ttriple | [172.10; 174.50] | K |
|
| Ttriple | 173.27 ± 0.40 | K | NIST |
| Ttriple | 173.27 ± 0.40 | K | NIST |
| Ttriple | 174.28 ± 0.06 | K | NIST |
| Ttriple | 174.16 ± 0.07 | K | NIST |
| Ttriple | 174.50 ± 0.25 | K | NIST |
| Ttriple | 172.10 ± 0.20 | K | NIST |
| Vc | [0.358; 0.358] | m3/kmol |
|
| Vc | 0.358 | m3/kmol | KDB |
| Vc | 0.358 | m3/kmol | NIST |
| Vc | 0.358 ± 0.001 | m3/kmol | NIST |
| Zc | 0.2729600 | KDB | |
| Zra | 0.27 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [159.41; 202.21] | J/mol×K | [341.55; 449.40] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 160 170 180 190 200 350 400 450 | ||||
| Cp,gas | 159.41 ± 0.32 | J/mol×K | 341.55 | NIST |
| Cp,gas | 164.22 ± 0.33 | J/mol×K | 353.20 | NIST |
| Cp,gas | 173.64 ± 0.35 | J/mol×K | 376.05 | NIST |
| Cp,gas | 188.07 ± 0.38 | J/mol×K | 412.40 | NIST |
| Cp,gas | 202.21 ± 0.40 | J/mol×K | 449.40 | NIST |
| Cp,liquid | [183.18; 191.88] | J/mol×K | [290.00; 300.00] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 184 186 188 190 192 290 295 300 | ||||
| Cp,liquid | 186.90 | J/mol×K | 290.00 | NIST |
| Cp,liquid | 183.18 | J/mol×K | 298.10 | NIST |
| Cp,liquid | 189.67 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 191.88 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 189.14 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 189.14 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 188.74 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 191.88 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 189.44 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 191.50 | J/mol×K | 300.00 | NIST |
| η | [0.0002839; 0.0107782] | Pa×s | [159.80; 333.45] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 2.00e-3 4.00e-3 6.00e-3 8.00e-3 0.01 200 250 300 | ||||
| η | 0.0107782 | Pa×s | 159.80 | Joback Calculated Property |
| η | 0.0036939 | Pa×s | 188.74 | Joback Calculated Property |
| η | 0.0016831 | Pa×s | 217.68 | Joback Calculated Property |
| η | 0.0009222 | Pa×s | 246.62 | Joback Calculated Property |
| η | 0.0005734 | Pa×s | 275.57 | Joback Calculated Property |
| η | 0.0003902 | Pa×s | 304.51 | Joback Calculated Property |
| η | 0.0002839 | Pa×s | 333.45 | Joback Calculated Property |
| ΔfusH | [0.28; 5.40] | kJ/mol | [126.80; 174.30] |
|
| ΔfusH | 5.40 | kJ/mol | 126.80 | NIST |
| ΔfusH | 0.28 | kJ/mol | 140.80 | NIST |
| ΔfusH | 0.58 | kJ/mol | 174.30 | NIST |
| ΔfusH | 0.58 | kJ/mol | 174.30 | NIST |
| ΔvapH | [26.30; 29.20] | kJ/mol | [250.00; 323.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 26.5 27 27.5 28 28.5 29 260 280 300 320 | ||||
| ΔvapH | 29.20 | kJ/mol | 250.00 | NIST |
| ΔvapH | 28.70 | kJ/mol | 295.50 | NIST |
| ΔvapH | 27.80 ± 0.10 | kJ/mol | 296.00 | NIST |
