- InChI
- InChI=1S/C5H10/c1-2-4-5-3-1/h1-5H2
- InChI Key
- RGSFGYAAUTVSQA-UHFFFAOYSA-N
- Formula
- C5H10
- SMILES
- C1CCCC1
- Molecular Weight1
- 70.13
- CAS
- 287-92-3
- Other Names
-
- PENTAMETHYLENE
- UN 1146
- 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,oc : Flash Point (Open Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- Rg : Radius of Gyration.
- 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).
- ΔsubH : Enthalpy of sublimation 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).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- ΔvapS : Entropy of vaporization at a given temperature (J/mol×K).
- 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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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.1960 | KDB | |
| Tig | 653.15 | K | KDB |
| AP | 289.950 | K | KDB |
| ΔcH°liquid | [-3291.40; -3290.90] | kJ/mol |
|
| ΔcH°liquid | -3291.40 ± 0.60 | kJ/mol | NIST |
| ΔcH°liquid | -3291.20 ± 1.30 | kJ/mol | NIST |
| ΔcH°liquid | -3290.90 ± 0.71 | kJ/mol | NIST |
| μ | 0.00 | debye | KDB |
| LFL | 1.10 | % in Air | KDB |
| UFL | 8.70 | % in Air | KDB |
| Tflash,oc | 266.48 | K | KDB |
| ΔfG° | 38.60 | kJ/mol | KDB |
| Rg | 3.1200 | KDB | |
| Δc,grossH | 3290.93 | kJ/mol | KDB |
| Δc,netH | 3070.889 | kJ/mol | KDB |
| ΔfH°gas | [-77.29; -76.40] | kJ/mol |
|
| ΔfH°gas | -77.29 | kJ/mol | KDB |
| ΔfH°gas | -76.40 ± 0.79 | kJ/mol | NIST |
| ΔfH°gas | -76.90 | kJ/mol | NIST |
| ΔfH°gas | -77.24 ± 0.75 | kJ/mol | NIST |
| ΔfH°liquid | [-105.90; -105.60] | kJ/mol |
|
| ΔfH°liquid | -105.60 ± 1.80 | kJ/mol | NIST |
| ΔfH°liquid | -105.90 ± 0.75 | kJ/mol | NIST |
| ΔfusH° | 1.57 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 27.29 | kJ/mol | Joback Calculated Property |
| IE | [9.83; 11.01] | eV |
|
| IE | 10.33 ± 0.15 | eV | NIST |
| IE | Outlier 9.83 ± 0.05 | eV | NIST |
| IE | 10.35 | eV | NIST |
| IE | 10.33 ± 0.15 | eV | NIST |
| IE | 10.30 ± 0.10 | eV | NIST |
| IE | 10.55 ± 0.03 | eV | NIST |
| IE | 10.54 ± 0.05 | eV | NIST |
| IE | 10.48 | eV | NIST |
| IE | 10.40 | eV | NIST |
| IE | 10.49 | eV | NIST |
| IE | 10.91 ± 0.07 | eV | NIST |
| IE | 10.50 ± 0.01 | eV | NIST |
| IE | 10.49 | eV | NIST |
| IE | 10.53 ± 0.05 | eV | NIST |
| IE | Outlier 11.01 | eV | NIST |
| IE | 10.70 ± 0.10 | eV | NIST |
| IE | 10.50 | eV | NIST |
| log10WS | [-2.64; -2.64] |
|
|
| log10WS | -2.64 | Aq. Sol... | |
| log10WS | -2.64 | Estimat... | |
| logPoct/wat | 1.950 | Crippen Calculated Property | |
| McVol | 70.450 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | [4430.00; 4514.03] | kPa |
|
| Pc | 4510.00 | kPa | KDB |
| Pc | 4510.00 ± 40.00 | kPa | NIST |
