- InChI
- InChI=1S/C8H18/c1-6(2)8(5)7(3)4/h6-8H,1-5H3
- InChI Key
- RLPGDEORIPLBNF-UHFFFAOYSA-N
- Formula
- C8H18
- SMILES
- CC(C)C(C)C(C)C
- Molecular Weight1
- 114.23
- CAS
- 565-75-3
- Other Names
-
- (CH3)2CHCH(CH3)CH(CH3)2
- 2,3,4-Trimethylpentane
- 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).
- 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).
- 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.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3150 | KDB | |
| AP | 341.450 | K | KDB |
| ΔcH°liquid | -5465.50 ± 1.60 | kJ/mol | NIST |
| ΔfG° | 18.92 | kJ/mol | KDB |
| Δc,grossH | 5465.48 | kJ/mol | KDB |
| Δc,netH | 5069.335 | kJ/mol | KDB |
| ΔfH°gas | [-217.60; -217.40] | kJ/mol |
|
| ΔfH°gas | -217.60 | kJ/mol | KDB |
| ΔfH°gas | -217.40 ± 1.70 | kJ/mol | NIST |
| ΔfH°liquid | -255.20 ± 1.70 | kJ/mol | NIST |
| ΔfusH° | 5.91 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [37.70; 37.82] | kJ/mol |
|
| ΔvapH° | 37.82 | kJ/mol | NIST |
| ΔvapH° | 37.70 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 37.70 | kJ/mol | NIST |
| ΔvapH° | 37.70 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 37.70 | kJ/mol | NIST |
| log10WS | [-4.80; -4.80] |
|
|
| log10WS | -4.80 | Aq. Sol... | |
| log10WS | -4.80 | Estimat... | |
| logPoct/wat | 2.934 | Crippen Calculated Property | |
| McVol | 123.580 | ml/mol | McGowan Calculated Property |
| Pc | [2729.80; 2730.00] | kPa |
|
| Pc | 2730.00 | kPa | KDB |
| Pc | 2730.00 ± 40.00 | kPa | NIST |
| Pc | 2729.80 ± 40.53 | kPa | NIST |
| ρc | [247.88; 247.88] | kg/m3 |
|
| ρc | 247.88 ± 4.57 | kg/m3 | NIST |
| ρc | 247.88 ± 4.57 | kg/m3 | NIST |
| Inp | [743.00; 771.30] |
|
|
| Inp | 747.10 | NIST | |
| Inp | 750.20 | NIST | |
| Inp | Outlier 765.10 | NIST | |
| Inp | 743.00 | NIST | |
| Inp | 745.00 | NIST | |
| Inp | Outlier 765.60 | NIST | |
| Inp | Outlier 771.30 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | Outlier 764.20 | NIST | |
| Inp | 743.00 | NIST | |
| Inp | Outlier 765.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 751.60 | NIST | |
| Inp | 755.05 | NIST | |
| Inp | 748.40 | NIST | |
| Inp | 749.80 | NIST | |
| Inp | 751.20 | NIST | |
| Inp | 752.70 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 748.30 | NIST | |
| Inp | 749.60 | NIST | |
| Inp | 751.00 | NIST | |
| Inp | 752.50 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 755.60 | NIST | |
| Inp | 751.90 | NIST | |
| Inp | 751.90 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 748.20 | NIST | |
| Inp | 749.70 | NIST | |
| Inp | 751.30 | NIST | |
| Inp | 752.90 | NIST | |
| Inp | 754.60 | NIST | |
| Inp | 756.40 | NIST | |
| Inp | 747.70 | NIST | |
| Inp | 748.30 | NIST | |
| Inp | 749.30 | NIST | |
| Inp | 750.10 | NIST | |
| Inp | 751.10 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 755.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 755.50 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 755.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 751.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 752.50 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 758.00 | NIST | |
| Inp | 751.00 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 755.00 | NIST | |
| Inp | 757.00 | NIST | |
| Inp | 750.50 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 751.00 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 743.00 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 746.70 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 759.00 | NIST | |
| Inp | 743.63 | NIST | |
| Inp | 747.60 | NIST | |
| Inp | 744.80 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 745.00 | NIST | |
| Inp | 743.00 | NIST | |
| Inp | 757.70 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 759.00 | NIST | |
| Inp | 755.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | 751.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 757.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 743.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 743.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 761.00 | NIST | |
| Inp | 760.00 | NIST | |
| Inp | 761.00 | NIST | |
| Inp | 760.00 | NIST | |
| Inp | 759.00 | NIST | |
| Inp | 745.00 | NIST | |
| S°gas | 427.20 ± 1.30 | J/mol×K | NIST |
| S°liquid | 329.32 | J/mol×K | NIST |
| Tboil | 386.60 | K | KDB |
| Tc | [566.30; 566.40] | K |
|
| Tc | 566.40 | K | KDB |
| Tc | 566.40 ± 0.50 | K | NIST |
| Tc | 566.30 | K | NIST |
| Tc | 566.34 ± 0.50 | K | NIST |
| Tfus | [163.75; 163.90] | K |
|
| Tfus | 163.90 | K | KDB |
| Tfus | 163.75 | K | Aq. Sol... |
| Ttriple | 163.63 ± 0.12 | K | NIST |
| Vc | [0.460; 0.460] | m3/kmol |
|
| Vc | 0.460 | m3/kmol | KDB |
| Vc | 0.460 | m3/kmol | NIST |
| Zc | 0.2666620 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [233.50; 304.96] | J/mol×K | [373.15; 523.15] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 240 260 280 300 400 450 500 | ||||
| Cp,gas | 233.50 ± 0.47 | J/mol×K | 373.15 | NIST |
| Cp,gas | 246.46 ± 0.49 | J/mol×K | 398.15 | NIST |
| Cp,gas | 248.11 | J/mol×K | 402.80 | NIST |
| Cp,gas | 251.50 ± 2.50 | J/mol×K | 417.00 | NIST |
| Cp,gas | 258.52 ± 0.52 | J/mol×K | 423.15 | NIST |
| Cp,gas | 271.05 ± 0.54 | J/mol×K | 448.15 | NIST |
| Cp,gas | 276.98 | J/mol×K | 463.60 | NIST |
| Cp,gas | 283.03 ± 0.57 | J/mol×K | 473.15 | NIST |
| Cp,gas | 293.98 ± 0.59 | J/mol×K | 498.15 | NIST |
| Cp,gas | 303.34 | J/mol×K | 521.60 | NIST |
| Cp,gas | 304.96 ± 0.61 | J/mol×K | 523.15 | NIST |
| Cp,liquid | [246.23; 247.32] | J/mol×K | [293.79; 298.15] |
|
| Cp,liquid | 246.23 | J/mol×K | 293.79 | NIST |
| Cp,liquid | 247.32 | J/mol×K | 298.15 | NIST |
| η | [0.0002228; 0.0624902] | Pa×s | [134.92; 381.12] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 0.01 0.02 0.03 0.04 0.05 0.06 200 300 | ||||
| η | 0.0624902 | Pa×s | 134.92 | Joback Calculated Property |
| η | 0.0081685 | Pa×s | 175.95 | Joback Calculated Property |
| η | 0.0023051 | Pa×s | 216.99 | Joback Calculated Property |
| η | 0.0009727 | Pa×s | 258.02 | Joback Calculated Property |
| η | 0.0005201 | Pa×s | 299.05 | Joback Calculated Property |
| η | 0.0003235 | Pa×s | 340.09 | Joback Calculated Property |
| η | 0.0002228 | Pa×s | 381.12 | Joback Calculated Property |
| ΔfusH | [9.27; 9.27] | kJ/mol | [163.60; 163.63] |
|
| ΔfusH | 9.27 | kJ/mol | 163.60 | NIST |
| ΔfusH | 9.27 | kJ/mol | 163.60 | NIST |
| ΔfusH | 9.27 | kJ/mol | 163.63 | NIST |
| ΔvapH | [32.36; 41.30] | kJ/mol | [250.50; 386.60] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 32 34 36 38 40 42 250 300 350 | ||||
| ΔvapH | 39.80 | kJ/mol | 250.50 | NIST |
| ΔvapH | 39.10 | kJ/mol | 256.00 | NIST |
| ΔvapH | 41.30 | kJ/mol | 324.50 | NIST |
| ΔvapH | 37.70 | kJ/mol | 344.00 | NIST |
| ΔvapH | 36.70 | kJ/mol | 349.00 | NIST |
| ΔvapH | 32.36 | kJ/mol | 386.60 | NIST |
| ΔvapH | 32.73 | kJ/mol | 386.60 | KDB |
| n0 | 1.40198 | 298.15 | KDB | |
| ρl | 719.00 | kg/m3 | 293.00 | KDB |
| ΔfusS | 56.64 | J/mol×K | 163.63 | NIST |
| γ | 0.02 | N/m | 298.20 | KDB |
| λ | [0.10; 0.11] | W/m×K | [259.06; 332.39] |
|
|
T(K) Liquid thermal conductivity (W/m×K) 0.1 0.1 0.11 0.11 260 280 300 320 | ||||
| λ | 0.11 | W/m×K | 259.06 | Thermal... |
| λ | 0.11 | W/m×K | 259.29 | Thermal... |
| λ | 0.11 | W/m×K | 259.54 | Thermal... |
| λ | 0.11 | W/m×K | 277.95 | Thermal... |
| λ | 0.11 | W/m×K | 278.19 | Thermal... |
| λ | 0.11 | W/m×K | 278.44 | Thermal... |
| λ | 0.10 | W/m×K | 297.33 | Thermal... |
| λ | 0.10 | W/m×K | 297.58 | Thermal... |
| λ | 0.10 | W/m×K | 297.84 | Thermal... |
| λ | 0.10 | W/m×K | 315.53 | Thermal... |
| λ | 0.10 | W/m×K | 315.77 | Thermal... |
| λ | 0.10 | W/m×K | 316.03 | Thermal... |
| λ | 0.10 | W/m×K | 331.87 | Thermal... |
| λ | 0.10 | W/m×K | 332.13 | Thermal... |
| λ | 0.10 | W/m×K | 332.39 | Thermal... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 130.00 | 728.3 |
| 283.15 | 4973.00 | 732.2 |
| 283.15 | 9993.00 | 736.0 |
| 283.15 | 14965.00 | 739.6 |
| 283.15 | 20000.00 | 743.0 |
| 283.15 | 25003.00 | 746.3 |
| 283.15 | 29990.00 | 749.5 |
| 283.15 | 35009.00 | 752.5 |
| 283.15 | 39961.00 | 755.4 |
| 283.15 | 45014.00 | 758.3 |
| 283.15 | 49986.00 | 761.0 |
| 283.15 | 54944.00 | 763.6 |
| 283.15 | 60030.00 | 766.3 |
| 283.15 | 65014.00 | 768.8 |
| 288.15 | 102.00 | 724.3 |
| 288.15 | 5015.00 | 728.4 |
| 288.15 | 9991.00 | 732.3 |
| 288.15 | 14975.00 | 736.0 |
| 288.15 | 20038.00 | 739.6 |
| 288.15 | 25021.00 | 743.0 |
| 288.15 | 29929.00 | 746.1 |
| 288.15 | 35037.00 | 749.3 |
| 288.15 | 40039.00 | 752.3 |
| 288.15 | 44998.00 | 755.2 |
| 288.15 | 49927.00 | 757.9 |
| 288.15 | 54967.00 | 760.6 |
| 288.15 | 59925.00 | 763.2 |
| 288.15 | 65032.00 | 765.9 |
| 293.15 | 111.00 | 720.4 |
| 293.15 | 5021.00 | 724.6 |
| 293.15 | 9998.00 | 728.6 |
| 293.15 | 14997.00 | 732.4 |
| 293.15 | 19997.00 | 736.1 |
| 293.15 | 25022.00 | 739.6 |
| 293.15 | 29930.00 | 742.8 |
| 293.15 | 34968.00 | 746.0 |
| 293.15 | 39974.00 | 749.1 |
| 293.15 | 45009.00 | 752.0 |
| 293.15 | 49965.00 | 754.9 |
| 293.15 | 54987.00 | 757.6 |
| 293.15 | 59945.00 | 760.3 |
| 293.15 | 65000.00 | 762.9 |
| 298.15 | 105.00 | 716.2 |
| 298.15 | 5072.00 | 720.6 |
| 298.15 | 9964.00 | 724.7 |
| 298.15 | 15013.00 | 728.7 |
| 298.15 | 20054.00 | 732.5 |
| 298.15 | 25008.00 | 736.0 |
| 298.15 | 29968.00 | 739.4 |
| 298.15 | 34937.00 | 742.6 |
| 298.15 | 40018.00 | 745.8 |
| 298.15 | 45064.00 | 748.8 |
| 298.15 | 50010.00 | 751.7 |
| 298.15 | 55015.00 | 754.5 |
| 298.15 | 59955.00 | 757.2 |
| 298.15 | 65024.00 | 759.9 |
| 303.15 | 100.00 | 712.0 |
| 303.15 | 4934.00 | 716.5 |
| 303.15 | 10038.00 | 720.9 |
| 303.15 | 14973.00 | 724.9 |
| 303.15 | 19957.00 | 728.7 |
| 303.15 | 25002.00 | 732.4 |
| 303.15 | 29980.00 | 735.9 |
| 303.15 | 34972.00 | 739.3 |
| 303.15 | 39972.00 | 742.5 |
| 303.15 | 44990.00 | 745.6 |
| 303.15 | 49984.00 | 748.5 |
| 303.15 | 54948.00 | 751.4 |
| 303.15 | 59951.00 | 754.2 |
| 303.15 | 65040.00 | 756.9 |
| 308.15 | 92.00 | 707.8 |
| 308.15 | 5051.00 | 712.5 |
| 308.15 | 9961.00 | 716.8 |
| 308.15 | 14959.00 | 721.0 |
| 308.15 | 20027.00 | 725.0 |
| 308.15 | 25025.00 | 728.8 |
| 308.15 | 29996.00 | 732.4 |
| 308.15 | 34959.00 | 735.7 |
| 308.15 | 40017.00 | 739.1 |
| 308.15 | 45023.00 | 742.2 |
| 308.15 | 49965.00 | 745.2 |
| 308.15 | 54977.00 | 748.2 |
| 308.15 | 60020.00 | 751.0 |
| 308.15 | 64995.00 | 753.8 |
| 313.15 | 99.00 | 703.6 |
| 313.15 | 4997.00 | 708.5 |
| 313.15 | 9998.00 | 713.1 |
| 313.15 | 15010.00 | 717.4 |
| 313.15 | 19994.00 | 721.4 |
| 313.15 | 25007.00 | 725.3 |
| 313.15 | 29995.00 | 729.0 |
| 313.15 | 35008.00 | 732.4 |
| 313.15 | 39993.00 | 735.8 |
| 313.15 | 45005.00 | 739.0 |
| 313.15 | 49990.00 | 742.1 |
| 313.15 | 55003.00 | 745.1 |
| 313.15 | 59996.00 | 748.0 |
| 313.15 | 64993.00 | 750.8 |
| 318.15 | 104.00 | 699.5 |
| 318.15 | 4961.00 | 704.4 |
| 318.15 | 10003.00 | 709.2 |
| 318.15 | 15026.00 | 713.7 |
| 318.15 | 19937.00 | 717.8 |
| 318.15 | 25012.00 | 721.8 |
| 318.15 | 29990.00 | 725.5 |
| 318.15 | 34991.00 | 729.1 |
| 318.15 | 39976.00 | 732.5 |
| 318.15 | 45028.00 | 735.8 |
| 318.15 | 49973.00 | 739.0 |
| 318.15 | 54916.00 | 742.0 |
| 318.15 | 59988.00 | 744.9 |
| 318.15 | 65015.00 | 747.8 |
| 323.15 | 111.00 | 695.4 |
| 323.15 | 5025.00 | 700.6 |
| 323.15 | 10013.00 | 705.5 |
| 323.15 | 14973.00 | 710.0 |
| 323.15 | 20028.00 | 714.4 |
| 323.15 | 25014.00 | 718.4 |
| 323.15 | 29976.00 | 722.2 |
| 323.15 | 34994.00 | 725.9 |
| 323.15 | 39992.00 | 729.4 |
| 323.15 | 45046.00 | 732.8 |
| 323.15 | 49980.00 | 736.0 |
| 323.15 | 54968.00 | 739.1 |
| 323.15 | 59988.00 | 742.1 |
| 323.15 | 65068.00 | 745.0 |
| 328.15 | 94.00 | 691.3 |
| 328.15 | 4971.00 | 696.6 |
| 328.15 | 9997.00 | 701.7 |
| 328.15 | 14959.00 | 706.4 |
| 328.15 | 19969.00 | 710.9 |
| 328.15 | 25055.00 | 715.1 |
| 328.15 | 29960.00 | 719.0 |
| 328.15 | 34966.00 | 722.7 |
| 328.15 | 40013.00 | 726.3 |
| 328.15 | 45034.00 | 729.8 |
| 328.15 | 50015.00 | 733.1 |
| 328.15 | 54973.00 | 736.2 |
| 328.15 | 59955.00 | 739.2 |
| 328.15 | 64992.00 | 742.2 |
| 333.15 | 95.00 | 687.1 |
| 333.15 | 4934.00 | 692.6 |
| 333.15 | 9973.00 | 697.9 |
| 333.15 | 14973.00 | 702.8 |
| 333.15 | 19993.00 | 707.4 |
| 333.15 | 24959.00 | 711.6 |
| 333.15 | 29952.00 | 715.7 |
| 333.15 | 34974.00 | 719.5 |
| 333.15 | 39961.00 | 723.2 |
| 333.15 | 44999.00 | 726.7 |
| 333.15 | 49992.00 | 730.1 |
| 333.15 | 54798.00 | 733.2 |
| 333.15 | 59952.00 | 736.4 |
| 333.15 | 65050.00 | 739.5 |
| 338.15 | 115.00 | 683.1 |
| 338.15 | 4978.00 | 688.9 |
| 338.15 | 9970.00 | 694.3 |
| 338.15 | 14966.00 | 699.3 |
| 338.15 | 19960.00 | 703.9 |
| 338.15 | 24994.00 | 708.4 |
| 338.15 | 30030.00 | 712.5 |
| 338.15 | 34973.00 | 716.3 |
| 338.15 | 39979.00 | 720.0 |
| 338.15 | 45024.00 | 723.6 |
| 338.15 | 50019.00 | 727.1 |
| 338.15 | 54928.00 | 730.3 |
| 338.15 | 59953.00 | 733.5 |
| 338.15 | 64998.00 | 736.6 |
| 343.15 | 109.00 | 678.8 |
| 343.15 | 5084.00 | 684.9 |
| 343.15 | 9963.00 | 690.4 |
| 343.15 | 15039.00 | 695.6 |
| 343.15 | 20010.00 | 700.4 |
| 343.15 | 24998.00 | 704.9 |
| 343.15 | 30054.00 | 709.2 |
| 343.15 | 35048.00 | 713.2 |
| 343.15 | 40023.00 | 717.0 |
| 343.15 | 44967.00 | 720.6 |
| 343.15 | 50023.00 | 724.2 |
| 343.15 | 54967.00 | 727.5 |
| 343.15 | 59995.00 | 730.7 |
| 343.15 | 64954.00 | 733.8 |
| 348.15 | 112.00 | 674.5 |
| 348.15 | 5011.00 | 680.8 |
| 348.15 | 10066.00 | 686.6 |
| 348.15 | 14992.00 | 691.9 |
| 348.15 | 19955.00 | 696.8 |
| 348.15 | 25042.00 | 701.5 |
| 348.15 | 29986.00 | 705.8 |
| 348.15 | 35004.00 | 709.9 |
| 348.15 | 40002.00 | 713.9 |
| 348.15 | 44996.00 | 717.6 |
| 348.15 | 49994.00 | 721.1 |
| 348.15 | 54995.00 | 724.6 |
| 348.15 | 60005.00 | 727.9 |
| 348.15 | 65009.00 | 731.0 |
| 353.15 | 109.00 | 670.1 |
| 353.15 | 4963.00 | 676.6 |
| 353.15 | 9919.00 | 682.5 |
| 353.15 | 15039.00 | 688.2 |
| 353.15 | 19995.00 | 693.2 |
| 353.15 | 24983.00 | 698.0 |
| 353.15 | 29960.00 | 702.4 |
| 353.15 | 34985.00 | 706.7 |
| 353.15 | 39983.00 | 710.7 |
| 353.15 | 45037.00 | 714.5 |
| 353.15 | 49989.00 | 718.1 |
| 353.15 | 54953.00 | 721.6 |
| 353.15 | 59909.00 | 724.9 |
| 353.15 | 65052.00 | 728.2 |
| 358.15 | 118.00 | 665.9 |
| 358.15 | 4955.00 | 672.5 |
| 358.15 | 9916.00 | 678.7 |
| 358.15 | 15035.00 | 684.5 |
| 358.15 | 19946.00 | 689.6 |
| 358.15 | 25037.00 | 694.6 |
| 358.15 | 29963.00 | 699.2 |
| 358.15 | 35027.00 | 703.4 |
| 358.15 | 40010.00 | 707.5 |
| 358.15 | 44955.00 | 711.4 |
| 358.15 | 50023.00 | 715.1 |
| 358.15 | 54980.00 | 718.7 |
| 358.15 | 59952.00 | 722.0 |
| 358.15 | 65021.00 | 725.4 |
| 363.15 | 101.00 | 661.3 |
| 363.15 | 4941.00 | 668.3 |
| 363.15 | 9928.00 | 674.7 |
| 363.15 | 15005.00 | 680.6 |
| 363.15 | 19958.00 | 686.0 |
| 363.15 | 24923.00 | 691.0 |
| 363.15 | 29983.00 | 695.8 |
| 363.15 | 34922.00 | 700.1 |
| 363.15 | 39992.00 | 704.4 |
| 363.15 | 45038.00 | 708.4 |
| 363.15 | 49985.00 | 712.2 |
| 363.15 | 54981.00 | 715.8 |
| 363.15 | 59985.00 | 719.3 |
| 363.15 | 65038.00 | 722.6 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [279.22; 413.45] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.42673e+01 | |||
| Coefficient B | -3.34524e+03 | |||
| Coefficient C | -3.99270e+01 | |||
| Temperature range, min. | 279.22 | |||
| Temperature range, max. | 413.45 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
| Pvap | 1.33 | kPa | 279.22 | Calculated Property |
| Pvap | 3.03 | kPa | 294.13 | Calculated Property |
| Pvap | 6.28 | kPa | 309.05 | Calculated Property |
| Pvap | 12.06 | kPa | 323.96 | Calculated Property |
| Pvap | 21.70 | kPa | 338.88 | Calculated Property |
| Pvap | 36.93 | kPa | 353.79 | Calculated Property |
| Pvap | 59.90 | kPa | 368.71 | Calculated Property |
| Pvap | 93.14 | kPa | 383.62 | Calculated Property |
| Pvap | 139.62 | kPa | 398.54 | Calculated Property |
| Pvap | 202.63 | kPa | 413.45 | Calculated Property |
| Pvap | [3.04e-06; 2702.14] | kPa | [163.95; 566.30] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 7.53988e+01 | |||
| Coefficient B | -6.92178e+03 | |||
| Coefficient C | -9.02988e+00 | |||
| Coefficient D | 6.13464e-06 | |||
| Temperature range, min. | 163.95 | |||
| Temperature range, max. | 566.30 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 200 300 400 500 | ||||
| Pvap | 3.04e-06 | kPa | 163.95 | Calculated Property |
| Pvap | 3.24e-03 | kPa | 208.66 | Calculated Property |
| Pvap | 0.22 | kPa | 253.36 | Calculated Property |
| Pvap | 3.58 | kPa | 298.07 | Calculated Property |
| Pvap | 24.98 | kPa | 342.77 | Calculated Property |
| Pvap | 103.66 | kPa | 387.48 | Calculated Property |
| Pvap | 307.29 | kPa | 432.18 | Calculated Property |
| Pvap | 727.54 | kPa | 476.89 | Calculated Property |
| Pvap | 1477.92 | kPa | 521.59 | Calculated Property |
| Pvap | 2702.14 | kPa | 566.30 | Calculated Property |
Similar Compounds
Find more compounds similar to Pentane, 2,3,4-trimethyl-.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
- P-r-T Data and Derivative Properties of 3-Methylpentane, 2,4-Dimethylpentane, and 2,3,4-Trimethylpentane from 283.15 to 363.15 K at Pressures up to 65 MPa
- 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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