- InChI
- InChI=1S/C5H10/c1-3-5-4-2/h3H,1,4-5H2,2H3
- InChI Key
- YWAKXRMUMFPDSH-UHFFFAOYSA-N
- Formula
- C5H10
- SMILES
- C=CCCC
- Molecular Weight1
- 70.13
- CAS
- 109-67-1
- Other Names
-
- 1-C5H10
- 1-Pentene 95
- PENT-1-ENE
- PENTENE-1
- PROPYLETHYLENE
- «alpha»-n-Amylene
- «alpha»-n-Amylene
- ω : Acentric Factor.
- Tig : Autoignition Temperature (K).
- 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).
- LFL : Lower Flammability Limit (% in Air).
- UFL : Upper Flammability Limit (% in Air).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- 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).
- 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).
- 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°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 | 0.2330 | KDB | |
| Tig | 548.15 | K | KDB |
| AP | 292.150 | K | KDB |
| ΔcH°liquid | -3349.72 ± 0.58 | kJ/mol | NIST |
| μ | 0.40 | debye | KDB |
| LFL | 1.40 | % in Air | KDB |
| UFL | 8.70 | % in Air | KDB |
| Tflash,cc | 255.37 | K | KDB |
| Tflash,oc | 222.04 | K | KDB |
| ΔfG° | 79.17 | kJ/mol | KDB |
| Δc,grossH | 3350.05 | kJ/mol | KDB |
| Δc,netH | 3130.009 | kJ/mol | KDB |
| ΔfH°gas | -20.93 | kJ/mol | KDB |
| ΔfusH° | 7.43 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [25.50; 29.82] | kJ/mol |
|
| ΔvapH° | 29.82 | kJ/mol | NIST |
| ΔvapH° | 25.50 | kJ/mol | NIST |
| ΔvapH° | 25.50 ± 0.10 | kJ/mol | NIST |
| IE | [9.42; 9.82] | eV |
|
| IE | 9.49 ± 0.03 | eV | NIST |
| IE | 9.50 | eV | NIST |
| IE | 9.52 ± 0.05 | eV | NIST |
| IE | 9.42 ± 0.02 | eV | NIST |
| IE | 9.52 ± 0.02 | eV | NIST |
| IE | 9.52 ± 0.00 | eV | NIST |
| IE | 9.48 | eV | NIST |
| IE | Outlier 9.82 ± 0.06 | eV | NIST |
| IE | 9.50 ± 0.02 | eV | NIST |
| IE | 9.50 ± 0.02 | eV | NIST |
| IE | 9.68 ± 0.01 | eV | NIST |
| IE | 9.54 ± 0.02 | eV | NIST |
| log10WS | [-2.68; -2.68] |
|
|
| log10WS | -2.68 | Aq. Sol... | |
| log10WS | -2.68 | Estimat... | |
| logPoct/wat | 1.973 | Crippen Calculated Property | |
| McVol | 77.010 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 4 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | [3550.00; 3560.00] | kPa |
|
| Pc | 3560.00 | kPa | KDB |
| Pc | 3560.00 ± 50.00 | kPa | NIST |
| Pc | 3550.00 ± 20.00 | kPa | NIST |
| Pc | 3551.00 ± 3.44 | kPa | NIST |
| ρc | [232.84; 234.95] | kg/m3 |
|
| ρc | 234.95 ± 3.51 | kg/m3 | NIST |
| ρc | 232.84 ± 2.10 | kg/m3 | NIST |
| Inp | [478.00; 500.00] |
|
|
| Inp | 489.00 | NIST | |
| Inp | 481.10 | NIST | |
| Inp | 485.00 | NIST | |
| Inp | 483.00 | NIST | |
| Inp | 480.00 | NIST | |
| Inp | 488.80 | NIST | |