| Pc | 4508.00 ± 40.53 | kPa | NIST |
| Pc | 4430.00 ± 50.66 | kPa | NIST |
| Pc | 4514.03 ± 5.06 | kPa | NIST |
| ρc | [270.01; 270.01] | kg/m3 |
|
| ρc | 270.01 ± 2.81 | kg/m3 | NIST |
| ρc | 270.01 ± 4.21 | kg/m3 | NIST |
| ρc | 270.01 ± 2.10 | kg/m3 | NIST |
| Inp | [520.00; 599.00] |
|
|
| Inp | 572.00 | NIST | |
| Inp | 587.00 | NIST | |
| Inp | 587.70 | NIST | |
| Inp | 558.00 | NIST | |
| Inp | 572.00 | NIST | |
| Inp | 573.00 | NIST | |
| Inp | 574.30 | NIST | |
| Inp | 582.40 | NIST | |
| Inp | Outlier 591.00 | NIST | |
| Inp | 562.00 | NIST | |
| Inp | 567.80 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 568.30 | NIST | |
| Inp | 568.40 | NIST | |
| Inp | 562.60 | NIST | |
| Inp | 587.60 | NIST | |
| Inp | 588.00 | NIST | |
| Inp | 565.00 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 572.00 | NIST | |
| Inp | 566.20 | NIST | |
| Inp | 587.90 | NIST | |
| Inp | 566.50 | NIST | |
| Inp | 565.60 | NIST | |
| Inp | 566.10 | NIST | |
| Inp | 569.40 | NIST | |
| Inp | 569.90 | NIST | |
| Inp | 574.50 | NIST | |
| Inp | 563.00 | NIST | |
| Inp | 565.00 | NIST | |
| Inp | 566.00 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 572.00 | NIST | |
| Inp | 567.80 | NIST | |
| Inp | 568.30 | NIST | |
| Inp | 577.00 | NIST | |
| Inp | 566.00 | NIST | |
| Inp | 582.00 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 567.00 | NIST | |
| Inp | 566.00 | NIST | |
| Inp | 565.00 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 568.80 | NIST | |
| Inp | 565.55 | NIST | |
| Inp | 563.30 | NIST | |
| Inp | 575.90 | NIST | |
| Inp | 573.00 | NIST | |
| Inp | 576.00 | NIST | |
| Inp | 567.00 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 566.00 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 573.00 | NIST | |
| Inp | 588.00 | NIST | |
| Inp | 566.00 | NIST | |
| Inp | 567.00 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 572.00 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 571.00 | NIST | |
| Inp | 573.00 | NIST | |
| Inp | 574.00 | NIST | |
| Inp | 566.30 | NIST | |
| Inp | 571.00 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 572.00 | NIST | |
| Inp | 563.00 | NIST | |
| Inp | 566.00 | NIST | |
| Inp | 569.00 | NIST | |
| Inp | 572.00 | NIST | |
| Inp | 562.00 | NIST | |
| Inp | 563.00 | NIST | |
| Inp | 564.00 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 578.00 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 562.00 | NIST | |
| Inp | Outlier 599.00 | NIST | |
| Inp | 587.00 | NIST | |
| Inp | 571.00 | NIST | |
| Inp | 557.00 | NIST | |
| Inp | 576.00 | NIST | |
| Inp | 566.50 | NIST | |
| Inp | 563.00 | NIST | |
| Inp | 553.70 | NIST | |
| Inp | 580.29 | NIST | |
| Inp | 563.20 | NIST | |