| ΔvapH | 28.30 | kJ/mol | 305.50 | NIST |
| ΔvapH | 26.31 | kJ/mol | 322.90 | NIST |
| ΔvapH | 26.30 | kJ/mol | 322.90 | KDB |
| ΔvapH | 26.30 ± 0.10 | kJ/mol | 323.00 | NIST |
| ν | [0.0000005; 0.0000006] | m2/s | [283.15; 313.15] |
|
| ν | 0.0000006 | m2/s | 283.15 | Experim... |
| ν | 0.0000005 | m2/s | 298.15 | Experim... |
| ν | 0.0000005 | m2/s | 313.15 | Experim... |
| n0 | [1.36595; 1.36608] | [298.15; 298.15] |
|
|
| n0 | 1.36595 | 298.15 | KDB | |
| n0 | 1.36608 | 298.15 | Liquid ... | |
| ρl | [644.59; 649.00] | kg/m3 | [293.00; 298.15] |
|
| ρl | 649.00 | kg/m3 | 293.00 | KDB |
| ρl | 644.92 | kg/m3 | 298.15 | Excess ... |
| ρl | 644.59 | kg/m3 | 298.15 | Excess ... |
| ΔfusS | [2.02; 42.57] | J/mol×K | [126.80; 174.30] |
|
| ΔfusS | 42.57 | J/mol×K | 126.80 | NIST |
| ΔfusS | 2.02 | J/mol×K | 140.80 | NIST |
| ΔfusS | 3.31 | J/mol×K | 174.30 | NIST |
| γ | [0.01; 0.02] | N/m | [233.09; 378.23] |
|
|
T(K) Surface Tension (N/m) 8.00e-3 0.01 0.01 0.01 0.02 0.02 0.02 0.02 250 300 350 | ||||
| γ | 0.02 | N/m | 233.09 | Surface... |
| γ | 0.02 | N/m | 238.10 | Surface... |
| γ | 0.02 | N/m | 243.13 | Surface... |
| γ | 0.02 | N/m | 248.11 | Surface... |
| γ | 0.02 | N/m | 253.12 | Surface... |
| γ | 0.02 | N/m | 258.12 | Surface... |
| γ | 0.02 | N/m | 263.13 | Surface... |
| γ | 0.02 | N/m | 268.10 | Surface... |
| γ | 0.02 | N/m | 273.10 | Surface... |
| γ | 0.02 | N/m | 278.08 | Surface... |
| γ | 0.02 | N/m | 283.09 | Surface... |
| γ | 0.02 | N/m | 288.17 | Surface... |
| γ | 0.02 | N/m | 293.12 | Surface... |
| γ | 0.02 | N/m | 298.10 | Surface... |
| γ | 0.02 | N/m | 298.20 | KDB |
| γ | 0.02 | N/m | 303.17 | Surface... |
| γ | 0.01 | N/m | 308.13 | Surface... |
| γ | 0.01 | N/m | 313.12 | Surface... |
| γ | 0.01 | N/m | 318.13 | Surface... |
| γ | 0.01 | N/m | 323.13 | Surface... |
| γ | 0.01 | N/m | 328.12 | Surface... |
| γ | 0.01 | N/m | 333.13 | Surface... |
| γ | 0.01 | N/m | 338.13 | 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 | 358.12 | Surface... |
| γ | 0.01 | N/m | 363.13 | Surface... |
| γ | 0.01 | N/m | 368.12 | Surface... |
| γ | 0.01 | N/m | 373.13 | Surface... |
| γ | 0.01 | N/m | 378.23 | Surface... |
| λ | [0.09; 0.11] | W/m×K | [257.48; 320.28] |
|
|
T(K) Liquid thermal conductivity (W/m×K) 0.09 0.1 0.1 0.11 260 280 300 320 | ||||
| λ | 0.11 | W/m×K | 257.48 | Thermal... |
| λ | 0.11 | W/m×K | 257.84 | Thermal... |
| λ | 0.11 | W/m×K | 258.30 | Thermal... |
| λ | 0.10 | W/m×K | 271.49 | Thermal... |
| λ | 0.10 | W/m×K | 271.84 | Thermal... |
| λ | 0.10 | W/m×K | 272.32 | Thermal... |
| λ | 0.10 | W/m×K | 279.86 | Thermal... |
| λ | 0.10 | W/m×K | 280.24 | Thermal... |
| λ | 0.10 | W/m×K | 280.73 | Thermal... |
| λ | 0.09 | W/m×K | 297.98 | Thermal... |
| λ | 0.09 | W/m×K | 298.42 | Thermal... |
| λ | 0.09 | W/m×K | 298.91 | Thermal... |
| λ | 0.09 | W/m×K | 319.35 | Thermal... |
| λ | 0.09 | W/m×K | 319.75 | Thermal... |
| λ | 0.09 | W/m×K | 320.28 | Thermal... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 100.00 | 283.15 | 658.57 |
| 100.00 | 288.15 | 653.96 |
| 100.00 | 293.15 | 649.25 |
| 100.00 | 298.15 | 644.46 |
| 100.00 | 303.15 | 639.75 |
| 100.00 | 308.15 | 634.86 |
| 100.00 | 313.15 | 630.04 |
| 100.00 | 318.15 | 625.06 |
| 100.00 | 323.15 | 620.03 |
| 2000.00 | 283.15 | 660.76 |
| 2000.00 | 288.15 | 656.25 |
| 2000.00 | 293.15 | 651.6 |
| 2000.00 | 298.15 | 646.95 |
| 2000.00 | 303.15 | 642.26 |
| 2000.00 | 308.15 | 637.48 |
| 2000.00 | 313.15 | 632.76 |
| 2000.00 | 318.15 | 627.98 |
| 2000.00 | 323.15 | 623.17 |
| 2000.00 | 328.15 | 618.2 |
| 5000.00 | 283.15 | 664.07 |
| 5000.00 | 288.15 | 659.62 |
| 5000.00 | 293.15 | 655.12 |
| 5000.00 | 298.15 | 650.7 |
| 5000.00 | 303.15 | 646.07 |
| 5000.00 | 308.15 | 641.54 |
| 5000.00 | 313.15 | 637.06 |
| 5000.00 | 318.15 | 632.33 |
| 5000.00 | 323.15 | 627.74 |
| 5000.00 | 328.15 | 623.02 |
| 7000.00 | 283.15 | 666.19 |
| 7000.00 | 288.15 | 661.74 |
| 7000.00 | 293.15 | 657.45 |
| 7000.00 | 298.15 | 653.04 |
| 7000.00 | 303.15 | 648.58 |
| 7000.00 | 308.15 | 644.04 |
| 7000.00 | 313.15 | 639.66 |
| 7000.00 | 318.15 | 635.14 |
| 7000.00 | 323.15 | 630.61 |
| 7000.00 | 328.15 | 626.02 |
| 10000.00 | 283.15 | 669.19 |
| 10000.00 | 288.15 | 664.88 |
| 10000.00 | 293.15 | 660.66 |
| 10000.00 | 298.15 | 656.38 |
| 10000.00 | 303.15 | 652.04 |
| 10000.00 | 308.15 | 647.69 |
| 10000.00 | 313.15 | 643.44 |
| 10000.00 | 318.15 | 639.02 |
| 10000.00 | 323.15 | 634.54 |
| 10000.00 | 328.15 | 630.26 |
| 20000.00 | 283.15 | 678.5 |
| 20000.00 | 288.15 | 674.51 |
| 20000.00 | 293.15 | 670.51 |
| 20000.00 | 298.15 | 666.62 |
| 20000.00 | 303.15 | 662.53 |
| 20000.00 | 308.15 | 658.58 |
| 20000.00 | 313.15 | 654.67 |
| 20000.00 | 318.15 | 650.69 |
| 20000.00 | 323.15 | 646.65 |
| 20000.00 | 328.15 | 642.58 |
| 30000.00 | 283.15 | 686.83 |
| 30000.00 | 288.15 | 683.05 |
| 30000.00 | 293.15 | 679.25 |
| 30000.00 | 298.15 | 675.66 |
| 30000.00 | 303.15 | 671.8 |
| 30000.00 | 308.15 | 668.08 |
| 30000.00 | 313.15 | 664.53 |
| 30000.00 | 318.15 | 660.78 |
| 30000.00 | 323.15 | 656.94 |
| 30000.00 | 328.15 | 653.14 |
| 40000.00 | 283.15 | 694.31 |
| 40000.00 | 288.15 | 690.77 |
| 40000.00 | 293.15 | 687.12 |
| 40000.00 | 298.15 | 683.71 |
| 40000.00 | 303.15 | 680.03 |
| 40000.00 | 308.15 | 676.55 |
| 40000.00 | 313.15 | 673.1 |
| 40000.00 | 318.15 | 669.72 |
| 40000.00 | 323.15 | 666.02 |
| 40000.00 | 328.15 | 662.51 |
| 50000.00 | 283.15 | 701.27 |
| 50000.00 | 288.15 | 697.81 |
| 50000.00 | 293.15 | 694.34 |
| 50000.00 | 298.15 | 691.09 |
| 50000.00 | 303.15 | 687.56 |
| 50000.00 | 308.15 | 684.38 |
| 50000.00 | 313.15 | 680.94 |
| 50000.00 | 318.15 | 677.73 |
| 50000.00 | 323.15 | 674.2 |
| 50000.00 | 328.15 | 670.88 |
| 60000.00 | 283.15 | 707.71 |
| 60000.00 | 288.15 | 704.32 |
| 60000.00 | 293.15 | 701.07 |
| 60000.00 | 298.15 | 697.88 |
| 60000.00 | 303.15 | 694.57 |
| 60000.00 | 308.15 | 691.41 |
| 60000.00 | 313.15 | 688.22 |
| 60000.00 | 318.15 | 685.05 |
| 60000.00 | 323.15 | 681.7 |
| 60000.00 | 328.15 | 678.64 |
| 65000.00 | 283.15 | 710.76 |
| 65000.00 | 288.15 | 707.61 |
| 65000.00 | 293.15 | 704.25 |
| 65000.00 | 298.15 | 701.14 |
| 65000.00 | 303.15 | 697.92 |
| 65000.00 | 308.15 | 695.23 |
| 65000.00 | 313.15 | 691.61 |
| 65000.00 | 318.15 | 688.58 |
| 65000.00 | 323.15 | 685.35 |
| 65000.00 | 328.15 | 682.59 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [231.63; 345.96] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.39639e+01 | |||
| Coefficient B | -2.69291e+03 | |||
| Coefficient C | -3.47320e+01 | |||
| Temperature range, min. | 231.63 | |||
| Temperature range, max. | 345.96 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 | ||||
| Pvap | 1.33 | kPa | 231.63 | Calculated Property |
| Pvap | 3.05 | kPa | 244.33 | Calculated Property |
| Pvap | 6.36 | kPa | 257.04 | Calculated Property |
| Pvap | 12.24 | kPa | 269.74 | Calculated Property |
| Pvap | 22.04 | kPa | 282.44 | Calculated Property |
| Pvap | 37.45 | kPa | 295.15 | Calculated Property |
| Pvap | 60.58 | kPa | 307.85 | Calculated Property |
| Pvap | 93.90 | kPa | 320.55 | Calculated Property |
| Pvap | 140.22 | kPa | 333.26 | Calculated Property |
| Pvap | 202.63 | kPa | 345.96 | Calculated Property |
| Pvap | [4.85e-03; 3097.05] | kPa | [174.28; 489.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 7.41375e+01 | |||
| Coefficient B | -5.64285e+03 | |||
| Coefficient C | -9.18104e+00 | |||
| Coefficient D | 9.58793e-06 | |||
| Temperature range, min. | 174.28 | |||
| Temperature range, max. | 489.00 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 200 300 400 | ||||
| Pvap | 4.85e-03 | kPa | 174.28 | Calculated Property |
| Pvap | 0.23 | kPa | 209.25 | Calculated Property |
| Pvap | 3.08 | kPa | 244.22 | Calculated Property |
| Pvap | 19.42 | kPa | 279.19 | Calculated Property |
| Pvap | 76.08 | kPa | 314.16 | Calculated Property |
| Pvap | 217.96 | kPa | 349.12 | Calculated Property |
| Pvap | 505.35 | kPa | 384.09 | Calculated Property |
| Pvap | 1012.80 | kPa | 419.06 | Calculated Property |
| Pvap | 1834.39 | kPa | 454.03 | Calculated Property |
| Pvap | 3097.05 | kPa | 489.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Butane, 2,2-dimethyl-.
Mixtures
- 2-Pyrrolidinone, 1-methyl- + Butane, 2,2-dimethyl-
- 1-Hexene + Butane, 2,2-dimethyl-
- Hexadecane + Butane, 2,2-dimethyl-
- Butane, 2,2-dimethyl- + Octadecane
- n-Butyl ether + Butane, 2,2-dimethyl-
- Di-n-propyl ether + Butane, 2,2-dimethyl-
- Propane, 1,2-dichloro- + Butane, 2,2-dimethyl-
- Butane, 2,2-dimethyl- + Propane, 1,3-dichloro-
- Tridecane + Butane, 2,2-dimethyl-
- Butane, 1-chloro- + Butane, 2,2-dimethyl-
- Butane, 2-chloro- + Butane, 2,2-dimethyl-
- Propane, 1-chloro-2-methyl- + Butane, 2,2-dimethyl-
- Propane, 2-chloro-2-methyl- + Butane, 2,2-dimethyl-
- Butane, 2,2-dimethyl- + Water
- Methane + Butane, 2,2-dimethyl- + Water
- Butane, 2,2-dimethyl- + Tetrahydrofuran
- 1-Hexene + Butane, 2,2-dimethyl- + Tetrahydrofuran
- Butane, 2,2-dimethyl- + Methyl Alcohol
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Liquid-liquid equilibrium data of water with neohexane, methylcyclohexane, tert-butyl methyl ether, n-heptane and vapor -liquid-liquid equilibrium with methane
- Liquid liquid equilibria of lactam containing binary systems
- Experimental and VTPR-predicted volumetric properties of branched hexanes
- 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
- 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
- Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
- Excess enthalpies of binary mixtures of 1-hexene with some branched alkanes at the temperature 298.15 K
- Influence of size and shape effects on the high-pressure solubility of n-alkanes: Experimental data, correlation and prediction
- Excess molar enthalpies of ternary mixtures (1-hexene + tetrahydrofuran + 2,2-dimethylbutane or 2,3-dimethylbutane) at the temperature 298.15 K
- Excess molar enthalpies of ternary mixtures (dibutyl ether or dipropyl ether + 2,2-dimethylbutane + 2,3-dimethylbutane) at the temperature 298.15 K
- 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
- 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
- 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
- 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, 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 water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
- The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
- Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
- Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
- The Critical Temperatures of a Number of (i) (Chloroalkane (C3 C4) + Hydrocarbon (C6 C7)) Binary Mixtures and (ii) (Aromatic Halocarbon (Chlorobenzene, Fluorobenzene, 1,2-Dichlorobenzene, or 1,3-Dichlorobenzene) + Alkane (C8)) Binary Mixtures
- Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
- Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
- Influence of High Pressure on the Liquidus Curve Shape in Binary Hydrocarbon Mixtures: Experimental Data, Correlation, and Prediction
- Liquid-Liquid Coexistence Curves for Binary Systems: Methanol + Cyclohexane and + Several Isomers of Hexane
- Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
- Surface Tension of 2,2-Dimethylbutane from (233 to 378) K
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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