| Inp | 489.00 | NIST | |
| Inp | 491.00 | NIST | |
| Inp | 488.00 | NIST | |
| Inp | 488.00 | NIST | |
| Inp | 489.00 | NIST | |
| Inp | 481.30 | NIST | |
| Inp | 488.80 | NIST | |
| Inp | Outlier 496.00 | NIST | |
| Inp | 489.00 | NIST | |
| Inp | 489.00 | NIST | |
| Inp | 492.00 | NIST | |
| Inp | 486.00 | NIST | |
| Inp | 481.60 | NIST | |
| Inp | 482.00 | NIST | |
| Inp | 481.50 | NIST | |
| Inp | 481.60 | NIST | |
| Inp | 482.00 | NIST | |
| Inp | 482.00 | NIST | |
| Inp | 486.80 | NIST | |
| Inp | 482.50 | NIST | |
| Inp | 482.00 | NIST | |
| Inp | 482.00 | NIST | |
| Inp | 481.07 | NIST | |
| Inp | 491.00 | NIST | |
| Inp | 482.00 | NIST | |
| Inp | 481.00 | NIST | |
| Inp | 481.00 | NIST | |
| Inp | 483.00 | NIST | |
| Inp | 483.00 | NIST | |
| Inp | 490.00 | NIST | |
| Inp | 483.00 | NIST | |
| Inp | 479.00 | NIST | |
| Inp | 485.00 | NIST | |
| Inp | 491.00 | NIST | |
| Inp | 491.00 | NIST | |
| Inp | 486.50 | NIST | |
| Inp | 487.00 | NIST | |
| Inp | 483.39 | NIST | |
| Inp | 483.67 | NIST | |
| Inp | 483.00 | NIST | |
| Inp | 478.00 | NIST | |
| Inp | 481.30 | NIST | |
| Inp | 482.00 | NIST | |
| Inp | 492.00 | NIST | |
| Inp | 482.00 | NIST | |
| Inp | Outlier 500.00 | NIST | |
| Inp | 488.00 | NIST | |
| Inp | 489.00 | NIST | |
| Inp | 491.00 | NIST | |
| Inp | 492.00 | NIST | |
| Inp | 492.00 | NIST | |
| Inp | Outlier 495.00 | NIST | |
| Inp | 488.00 | NIST | |
| Inp | 483.00 | NIST | |
| Inp | 483.00 | NIST | |
| Inp | 487.00 | NIST | |
| Inp | 483.00 | NIST | |
| Inp | 486.00 | NIST | |
| Inp | 483.00 | NIST | |
| Inp | 483.00 | NIST | |
| Inp | 483.00 | NIST | |
| Inp | 491.00 | NIST | |
| Inp | 479.00 | NIST | |
| Inp | 489.00 | NIST | |
| Inp | 484.00 | NIST | |
| Inp | 488.00 | NIST | |
| Inp | 488.00 | NIST | |
| Inp | 483.00 | NIST | |
| Inp | 488.00 | NIST | |
| Inp | 488.00 | NIST | |
| Inp | 483.00 | NIST | |
| Inp | 485.00 | NIST | |
| Inp | 492.00 | NIST | |
| Inp | 492.00 | NIST | |
| Inp | 492.00 | NIST | |
| Inp | 479.00 | NIST | |
| Inp | 483.00 | NIST | |
| Inp | 484.00 | NIST | |
| Inp | 488.00 | NIST | |
| Inp | 492.00 | NIST | |
| I | [523.00; 534.00] |
|
|
| I | 532.00 | NIST | |
| I | 523.00 | NIST | |
| I | 534.00 | NIST | |
| S°liquid | [262.55; 262.60] | J/mol×K |
|
| S°liquid | 262.60 | J/mol×K | NIST |
| S°liquid | 262.60 | J/mol×K | NIST |
| S°liquid | 262.55 | J/mol×K | NIST |
| Tboil | 303.11 | K | KDB |
| Tc | [463.77; 466.59] | K |
|
| Tc | 464.80 | K | KDB |
| Tc | Outlier 466.59 | K | Vapor P... |
| Tc | 464.80 ± 0.50 | K | NIST |
| Tc | 464.70 | K | NIST |
| Tc | 465.10 ± 0.30 | K | NIST |