| Inp | 556.60 | NIST | |
| Inp | 554.33 | NIST | |
| Inp | 554.33 | NIST | |
| Inp | 554.13 | NIST | |
| Inp | 554.24 | NIST | |
| Inp | 554.00 | NIST | |
| Inp | 557.00 | NIST | |
| Inp | 559.00 | NIST | |
| Inp | 564.00 | NIST | |
| Inp | 564.00 | NIST | |
| Inp | 565.00 | NIST | |
| Inp | 571.00 | NIST | |
| Inp | 566.00 | NIST | |
| Inp | 566.00 | NIST | |
| Inp | 569.00 | NIST | |
| Inp | Outlier 520.00 | NIST | |
| Inp | Outlier 524.00 | NIST | |
| Inp | 560.00 | NIST | |
| Inp | 560.00 | NIST | |
| Inp | 564.00 | NIST | |
| Inp | 562.00 | NIST | |
| Inp | 554.50 | NIST | |
| Inp | 564.00 | NIST | |
| Inp | 554.00 | NIST | |
| Inp | Outlier 527.00 | NIST | |
| Inp | 562.00 | NIST | |
| Inp | 563.00 | NIST | |
| Inp | 587.00 | NIST | |
| Inp | 566.00 | NIST | |
| Inp | 587.00 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 564.00 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 560.00 | NIST | |
| Inp | 558.00 | NIST | |
| Inp | Outlier 533.00 | NIST | |
| Inp | 572.00 | NIST | |
| Inp | 557.00 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 577.00 | NIST | |
| Inp | 573.00 | NIST | |
| Inp | 564.00 | NIST | |
| Inp | 573.00 | NIST | |
| Inp | 564.00 | NIST | |
| Inp | 559.00 | NIST | |
| Inp | 553.70 | NIST | |
| Inp | 554.33 | NIST | |
| Inp | 566.50 | NIST | |
| I | [694.00; 720.00] |
|
|
| I | 694.00 | NIST | |
| I | 700.00 | NIST | |
| I | 710.00 | NIST | |
| I | 698.00 | NIST | |
| I | 700.00 | NIST | |
| I | 720.00 | NIST | |
| I | 694.00 | NIST | |
| I | 720.00 | NIST | |
| S°liquid | [204.14; 206.70] | J/mol×K |
|
| S°liquid | 204.14 | J/mol×K | NIST |
| S°liquid | 204.47 | J/mol×K | NIST |
| S°liquid | 206.70 | J/mol×K | NIST |
| Tboil | 322.40 | K | KDB |
| Tc | [511.60; 511.75] | K |
|
| Tc | 511.70 | K | KDB |
| Tc | 511.70 ± 0.20 | K | NIST |
| Tc | 511.60 | K | NIST |
| Tc | 511.70 ± 0.20 | K | NIST |
| Tc | 511.60 ± 0.15 | K | NIST |
| Tc | 511.75 ± 0.05 | K | NIST |
| Tfus | [176.64; 180.05] | K |
|
| Tfus | 179.30 | K | KDB |
| Tfus | 179.20 | K | Aq. Sol... |
| Tfus | Outlier 176.64 ± 0.30 | K | NIST |
| Tfus | 179.60 ± 0.30 | K | NIST |
| Tfus | 179.55 ± 0.30 | K | NIST |
| Tfus | Outlier 177.06 ± 0.20 | K | NIST |
| Tfus | 179.25 ± 0.40 | K | NIST |
| Tfus | 179.26 ± 0.40 | K | NIST |
| Tfus | 179.69 ± 0.10 | K | NIST |
| Tfus | 179.26 ± 0.07 | K | NIST |
| Tfus | 179.38 ± 0.05 | K | NIST |
| Tfus | 179.25 ± 0.06 | K | NIST |
| Tfus | 179.26 ± 0.05 | K | NIST |
| Tfus | 179.28 ± 0.04 | K | NIST |
| Tfus | 179.35 ± 0.20 | K | NIST |
| Tfus | 179.35 ± 0.20 | K | NIST |
| Tfus | 179.23 ± 0.01 | K | NIST |
| Tfus | 179.23 ± 0.05 | K | NIST |
| Tfus | 179.25 ± 0.07 | K | NIST |
| Tfus | 179.38 ± 0.05 | K | NIST |
| Tfus | 179.23 ± 0.40 | K | NIST |
| Tfus | 179.68 ± 0.30 | K | NIST |
| Tfus | 179.31 ± 0.20 | K | NIST |
| Tfus | 178.85 ± 0.30 | K | NIST |
| Tfus | 178.85 ± 0.30 | K | NIST |
| Tfus | 178.85 ± 0.20 | K | NIST |
| Tfus | 178.85 ± 0.30 | K | NIST |
| Tfus | 178.15 ± 0.50 | K | NIST |
| Tfus | 178.35 ± 0.50 | K | NIST |
| Tfus | 180.05 ± 0.50 | K | NIST |
| Ttriple | [179.00; 179.71] | K |
|
| Ttriple | 179.71 ± 0.05 | K | NIST |
| Ttriple | 179.71 ± 0.01 | K | NIST |
| Ttriple | 179.69 ± 0.08 | K | NIST |
| Ttriple | 179.00 ± 0.20 | K | NIST |
| Vc | [0.259; 0.259] | m3/kmol |
|
| Vc | 0.259 | m3/kmol | KDB |
| Vc | 0.259 | m3/kmol | NIST |
| Zc | 0.2745520 | KDB | |
| Zra | 0.27 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [93.96; 160.10] | J/mol×K | [329.05; 539.00] |
|
| Cp,gas | 93.96 ± 0.19 | J/mol×K | 329.05 | NIST |
| Cp,gas | 102.01 ± 0.84 | J/mol×K | 353.00 | NIST |
| Cp,gas | 108.16 ± 0.84 | J/mol×K | 372.00 | NIST |
| Cp,gas | 117.30 ± 1.30 | J/mol×K | 395.00 | NIST |
| Cp,gas | 117.09 ± 0.23 | J/mol×K | 395.05 | NIST |
| Cp,gas | 126.30 ± 1.30 | J/mol×K | 424.00 | NIST |
| Cp,gas | 138.70 ± 1.30 | J/mol×K | 463.00 | NIST |
| Cp,gas | 139.47 ± 0.28 | J/mol×K | 463.10 | NIST |
| Cp,gas | 150.70 ± 1.70 | J/mol×K | 503.00 | NIST |
| Cp,gas | 160.10 ± 1.70 | J/mol×K | 539.00 | NIST |
| Cp,liquid | [125.90; 128.83] | J/mol×K | [293.15; 300.00] |
|
| Cp,liquid | 126.17 | J/mol×K | 293.15 | NIST |
| Cp,liquid | 125.90 | J/mol×K | 293.70 | NIST |
| Cp,liquid | 126.74 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 126.87 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 127.28 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 126.78 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 128.83 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 127.44 | J/mol×K | 300.00 | NIST |
| η | [0.0002502; 0.0007268] | Pa×s | [253.15; 353.15] |
|
| η | 0.0007268 | Pa×s | 253.15 | Saturat... |
| η | 0.0006786 | Pa×s | 258.15 | Saturat... |
| η | 0.0006347 | Pa×s | 263.15 | Saturat... |
| η | 0.0005930 | Pa×s | 268.15 | Saturat... |
| η | 0.0005567 | Pa×s | 273.15 | Saturat... |
| η | 0.0005224 | Pa×s | 278.15 | Saturat... |
| η | 0.0005230 | Pa×s | 278.15 | Tempera... |
| η | 0.0004932 | Pa×s | 283.15 | Tempera... |
| η | 0.0004922 | Pa×s | 283.15 | Saturat... |
| η | 0.0004646 | Pa×s | 288.15 | Saturat... |
| η | 0.0004657 | Pa×s | 288.15 | Tempera... |
| η | 0.0004390 | Pa×s | 293.15 | Dynamic... |
| η | 0.0004380 | Pa×s | 293.15 | Density... |
| η | 0.0004390 | Pa×s | 293.15 | Viscosi... |
| η | 0.0004380 | Pa×s | 293.15 | Viscosi... |
| η | 0.0004405 | Pa×s | 293.15 | Tempera... |
| η | 0.0004382 | Pa×s | 293.15 | Saturat... |
| η | 0.0004390 | Pa×s | 293.15 | Dynamic... |
| η | 0.0004148 | Pa×s | 298.15 | Saturat... |
| η | 0.0004173 | Pa×s | 298.15 | Tempera... |
| η | 0.0004160 | Pa×s | 298.15 | Dynamic... |
| η | 0.0004160 | Pa×s | 298.15 | Viscosi... |
| η | 0.0004160 | Pa×s | 298.15 | Dynamic... |
| η | 0.0004150 | Pa×s | 298.15 | Density... |
| η | 0.0003940 | Pa×s | 303.15 | Viscosi... |
| η | 0.0003940 | Pa×s | 303.15 | Dynamic... |
| η | 0.0003923 | Pa×s | 303.15 | Saturat... |
| η | 0.0003940 | Pa×s | 303.15 | Dynamic... |
| η | 0.0003940 | Pa×s | 303.15 | Density... |
| η | 0.0003714 | Pa×s | 308.15 | Saturat... |
| η | 0.0003740 | Pa×s | 308.15 | Density... |
| η | 0.0003550 | Pa×s | 313.15 | Density... |
| η | 0.0003521 | Pa×s | 313.15 | Saturat... |
| η | 0.0003350 | Pa×s | 318.15 | Saturat... |
| η | 0.0003190 | Pa×s | 323.15 | Saturat... |
| η | 0.0003048 | Pa×s | 328.15 | Saturat... |
| η | 0.0002912 | Pa×s | 333.15 | Saturat... |
| η | 0.0002793 | Pa×s | 338.15 | Saturat... |
| η | 0.0002690 | Pa×s | 343.15 | Saturat... |
| η | 0.0002590 | Pa×s | 348.15 | Saturat... |
| η | 0.0002502 | Pa×s | 353.15 | Saturat... |
| ΔfusH | [0.34; 4.90] | kJ/mol | [122.00; 179.70] |
|
| ΔfusH | 4.90 | kJ/mol | 122.00 | NIST |
| ΔfusH | 0.34 | kJ/mol | 138.00 | NIST |
| ΔfusH | 0.60 | kJ/mol | 179.70 | NIST |
| ΔfusH | 0.60 | kJ/mol | 179.70 | NIST |
| ΔsubH | 42.60 | kJ/mol | 122.00 | NIST |
| ΔvapH | [27.20; 29.21] | kJ/mol | [298.15; 481.50] |
|
| ΔvapH | 29.21 | kJ/mol | 298.15 | NIST |
| ΔvapH | 29.20 | kJ/mol | 305.50 | NIST |
| ΔvapH | 29.00 | kJ/mol | 306.00 | NIST |
| ΔvapH | 27.90 ± 0.10 | kJ/mol | 310.00 | NIST |
| ΔvapH | 27.30 ± 0.10 | kJ/mol | 322.00 | NIST |
| ΔvapH | 27.30 | kJ/mol | 322.40 | KDB |
| ΔvapH | 27.30 | kJ/mol | 322.40 | NIST |
| ΔvapH | 27.40 | kJ/mol | 323.00 | NIST |
| ΔvapH | 28.00 | kJ/mol | 353.00 | NIST |
| ΔvapH | 27.20 | kJ/mol | 418.00 | NIST |
| ΔvapH | 27.50 | kJ/mol | 481.50 | NIST |
| n0 | [1.39456; 1.40640] | [293.15; 313.15] |
|
|
| n0 | 1.40640 | 293.15 | Isobari... | |
| n0 | 1.40363 | 298.15 | KDB | |
| n0 | 1.40292 | 298.15 | Density... | |
| n0 | 1.39456 | 313.15 | Density... | |
| ρl | [726.57; 762.30] | kg/m3 | [273.15; 308.15] |
|
| ρl | 762.30 | kg/m3 | 273.15 | Phase e... |
| ρl | 757.50 | kg/m3 | 278.15 | Phase e... |
| ρl | 752.60 | kg/m3 | 283.15 | Phase e... |
| ρl | 747.70 | kg/m3 | 288.15 | Phase e... |
| ρl | 745.00 | kg/m3 | 293.00 | KDB |
| ρl | 742.80 | kg/m3 | 293.15 | Phase e... |
| ρl | 745.70 | kg/m3 | 293.15 | Correla... |
| ρl | 739.74 | kg/m3 | 298.15 | Experim... |
| ρl | 737.80 | kg/m3 | 298.15 | Phase e... |
| ρl | 733.63 | kg/m3 | 298.15 | Densiti... |
| ρl | 740.00 | kg/m3 | 298.15 | Density... |
| ρl | 726.57 | kg/m3 | 308.15 | Densiti... |
| ΔfusS | [2.49; 40.13] | J/mol×K | [122.00; 179.70] |
|
| ΔfusS | 40.13 | J/mol×K | 122.00 | NIST |
| ΔfusS | 2.49 | J/mol×K | 138.00 | NIST |
| ΔfusS | 3.35 | J/mol×K | 179.70 | NIST |
| csound,fluid | [1129.90; 1283.50] | m/s | [283.15; 313.15] |
|
| csound,fluid | 1283.50 | m/s | 283.15 | Speeds ... |
| csound,fluid | 1206.60 | m/s | 298.15 | Speeds ... |
| csound,fluid | 1129.90 | m/s | 313.15 | Speeds ... |
| γ | [0.02; 0.02] | N/m | [283.15; 313.15] |
|
| γ | 0.02 | N/m | 283.15 | Thermop... |
| γ | 0.02 | N/m | 293.20 | KDB |
| γ | 0.02 | N/m | 298.15 | Thermop... |
| γ | 0.02 | N/m | 313.15 | Thermop... |
| ΔvapS | 97.98 | J/mol×K | 298.15 | NIST |
| λ | [0.12; 0.14] | W/m×K | [257.08; 316.54] |
|
| λ | 0.14 | W/m×K | 257.08 | Thermal... |
| λ | 0.14 | W/m×K | 257.27 | Thermal... |
| λ | 0.14 | W/m×K | 257.40 | Thermal... |
| λ | 0.13 | W/m×K | 276.13 | Thermal... |
| λ | 0.13 | W/m×K | 276.33 | Thermal... |
| λ | 0.13 | W/m×K | 276.47 | Thermal... |
| λ | 0.13 | W/m×K | 293.63 | Thermal... |
| λ | 0.13 | W/m×K | 293.83 | Thermal... |
| λ | 0.13 | W/m×K | 293.97 | Thermal... |
| λ | 0.13 | W/m×K | 300.67 | Thermal... |
| λ | 0.13 | W/m×K | 300.87 | Thermal... |
| λ | 0.13 | W/m×K | 301.01 | Thermal... |
| λ | 0.12 | W/m×K | 316.21 | Thermal... |
| λ | 0.12 | W/m×K | 316.40 | Thermal... |
| λ | 0.12 | W/m×K | 316.54 | Thermal... |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 273.15 | 100.00 | 0.0006 |
| 273.15 | 10000.00 | 0.0006 |
| 273.15 | 30000.00 | 0.0007 |
| 273.15 | 40000.00 | 0.0008 |
| 293.15 | 100.00 | 0.0004 |
| 293.15 | 10000.00 | 0.0005 |
| 293.15 | 30000.00 | 0.0006 |
| 293.15 | 40000.00 | 0.0006 |
| 298.15 | 100.00 | 0.0004 |
| 298.15 | 10000.00 | 0.0005 |
| 298.15 | 30000.00 | 0.0005 |
| 298.15 | 40000.00 | 0.0006 |
| 313.15 | 10000.00 | 0.0004 |
| 313.15 | 30000.00 | 0.0005 |
| 313.15 | 45000.00 | 0.0005 |
| 333.15 | 10000.00 | 0.0003 |
| 333.15 | 30000.00 | 0.0004 |
| 333.15 | 45000.00 | 0.0004 |
| 353.15 | 15000.00 | 0.0003 |
| 353.15 | 30000.00 | 0.0003 |
| 353.15 | 45000.00 | 0.0004 |
| Reference | ||
Speed of sound, m/s
Operational condition: Frequency, MHz = 8 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Speed of sound, m/s - Liquid |
| 258.15 | 100.00 | 1419.058 |
| 258.15 | 5072.00 | 1446.07 |
| 258.15 | 10244.00 | 1473.008 |
| 258.15 | 15262.00 | 1498.119 |
| 258.15 | 20158.00 | 1521.653 |
| 258.15 | 25083.00 | 1544.511 |
| 258.15 | 30141.00 | 1567.131 |
| 273.15 | 100.00 | 1336.626 |
| 273.15 | 5169.00 | 1366.736 |
| 273.15 | 10059.00 | 1394.32 |
| 273.15 | 15219.00 | 1422.015 |
| 273.15 | 20251.00 | 1447.913 |
| 273.15 | 25184.00 | 1472.273 |
| 273.15 | 30227.00 | 1496.252 |
| 293.15 | 105.00 | 1230.093 |
| 293.15 | 5059.00 | 1262.962 |
| 293.15 | 10088.00 | 1294.375 |
| 293.15 | 15198.00 | 1324.591 |
| 293.15 | 20121.00 | 1352.283 |
| 293.15 | 25192.00 | 1379.573 |
| 293.15 | 30134.00 | 1404.98 |
| 313.15 | 107.00 | 1126.831 |
| 313.15 | 5113.00 | 1164.014 |
| 313.15 | 10058.00 | 1198.273 |
| 313.15 | 15132.00 | 1231.306 |
| 313.15 | 20097.00 | 1261.807 |
| 313.15 | 25098.00 | 1290.997 |
| 313.15 | 30162.00 | 1319.175 |
| 333.15 | 149.00 | 1026.636 |
| 333.15 | 5035.00 | 1067.634 |
| 333.15 | 10139.00 | 1106.967 |
| 333.15 | 15108.00 | 1142.542 |
| 333.15 | 20130.00 | 1176.238 |
| 333.15 | 25152.00 | 1207.969 |
| 333.15 | 30170.00 | 1238.041 |
| 353.15 | 261.00 | 929.399 |
| 353.15 | 5019.00 | 974.633 |
| 353.15 | 10069.00 | 1018.218 |
| 353.15 | 15107.00 | 1058.051 |
| 353.15 | 20063.00 | 1094.384 |
| 353.15 | 25009.00 | 1128.301 |
| 353.15 | 30157.00 | 1161.49 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [232.47; 344.93] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.42014e+01 | |||
| Coefficient B | -2.76893e+03 | |||
| Coefficient C | -3.34600e+01 | |||
| Temperature range, min. | 232.47 | |||
| Temperature range, max. | 344.93 | |||
| Pvap | 1.33 | kPa | 232.47 | Calculated Property |
| Pvap | 3.03 | kPa | 244.97 | Calculated Property |
| Pvap | 6.30 | kPa | 257.46 | Calculated Property |
| Pvap | 12.10 | kPa | 269.96 | Calculated Property |
| Pvap | 21.78 | kPa | 282.45 | Calculated Property |
| Pvap | 37.05 | kPa | 294.95 | Calculated Property |
| Pvap | 60.05 | kPa | 307.44 | Calculated Property |
| Pvap | 93.32 | kPa | 319.94 | Calculated Property |
| Pvap | 139.76 | kPa | 332.43 | Calculated Property |
| Pvap | 202.65 | kPa | 344.93 | Calculated Property |
| Pvap | [8.36e-03; 4529.34] | kPa | [179.28; 511.76] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.44024e+01 | |||
| Coefficient B | -5.38926e+03 | |||
| Coefficient C | -7.58416e+00 | |||
| Coefficient D | 7.08554e-06 | |||
| Temperature range, min. | 179.28 | |||
| Temperature range, max. | 511.76 | |||
| Pvap | 8.36e-03 | kPa | 179.28 | Calculated Property |
| Pvap | 0.38 | kPa | 216.22 | Calculated Property |
| Pvap | 4.94 | kPa | 253.16 | Calculated Property |
| Pvap | 30.50 | kPa | 290.11 | Calculated Property |
| Pvap | 117.76 | kPa | 327.05 | Calculated Property |
| Pvap | 333.73 | kPa | 363.99 | Calculated Property |
| Pvap | 766.37 | kPa | 400.93 | Calculated Property |
| Pvap | 1520.52 | kPa | 437.88 | Calculated Property |
| Pvap | 2721.67 | kPa | 474.82 | Calculated Property |
| Pvap | 4529.34 | kPa | 511.76 | Calculated Property |
Similar Compounds
Find more compounds similar to Cyclopentane.
Mixtures
- 1,3-Dioxolane + Cyclopentane
- Cyclopentane + 1,4-Dioxane
- Cyclopentane + Ethanol
- 1-Propanol + Cyclopentane
- Cyclopentane + 1-Butanol
- Cyclopentane + Ethanol, 2,2'-oxybis-
- Cyclopentane + Triethylene glycol
- 1,2-Ethanediol + Cyclopentane
- Cyclopentane + Cycloheptane
- Cyclopentane + Hexadecane + Cycloheptane
- Cyclopentane + Pentane
- 2-Butene, 2-methyl- + Cyclopentane
- Cyclopentane + Cyclopentene
- Isoprene + Cyclopentane
- Cyclopentane + Propanoic acid + Water
- Cyclopentane + Water
- Cyclopentane + Carbonic acid, dimethyl ester
- Diethyl carbonate + Cyclopentane
- Cyclopentane + Acetone
- 2-Butanone + Cyclopentane
Find more mixtures with Cyclopentane.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Speeds of Sound and Isentropic Compressibilities for Binary Mixtures of a Cyclic Diether with a Cyclic Compound at Three Temperatures
- Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, trihexyl(tetradecyl)-phosphonium tris(pentafluoroethyl) trifluorophosphate, by gas liquid chromatography
- Experimental and predicted vapour liquid equilibrium of 1,4-dioxane with cycloalkanes and benzene
- Experimental liquid liquid equilibria of 1-methylimidazole with hydrocarbons and ethers
- Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, tributylmethylphosphonium methylsulphate by gas liquid chromatography
- 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
- 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
- On the behaviour of solutions of xenon in liquid cycloalkanes: Solubility of xenon in cyclopentane
- Phase equilibrium relations for binary mixed hydrate systemscomposed of carbon dioxide and cyclopentane derivatives
- 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
- Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
- Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
- New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
- Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
- The determination of activity coefficients at infinite dilution using g.l.c. for hydrocarbons in furfural at T = 278:15 K and T = 298:15 K
- Activity coefficients at infinite dilution for hydrocarbons in furfuryl alcohol at T=(278.15 and 298.15) K, determined by g.l.c.
- Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid 1-butyl-3-methyl-imidazolium 2-(2-methoxyethoxy) ethyl sulfate using g.l.c. at T = (298.15, 303.15, and 308.15) K
- Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid hexyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)-imide using g.l.c. at T = (298.15, 313.15, and 333.15) K
- 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)
- Measurement of activity coefficients at infinite dilution using polar and non-polar solutes in the ionic liquid 1-methyl-3-octyl-imidazolium diethyleneglycolmonomethylethersulfate at T = (288.15, 298.15, and 313.15) K
- Thermophysical study of 1,4-dioxane with cycloalkane mixtures
- Dynamic viscosities of binary mixtures of cycloalkanes with primary alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO interaction parameters
- Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
- Development of a Henry s constant correlation and solubility measurements of n-pentane, i-pentane, cyclopentane, n-hexane, and toluene in water
- 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
- Influence of temperature on the (liquid + liquid) equilibria of {3-methyl pentane + cyclopentane + methanol} ternary system at T = (293.15, 297.15, and 299.15) K
- 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 of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium trifluoromethanesulfonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
- Activity coefficients at infinite dilution for solutes in the trioctylmethylammonium bis(trifluoromethylsulfonyl)imide ionic liquid using gas liquid chromatography
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-octyl-3-methylimidazolium hexafluorophosphate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
- 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 solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
- 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
- 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 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
- Determination of infinite dilution activity coefficients using HS-SPME/GC/FID for hydrocarbons in furfural at temperatures of (298.15, 308.15, and 318.15) 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
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- 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 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
- 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
- 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
- