- InChI
- InChI=1S/C7H16/c1-5-6-7(2,3)4/h5-6H2,1-4H3
- InChI Key
- CXOWYJMDMMMMJO-UHFFFAOYSA-N
- Formula
- C7H16
- SMILES
- CCCC(C)(C)C
- Molecular Weight1
- 100.20
- CAS
- 590-35-2
- Other Names
-
- 2,2-Dimethylpentane
- 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).
- μ : Dipole Moment (debye).
- 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).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-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).
- Tboilr : Boiling point at reduced pressure (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 | 0.2870 | KDB | |
| AP | 350.750 | K | KDB |
| ΔcH°liquid | [-4802.60; -4798.00] | kJ/mol |
|
| ΔcH°liquid | -4802.60 ± 1.30 | kJ/mol | NIST |
| ΔcH°liquid | -4798.00 ± 1.00 | kJ/mol | NIST |
| μ | 0.00 | debye | KDB |
| ΔfG° | 0.84 | kJ/mol | KDB |
| Δc,grossH | 4802.60 | kJ/mol | KDB |
| Δc,netH | 4450.479 | kJ/mol | KDB |
| ΔfH°gas | [-209.50; -206.20] | kJ/mol |
|
| ΔfH°gas | -206.30 | kJ/mol | KDB |
| ΔfH°gas | -206.20 ± 1.30 | kJ/mol | NIST |
| ΔfH°gas | -209.50 | kJ/mol | NIST |
| ΔfH°liquid | [-242.00; -238.70] | kJ/mol |
|
| ΔfH°liquid | -238.70 ± 1.30 | kJ/mol | NIST |
| ΔfH°liquid | -242.00 ± 1.00 | kJ/mol | NIST |
| ΔfusH° | 6.47 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [32.20; 32.56] | kJ/mol |
|
| ΔvapH° | 32.56 | kJ/mol | NIST |
| ΔvapH° | 32.40 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 32.40 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 32.20 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 32.42 | kJ/mol | NIST |
| log10WS | [-4.36; -4.36] |
|
|
| log10WS | -4.36 | Aq. Sol... | |
| log10WS | -4.36 | Estimat... | |
| logPoct/wat | 2.833 | Crippen Calculated Property | |
| McVol | 109.490 | ml/mol | McGowan Calculated Property |
| Pc | [2770.00; 2877.63] | kPa |
|
| Pc | 2770.00 | kPa | KDB |
| Pc | 2770.00 ± 50.00 | kPa | NIST |
| Pc | 2773.00 ± 40.53 | kPa | NIST |
| Pc | 2877.63 ± 50.66 | kPa | NIST |
| ρc | [241.49; 241.49] | kg/m3 |
|
| ρc | 241.49 ± 5.01 | kg/m3 | NIST |
| ρc | 241.49 ± 5.01 | kg/m3 | NIST |
| Inp | [615.96; 673.00] |
|
|
| Inp | 622.40 | NIST | |
| Inp | 624.10 | NIST | |
| Inp | 627.70 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 621.00 | NIST | |
| Inp | 628.00 | NIST | |
| Inp | 621.80 | NIST | |
| Inp | 625.70 | NIST | |
| Inp | 625.60 | NIST | |
| Inp | 625.70 | NIST | |
| Inp | 625.60 | NIST | |
| Inp | 625.70 | NIST | |
| Inp | 627.90 | NIST | |
| Inp | 625.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 628.00 | NIST | |
| Inp | 624.80 | NIST | |
| Inp | 628.10 | NIST | |
| Inp | 625.60 | NIST | |
| Inp | 626.90 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 627.00 | NIST | |
| Inp | 625.60 | NIST | |
| Inp | 626.90 | NIST | |
| Inp | 623.80 | NIST | |
| Inp | 624.80 | NIST | |
| Inp | 625.10 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 625.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 627.00 | NIST | |
| Inp | 627.00 | NIST | |
| Inp | 622.70 | NIST | |
| Inp | 623.20 | NIST | |
| Inp | 623.80 | NIST | |
| Inp | 624.40 | NIST | |
| Inp | 625.10 | NIST | |
| Inp | 625.80 | NIST | |
| Inp | 625.70 | NIST | |
| Inp | 625.60 | NIST | |
| Inp | 625.00 | NIST | |
| Inp | 625.00 | NIST | |
| Inp | 625.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 624.00 | NIST | |
| Inp | 623.40 | NIST | |
| Inp | 624.60 | NIST | |
| Inp | 625.70 | NIST | |
| Inp | 627.00 | NIST | |
| Inp | 628.30 | NIST | |
| Inp | 629.70 | NIST | |
| Inp | 627.20 | NIST | |
| Inp | 626.50 | NIST | |
| Inp | 625.60 | NIST | |
| Inp | 625.00 | NIST | |
| Inp | 624.10 | NIST | |
| Inp | 623.10 | NIST | |
| Inp | 625.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 624.00 | NIST | |
| Inp | 625.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 627.00 | NIST | |
| Inp | 628.00 | NIST | |
| Inp | 627.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 624.20 | NIST | |
| Inp | 625.00 | NIST | |
| Inp | 625.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 627.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 627.00 | NIST | |
| Inp | 629.70 | NIST | |
| Inp | 630.40 | NIST | |
| Inp | 631.70 | NIST | |
| Inp | 627.79 | NIST | |
| Inp | 628.51 | NIST | |
| Inp | 621.00 | NIST | |
| Inp | 622.00 | NIST | |
| Inp | 623.00 | NIST | |
| Inp | 623.00 | NIST | |
| Inp | 624.00 | NIST | |
| Inp | 625.80 | NIST | |
| Inp | 622.00 | NIST | |
| Inp | 625.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | Outlier 673.00 | NIST | |
| Inp | 624.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 627.00 | NIST | |
| Inp | 628.00 | NIST | |
| Inp | 624.50 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 624.00 | NIST | |
| Inp | 625.00 | NIST | |
| Inp | 627.00 | NIST | |
| Inp | 625.00 | NIST | |
| Inp | 625.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 625.00 | NIST | |
| Inp | 618.00 | NIST | |
| Inp | 620.00 | NIST | |
| Inp | 624.25 | NIST | |
| Inp | 628.00 | NIST | |
| Inp | 621.40 | NIST | |
| Inp | 615.96 | NIST | |
| Inp | 616.70 | NIST | |
| Inp | 618.20 | NIST | |
| Inp | 620.50 | NIST | |
| Inp | 618.59 | NIST | |
| Inp | 618.60 | NIST | |
| Inp | 619.00 | NIST | |
| Inp | 618.00 | NIST | |
| Inp | 620.00 | NIST | |
| Inp | 624.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 624.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 629.00 | NIST | |
| Inp | 627.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 619.00 | NIST | |
| Inp | 625.00 | NIST | |
| Inp | 622.00 | NIST | |
| Inp | 623.00 | NIST | |
| Inp | 628.00 | NIST | |
| Inp | 619.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | Outlier 669.00 | NIST | |
| Inp | 628.00 | NIST | |
| Inp | Outlier 659.00 | NIST | |
| Inp | 627.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 620.00 | NIST | |
| Inp | 627.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 623.00 | NIST | |
| Inp | 621.00 | NIST | |
| Inp | 622.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 635.00 | NIST | |
| Inp | Outlier 659.00 | NIST | |
| Inp | 633.00 | NIST | |
| Inp | 620.00 | NIST | |
| Inp | 628.00 | NIST | |
| Inp | 627.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 623.00 | NIST | |
| Inp | 624.25 | NIST | |
| S°gas | 392.88 | J/mol×K | NIST |
| S°liquid | [284.90; 300.29] | J/mol×K |
|
| S°liquid | 300.29 | J/mol×K | NIST |
| S°liquid | 284.90 | J/mol×K | NIST |
| Tboil | [351.65; 363.15] | K |
|
| Tboil | 352.30 | K | KDB |
| Tboil | 352.40 | K | NIST |
| Tboil | 352.40 | K | NIST |
| Tboil | 352.65 ± 0.30 | K | NIST |
| Tboil | 353.00 ± 2.00 | K | NIST |
| Tboil | 352.35 ± 0.30 | K | NIST |
| Tboil | 351.65 ± 1.50 | K | NIST |
| Tboil | 352.45 ± 0.30 | K | NIST |
| Tboil | 352.33 ± 0.30 | K | NIST |
| Tboil | 352.35 ± 0.30 | K | NIST |
| Tboil | 352.30 ± 0.30 | K | NIST |
| Tboil | 352.34 ± 0.02 | K | NIST |
| Tboil | 352.15 ± 0.50 | K | NIST |
| Tboil | 352.25 ± 0.50 | K | NIST |
| Tboil | 352.35 ± 0.50 | K | NIST |
| Tboil | 352.15 ± 0.40 | K | NIST |
| Tboil | 352.40 ± 0.50 | K | NIST |
| Tboil | 352.25 ± 0.30 | K | NIST |
| Tboil | 352.15 ± 1.00 | K | NIST |
| Tboil | 352.33 ± 0.20 | K | NIST |
| Tboil | 352.35 ± 0.20 | K | NIST |
| Tboil | 352.35 ± 0.30 | K | NIST |
| Tboil | 352.35 ± 0.01 | K | NIST |
| Tboil | 352.35 ± 0.20 | K | NIST |
| Tboil | 352.35 ± 0.30 | K | NIST |
| Tboil | 352.35 ± 0.20 | K | NIST |
| Tboil | 352.35 ± 0.20 | K | NIST |
| Tboil | 352.25 ± 0.50 | K | NIST |
| Tboil | 352.35 ± 0.20 | K | NIST |
| Tboil | 352.35 ± 0.05 | K | NIST |
| Tboil | 352.25 ± 0.30 | K | NIST |
| Tboil | 352.40 ± 0.50 | K | NIST |
| Tboil | 352.35 ± 0.10 | K | NIST |
| Tboil | 352.40 ± 0.30 | K | NIST |
| Tboil | 352.00 ± 0.50 | K | NIST |
| Tboil | 351.95 ± 0.50 | K | NIST |
| Tboil | 352.45 ± 0.50 | K | NIST |
| Tboil | 352.36 ± 0.20 | K | NIST |
| Tboil | 352.45 ± 0.30 | K | NIST |
| Tboil | 352.36 ± 0.20 | K | NIST |
| Tboil | 352.45 ± 0.50 | K | NIST |
| Tboil | 352.15 ± 0.50 | K | NIST |
| Tboil | 352.45 ± 0.20 | K | NIST |
| Tboil | 352.05 ± 0.50 | K | NIST |
| Tboil | 352.05 ± 0.50 | K | NIST |
| Tboil | 351.95 ± 0.50 | K | NIST |
| Tboil | 352.45 ± 0.50 | K | NIST |
| Tboil | 352.05 ± 0.50 | K | NIST |
| Tboil | 352.05 ± 0.50 | K | NIST |
| Tboil | 353.65 ± 1.00 | K | NIST |
| Tboil | 352.45 ± 0.50 | K | NIST |
| Tboil | 352.45 ± 0.50 | K | NIST |
| Tboil | Outlier 363.15 ± 0.30 | K | NIST |
| Tboil | 353.96 ± 1.00 | K | NIST |
| Tc | [520.44; 520.85] | K |
|
| Tc | 520.50 | K | KDB |
| Tc | 520.50 ± 0.50 | K | NIST |
| Tc | 520.44 ± 0.40 | K | NIST |
| Tc | 520.85 ± 0.50 | K | NIST |
| Tfus | [149.25; 149.30] | K |
|
| Tfus | 149.30 | K | KDB |
| Tfus | 149.25 | K | Aq. Sol... |
| Ttriple | [148.10; 149.43] | K |
|
| Ttriple | 149.37 ± 0.08 | K | NIST |
| Ttriple | 149.43 ± 0.06 | K | NIST |
| Ttriple | 149.37 ± 0.06 | K | NIST |
| Ttriple | 149.41 ± 0.03 | K | NIST |
| Ttriple | 149.38 ± 0.05 | K | NIST |
| Ttriple | 149.42 ± 0.02 | K | NIST |
| Ttriple | Outlier 148.10 ± 0.20 | K | NIST |
| Vc | [0.416; 0.416] | m3/kmol |
|
| Vc | 0.416 | m3/kmol | KDB |
| Vc | 0.416 | m3/kmol | NIST |
| Zc | 0.2662660 | KDB | |
| Zra | 0.27 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [194.59; 266.45] | J/mol×K | [356.33; 530.89] |
|
| Cp,gas | 194.59 | J/mol×K | 356.33 | Joback Calculated Property |
| Cp,gas | 208.03 | J/mol×K | 385.42 | Joback Calculated Property |
| Cp,gas | 220.86 | J/mol×K | 414.52 | Joback Calculated Property |
| Cp,gas | 233.09 | J/mol×K | 443.61 | Joback Calculated Property |
| Cp,gas | 244.75 | J/mol×K | 472.71 | Joback Calculated Property |
| Cp,gas | 255.86 | J/mol×K | 501.80 | Joback Calculated Property |
| Cp,gas | 266.45 | J/mol×K | 530.89 | Joback Calculated Property |
| Cp,liquid | [217.10; 221.12] | J/mol×K | [294.10; 298.15] |
|
| Cp,liquid | 217.10 | J/mol×K | 294.10 | NIST |
| Cp,liquid | 221.12 | J/mol×K | 298.15 | NIST |
| η | [0.0002842; 0.0112423] | Pa×s | [171.07; 356.33] |
|
| η | 0.0112423 | Pa×s | 171.07 | Joback Calculated Property |
| η | 0.0038120 | Pa×s | 201.95 | Joback Calculated Property |
| η | 0.0017220 | Pa×s | 232.82 | Joback Calculated Property |
| η | 0.0009370 | Pa×s | 263.70 | Joback Calculated Property |
| η | 0.0005792 | Pa×s | 294.58 | Joback Calculated Property |
| η | 0.0003923 | Pa×s | 325.45 | Joback Calculated Property |
| η | 0.0002842 | Pa×s | 356.33 | Joback Calculated Property |
| ΔfusH | [5.82; 5.86] | kJ/mol | [148.10; 149.43] |
|
| ΔfusH | 5.86 | kJ/mol | 148.10 | NIST |
| ΔfusH | 5.86 | kJ/mol | 148.10 | NIST |
| ΔfusH | 5.86 | kJ/mol | 148.10 | NIST |
| ΔfusH | 5.82 | kJ/mol | 149.43 | NIST |
| ΔvapH | [28.10; 33.20] | kJ/mol | [308.00; 418.00] |
|
| ΔvapH | 31.80 ± 0.10 | kJ/mol | 308.00 | NIST |
| ΔvapH | 31.40 ± 0.10 | kJ/mol | 315.00 | NIST |
| ΔvapH | 33.20 | kJ/mol | 315.50 | NIST |
| ΔvapH | 32.80 | kJ/mol | 319.00 | NIST |
| ΔvapH | 32.60 | kJ/mol | 320.50 | NIST |
| ΔvapH | 31.00 ± 0.10 | kJ/mol | 323.00 | NIST |
| ΔvapH | 30.50 ± 0.10 | kJ/mol | 330.00 | NIST |
| ΔvapH | 30.10 ± 0.10 | kJ/mol | 338.00 | NIST |
| ΔvapH | 29.40 ± 0.10 | kJ/mol | 348.00 | NIST |
| ΔvapH | 29.23 | kJ/mol | 352.40 | NIST |
| ΔvapH | 29.16 | kJ/mol | 352.40 | KDB |
| ΔvapH | 28.80 ± 0.10 | kJ/mol | 358.00 | NIST |
| ΔvapH | 28.10 ± 0.10 | kJ/mol | 368.00 | NIST |
| ΔvapH | 30.10 | kJ/mol | 418.00 | NIST |
| n0 | 1.37955 | 298.15 | KDB | |
| ρl | 674.00 | kg/m3 | 293.00 | KDB |
| ΔfusS | [38.98; 39.58] | J/mol×K | [148.10; 149.43] |
|
| ΔfusS | 39.58 | J/mol×K | 148.10 | NIST |
| ΔfusS | 38.98 | J/mol×K | 149.43 | NIST |
| γ | 0.02 | N/m | 298.20 | KDB |
| λ | [0.09; 0.11] | W/m×K | [256.16; 337.64] |
|
| λ | 0.11 | W/m×K | 256.16 | Thermal... |
| λ | 0.11 | W/m×K | 256.52 | Thermal... |
| λ | 0.11 | W/m×K | 256.84 | Thermal... |
| λ | 0.10 | W/m×K | 275.45 | Thermal... |
| λ | 0.10 | W/m×K | 275.83 | Thermal... |
| λ | 0.10 | W/m×K | 276.13 | Thermal... |
| λ | 0.10 | W/m×K | 296.32 | Thermal... |
| λ | 0.10 | W/m×K | 296.69 | Thermal... |
| λ | 0.10 | W/m×K | 297.02 | Thermal... |
| λ | 0.09 | W/m×K | 317.22 | Thermal... |
| λ | 0.09 | W/m×K | 317.63 | Thermal... |
| λ | 0.09 | W/m×K | 317.95 | Thermal... |
| λ | 0.09 | W/m×K | 336.91 | Thermal... |
| λ | 0.09 | W/m×K | 337.31 | Thermal... |
| λ | 0.09 | W/m×K | 337.64 | Thermal... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 351.20 | K | 99.10 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [253.24; 377.18] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.41875e+01 | |||
| Coefficient B | -3.04378e+03 | |||
| Coefficient C | -3.42570e+01 | |||
| Temperature range, min. | 253.24 | |||
| Temperature range, max. | 377.18 | |||
| Pvap | 1.33 | kPa | 253.24 | Calculated Property |
| Pvap | 3.04 | kPa | 267.01 | Calculated Property |
| Pvap | 6.30 | kPa | 280.78 | Calculated Property |
| Pvap | 12.11 | kPa | 294.55 | Calculated Property |
| Pvap | 21.79 | kPa | 308.32 | Calculated Property |
| Pvap | 37.07 | kPa | 322.10 | Calculated Property |
| Pvap | 60.08 | kPa | 335.87 | Calculated Property |
| Pvap | 93.35 | kPa | 349.64 | Calculated Property |
| Pvap | 139.79 | kPa | 363.41 | Calculated Property |
| Pvap | 202.65 | kPa | 377.18 | Calculated Property |
| Pvap | [4.58e-06; 2712.21] | kPa | [149.34; 520.50] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.63234e+01 | |||
| Coefficient B | -5.95594e+03 | |||
| Coefficient C | -7.76366e+00 | |||
| Coefficient D | 5.84993e-06 | |||
| Temperature range, min. | 149.34 | |||
| Temperature range, max. | 520.50 | |||
| Pvap | 4.58e-06 | kPa | 149.34 | Calculated Property |
| Pvap | 4.19e-03 | kPa | 190.58 | Calculated Property |
| Pvap | 0.26 | kPa | 231.82 | Calculated Property |
| Pvap | 4.04 | kPa | 273.06 | Calculated Property |
| Pvap | 27.32 | kPa | 314.30 | Calculated Property |
| Pvap | 111.07 | kPa | 355.54 | Calculated Property |
| Pvap | 324.02 | kPa | 396.78 | Calculated Property |
| Pvap | 755.80 | kPa | 438.02 | Calculated Property |
| Pvap | 1511.03 | kPa | 479.26 | Calculated Property |
| Pvap | 2712.21 | kPa | 520.50 | Calculated Property |
Similar Compounds
Find more compounds similar to Pentane, 2,2-dimethyl-.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.