| Tc | 463.77 ± 0.20 | K | NIST |
| Tc | 464.74 ± 0.03 | K | NIST |
| Tfus | [107.75; 108.08] | K |
|
| Tfus | 107.90 | K | KDB |
| Tfus | 108.08 | K | Aq. Sol... |
| Tfus | 107.75 ± 0.20 | K | NIST |
| Tfus | 107.78 ± 0.20 | K | NIST |
| Tfus | 107.88 ± 0.10 | K | NIST |
| Ttriple | [5.80; 108.01] | K |
|
| Ttriple | 108.01 ± 0.00 | K | NIST |
| Ttriple | 107.79 ± 0.00 | K | NIST |
| Ttriple | 5.80 ± 0.01 | K | NIST |
| Ttriple | 107.90 ± 0.50 | K | NIST |
| Vc | [0.298; 0.298] | m3/kmol |
|
| Vc | 0.298 | m3/kmol | KDB |
| Vc | 0.298 | m3/kmol | NIST |
| Zc | 0.2748820 | KDB | |
| Zra | 0.27 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [112.34; 157.69] | J/mol×K | [311.09; 471.08] |
|
| Cp,gas | 112.34 ± 0.33 | J/mol×K | 311.09 | NIST |
| Cp,gas | 126.15 ± 0.38 | J/mol×K | 357.51 | NIST |
| Cp,gas | 139.08 ± 0.42 | J/mol×K | 402.32 | NIST |
| Cp,gas | 148.41 ± 0.45 | J/mol×K | 436.01 | NIST |
| Cp,gas | 157.69 ± 0.47 | J/mol×K | 471.08 | NIST |
| Cp,liquid | [154.00; 155.31] | J/mol×K | [294.00; 298.15] |
|
| Cp,liquid | 154.30 | J/mol×K | 294.00 | NIST |
| Cp,liquid | 154.87 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 154.00 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 155.31 | J/mol×K | 298.15 | NIST |
| η | [0.0001949; 0.0027701] | Pa×s | [144.35; 310.48] |
|
| η | 0.0027701 | Pa×s | 144.35 | Joback Calculated Property |
| η | 0.0012467 | Pa×s | 172.04 | Joback Calculated Property |
| η | 0.0007001 | Pa×s | 199.73 | Joback Calculated Property |
| η | 0.0004525 | Pa×s | 227.42 | Joback Calculated Property |
| η | 0.0003215 | Pa×s | 255.10 | Joback Calculated Property |
| η | 0.0002442 | Pa×s | 282.79 | Joback Calculated Property |
| η | 0.0001949 | Pa×s | 310.48 | Joback Calculated Property |
| ΔfusH | [5.81; 5.94] | kJ/mol | [107.80; 108.02] |
|
| ΔfusH | 5.88 | kJ/mol | 107.80 | NIST |
| ΔfusH | 5.81 | kJ/mol | 107.90 | NIST |
| ΔfusH | 5.81 | kJ/mol | 107.90 | NIST |
| ΔfusH | 5.81 | kJ/mol | 107.90 | NIST |
| ΔfusH | 5.81 | kJ/mol | 107.90 | NIST |
| ΔfusH | 5.94 | kJ/mol | 108.02 | NIST |
| ΔvapH | [25.20; 29.10] | kJ/mol | [264.50; 340.50] |
|
| ΔvapH | 29.10 | kJ/mol | 264.50 | NIST |
| ΔvapH | 26.20 ± 0.10 | kJ/mol | 284.00 | NIST |
| ΔvapH | 26.30 | kJ/mol | 290.50 | NIST |
| ΔvapH | 26.70 | kJ/mol | 295.00 | NIST |
| ΔvapH | 25.20 ± 0.10 | kJ/mol | 303.00 | NIST |
| ΔvapH | 25.20 | kJ/mol | 303.10 | NIST |
| ΔvapH | 26.90 | kJ/mol | 303.50 | NIST |
| ΔvapH | 25.20 | kJ/mol | 305.80 | KDB |
| ΔvapH | 25.70 | kJ/mol | 340.50 | NIST |
| n0 | 1.36835 | 298.15 | KDB | |
| ρl | 640.00 | kg/m3 | 293.00 | KDB |
| ΔfusS | [53.82; 55.00] | J/mol×K | [107.80; 108.02] |
|
| ΔfusS | 54.56 | J/mol×K | 107.80 | NIST |
| ΔfusS | 53.82 | J/mol×K | 107.90 | NIST |
| ΔfusS | 53.82 | J/mol×K | 107.90 | NIST |
| ΔfusS | 55.00 | J/mol×K | 107.90 | NIST |
| ΔfusS | 54.97 | J/mol×K | 108.02 | NIST |
| γ | 0.02 | N/m | 298.20 | KDB |
| λ | [0.11; 0.13] | W/m×K | [257.36; 301.75] |
|
| λ | 0.13 | W/m×K | 257.36 | Thermal... |
| λ | 0.13 | W/m×K | 257.67 | Thermal... |
| λ | 0.13 | W/m×K | 257.93 | Thermal... |
| λ | 0.12 | W/m×K | 276.47 | Thermal... |
| λ | 0.12 | W/m×K | 276.82 | Thermal... |
| λ | 0.12 | W/m×K | 277.07 | Thermal... |
| λ | 0.11 | W/m×K | 294.04 | Thermal... |
| λ | 0.11 | W/m×K | 294.42 | Thermal... |
| λ | 0.11 | W/m×K | 294.66 | Thermal... |
| λ | 0.11 | W/m×K | 301.07 | Thermal... |
| λ | 0.11 | W/m×K | 301.46 | Thermal... |
| λ | 0.11 | W/m×K | 301.75 | Thermal... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.48 | 100.00 | 650.3 |
| 283.48 | 500.00 | 650.8 |
| 283.48 | 1000.00 | 651.6 |
| 283.48 | 3000.00 | 654.0 |
| 283.49 | 5000.00 | 656.3 |
| 283.49 | 10000.00 | 661.8 |
| 283.49 | 15000.00 | 666.9 |
| 283.49 | 20000.00 | 671.7 |
| 283.49 | 25000.00 | 676.2 |
| 283.49 | 30000.00 | 680.4 |
| 283.49 | 35000.00 | 684.5 |
| 283.49 | 40000.00 | 688.4 |
| 283.49 | 45000.00 | 692.1 |
| 283.49 | 50000.00 | 695.7 |
| 283.49 | 55000.00 | 699.1 |
| 283.49 | 60000.00 | 702.5 |
| 283.48 | 70000.00 | 708.8 |
| 283.48 | 80000.00 | 714.8 |
| 283.49 | 90000.00 | 720.4 |
| 283.49 | 100000.00 | 725.7 |
| 293.42 | 100.00 | 640.1 |
| 293.42 | 500.00 | 640.7 |
| 293.42 | 1000.00 | 641.4 |
| 293.42 | 3000.00 | 644.0 |
| 293.42 | 5000.00 | 646.5 |
| 293.42 | 10000.00 | 652.4 |
| 293.43 | 15000.00 | 657.9 |
| 293.43 | 20000.00 | 663.0 |
| 293.43 | 25000.00 | 667.8 |
| 293.44 | 30000.00 | 672.3 |
| 293.43 | 35000.00 | 676.7 |
| 293.42 | 40000.00 | 680.8 |
| 293.43 | 45000.00 | 684.7 |
| 293.43 | 50000.00 | 688.4 |
| 293.42 | 55000.00 | 692.0 |
| 293.42 | 60000.00 | 695.5 |
| 293.42 | 70000.00 | 702.2 |
| 293.42 | 80000.00 | 708.3 |
| 293.42 | 90000.00 | 714.1 |
| 293.42 | 100000.00 | 719.6 |
| 303.33 | 100.00 | 629.8 |
| 303.33 | 1000.00 | 631.1 |
| 303.33 | 3000.00 | 634.0 |
| 303.34 | 5000.00 | 636.7 |
| 303.34 | 10000.00 | 643.1 |
| 303.34 | 15000.00 | 649.0 |
| 303.34 | 20000.00 | 654.5 |
| 303.34 | 25000.00 | 659.6 |
| 303.34 | 30000.00 | 664.4 |
| 303.33 | 35000.00 | 668.9 |
| 303.34 | 40000.00 | 673.2 |
| 303.34 | 45000.00 | 677.3 |
| 303.34 | 50000.00 | 681.2 |
| 303.35 | 55000.00 | 685.0 |
| 303.35 | 60000.00 | 688.6 |
| 303.35 | 70000.00 | 695.6 |
| 303.34 | 80000.00 | 702.0 |
| 303.34 | 90000.00 | 707.9 |
| 303.35 | 100000.00 | 713.6 |
| 313.27 | 500.00 | 620.4 |
| 313.28 | 1000.00 | 621.3 |
| 313.27 | 3000.00 | 624.5 |
| 313.27 | 5000.00 | 627.5 |
| 313.27 | 10000.00 | 634.4 |
| 313.28 | 15000.00 | 640.8 |
| 313.28 | 20000.00 | 646.7 |
| 313.28 | 25000.00 | 652.1 |
| 313.28 | 30000.00 | 657.2 |
| 313.29 | 35000.00 | 661.9 |
| 313.29 | 40000.00 | 666.6 |
| 313.28 | 45000.00 | 670.8 |
| 313.28 | 50000.00 | 674.9 |
| 313.29 | 55000.00 | 678.8 |
| 313.29 | 60000.00 | 682.6 |
| 313.28 | 70000.00 | 689.9 |
| 313.29 | 80000.00 | 696.4 |
| 313.29 | 90000.00 | 702.6 |
| 313.29 | 100000.00 | 708.4 |
| 323.18 | 500.00 | 608.6 |
| 323.18 | 1000.00 | 609.3 |
| 323.18 | 3000.00 | 612.8 |
| 323.18 | 5000.00 | 616.1 |
| 323.19 | 10000.00 | 623.7 |
| 323.19 | 15000.00 | 630.6 |
| 323.19 | 20000.00 | 636.9 |
| 323.19 | 25000.00 | 642.7 |
| 323.19 | 30000.00 | 648.1 |
| 323.19 | 35000.00 | 653.1 |
| 323.19 | 40000.00 | 657.9 |
| 323.19 | 45000.00 | 662.4 |
| 323.19 | 50000.00 | 666.7 |
| 323.19 | 55000.00 | 670.8 |
| 323.19 | 60000.00 | 674.7 |
| 323.19 | 70000.00 | 682.2 |
| 323.19 | 80000.00 | 689.1 |
| 323.19 | 90000.00 | 695.4 |
| 323.19 | 100000.00 | 701.5 |
| 333.04 | 500.00 | 597.2 |
| 333.04 | 1000.00 | 598.1 |
| 333.04 | 3000.00 | 601.9 |
| 333.04 | 5000.00 | 605.6 |
| 333.04 | 10000.00 | 613.9 |
| 333.05 | 15000.00 | 621.4 |
| 333.05 | 20000.00 | 628.1 |
| 333.05 | 25000.00 | 634.3 |
| 333.05 | 30000.00 | 640.0 |
| 333.05 | 35000.00 | 645.3 |
| 333.05 | 40000.00 | 650.4 |
| 333.05 | 45000.00 | 655.1 |
| 333.05 | 50000.00 | 659.6 |
| 333.05 | 55000.00 | 663.9 |
| 333.05 | 60000.00 | 668.0 |
| 333.05 | 70000.00 | 675.8 |
| 333.06 | 80000.00 | 683.0 |
| 333.06 | 90000.00 | 689.6 |
| 333.05 | 100000.00 | 695.8 |
| 342.94 | 500.00 | 585.8 |
| 342.94 | 1000.00 | 586.8 |
| 342.95 | 3000.00 | 591.2 |
| 342.95 | 5000.00 | 595.3 |
| 342.95 | 10000.00 | 604.4 |
| 342.96 | 15000.00 | 612.5 |
| 342.96 | 20000.00 | 619.8 |
| 342.96 | 25000.00 | 626.3 |
| 342.96 | 30000.00 | 632.4 |
| 342.96 | 35000.00 | 638.1 |
| 342.96 | 40000.00 | 643.4 |
| 342.96 | 45000.00 | 648.4 |
| 342.96 | 50000.00 | 653.0 |
| 342.96 | 55000.00 | 657.5 |
| 342.96 | 60000.00 | 661.8 |
| 342.95 | 70000.00 | 669.9 |
| 342.95 | 80000.00 | 677.2 |
| 342.94 | 90000.00 | 684.0 |
| 342.95 | 100000.00 | 690.4 |
| 352.82 | 500.00 | 574.2 |
| 352.82 | 1000.00 | 575.6 |
| 352.82 | 3000.00 | 580.5 |
| 352.82 | 5000.00 | 585.1 |
| 352.82 | 10000.00 | 595.2 |
| 352.83 | 15000.00 | 603.9 |
| 352.83 | 20000.00 | 611.7 |
| 352.83 | 25000.00 | 618.7 |
| 352.83 | 30000.00 | 625.2 |
| 352.83 | 35000.00 | 631.2 |
| 352.83 | 40000.00 | 636.7 |
| 352.83 | 45000.00 | 641.9 |
| 352.83 | 50000.00 | 646.9 |
| 352.83 | 55000.00 | 651.5 |
| 352.84 | 60000.00 | 655.9 |
| 352.83 | 70000.00 | 664.3 |
| 352.83 | 80000.00 | 671.9 |
| 352.83 | 90000.00 | 679.0 |
| 352.83 | 100000.00 | 685.6 |
| 362.67 | 500.00 | 560.5 |
| 362.67 | 1000.00 | 561.8 |
| 362.67 | 3000.00 | 567.4 |
| 362.68 | 5000.00 | 572.6 |
| 362.68 | 10000.00 | 583.8 |
| 362.68 | 15000.00 | 593.3 |
| 362.68 | 20000.00 | 601.7 |
| 362.68 | 25000.00 | 609.2 |
| 362.68 | 30000.00 | 616.1 |
| 362.68 | 35000.00 | 622.4 |
| 362.68 | 40000.00 | 628.2 |
| 362.68 | 45000.00 | 633.7 |
| 362.68 | 50000.00 | 638.9 |
| 362.68 | 55000.00 | 643.7 |
| 362.68 | 60000.00 | 648.3 |
| 362.68 | 70000.00 | 657.1 |
| 362.67 | 80000.00 | 664.9 |
| 362.68 | 90000.00 | 672.2 |
| 362.67 | 100000.00 | 679.0 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [217.89; 325.69] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.40675e+01 | |||
| Coefficient B | -2.58895e+03 | |||
| Coefficient C | -3.00140e+01 | |||
| Temperature range, min. | 217.89 | |||
| Temperature range, max. | 325.69 | |||
| Pvap | 1.33 | kPa | 217.89 | Calculated Property |
| Pvap | 3.04 | kPa | 229.87 | Calculated Property |
| Pvap | 6.33 | kPa | 241.85 | Calculated Property |
| Pvap | 12.18 | kPa | 253.82 | Calculated Property |
| Pvap | 21.92 | kPa | 265.80 | Calculated Property |
| Pvap | 37.27 | kPa | 277.78 | Calculated Property |
| Pvap | 60.35 | kPa | 289.76 | Calculated Property |
| Pvap | 93.65 | kPa | 301.73 | Calculated Property |
| Pvap | 140.02 | kPa | 313.71 | Calculated Property |
| Pvap | 202.65 | kPa | 325.69 | Calculated Property |
| Pvap | [9.78e-09; 3613.80] | kPa | [110.00; 464.78] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 8.33214e+01 | |||
| Coefficient B | -5.67565e+03 | |||
| Coefficient C | -1.07068e+01 | |||
| Coefficient D | 1.31421e-05 | |||
| Temperature range, min. | 110.00 | |||
| Temperature range, max. | 464.78 | |||
| Pvap | 9.78e-09 | kPa | 110.00 | Calculated Property |
| Pvap | 3.44e-04 | kPa | 149.42 | Calculated Property |
| Pvap | 0.09 | kPa | 188.84 | Calculated Property |
| Pvap | 2.71 | kPa | 228.26 | Calculated Property |
| Pvap | 24.81 | kPa | 267.68 | Calculated Property |
| Pvap | 116.72 | kPa | 307.10 | Calculated Property |
| Pvap | 367.91 | kPa | 346.52 | Calculated Property |
| Pvap | 903.88 | kPa | 385.94 | Calculated Property |
| Pvap | 1898.08 | kPa | 425.36 | Calculated Property |
| Pvap | 3613.80 | kPa | 464.78 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Pentene.
Mixtures
- 1-Pentene + Ethanol, 2,2'-oxybis-
- Triethylene glycol + 1-Pentene
- 1-Pentene + N-Formylmorpholine
- 2-Pyrrolidinone, 1-methyl- + 1-Pentene
- 1-Pentene + 1-Octadecanol
- 1-Pentene + 1-Eicosanol
- 1-Pentene + 1,8-Diaminooctane
- 1-Pentene + 1,10-Diaminodecane
- 1,12-Dodecanediamine + 1-Pentene
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid N-butyl-4-methylpyridinium tosylate using GLC at T = (328.15, 333.15, 338.15, and 343.15)K
- Measurement and prediction of activity coefficients at infinite dilution ( ), vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1,1-dialkyl-pyrrolidinium bis(trifluoromethylsulfonyl)imide using mod. UNIFAC (Dortmund)
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
- Activity coefficients at infinite dilution measurements for organic solutes and water in the 1-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium bis(trifluoromethylsulfonyl)-imide ionic liquids The cation influence
- Measurements of different thermodynamic properties of systems containing ionic liquids and correlation of these properties using modified UNIFAC (Dortmund)
- 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
- Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
- Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
- Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
- Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
- Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid trihexyltetradecylphosphonium-bis-(2,4,4-trimethylpentyl)- phosphinate using g.l.c. at T = (303.15, 308.15, 313.15, and 318.15) K
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid triethylsulphonium bis(trifluoromethylsulfonyl)imide
- Measurements of activity coefficients at infinite dilution of aliphatic and aromatic hydrocarbons, alcohols, thiophene, tetrahydrofuran, MTBE, and water in ionic liquid [BMIM][SCN] using GLC
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
- Activity coefficients at infinite dilution for solutes in the trioctylmethylammonium bis(trifluoromethylsulfonyl)imide ionic liquid using gas liquid chromatography
- Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
- Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyl(tetradecyl)phosphonium tetrafluoroborate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 373.15) K
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium hexafluoroantimonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid, methyl(trioctyl)ammonium thiosalicylate, [N1888][TS] by gas liquid chromatography at T = (303.15, 313.15, and 323.15) K
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
- 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
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium hexafluorophosphate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 363.15) K
- 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
- 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 of organic solutes in N-formylmorpholine and N-methylpyrrolidone from gas-liquid chromatography
- 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
- Activity coefficients at infinite dilution of organic solutes in diethylene glycol and triethylene glycol from gas-liquid chromatography
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography at T = (313.15, 333.15, 353.15 and 373.15) K
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
- The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
- Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium 2-(2-methoxyethoxy) ethylsulfate at T = (308.15, 313.15, 323.15 and 333.15) K using gas + liquid chromatography
- Use of water in aiding olefin/paraffin (liquid + liquid) extraction via complexation with a silver bis(trifluoromethylsulfonyl)imide salt
- 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 and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- 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
- Screening of environmental friendly ionic liquid as a solvent for the different types of separations problem: Insight from activity coefficients at infinite dilution measurement using (gas + liquid) chromatography technique
- 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
- Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
- Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
- 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
- Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
- Vapor Pressures and Vapor Liquid Critical Properties of Four Pentene Isomers
- Liquid Density of n-Pentene, n-Hexene, and n-Heptene at Temperatures from 283.15 to 363.15 K and Pressures up to 100 MPa
- 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 Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 5. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-butyl-imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using Gas-Liquid Chromatography
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 6. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-octyl-imidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- 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
- 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
- Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
- Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution by GLC in Alkanediamines as Stationary Phases
- Enhancing liquid-phase olefin-paraffin separations using novel silver-based ionic liquids
- Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid, Trihexyltetradecylphosphonium Bis(trifluoromethylsulfonyl) Imide, Using Gas-Liquid Chromatography at T ) (303.15, 308.15, 313.15, and 318.15) K
- Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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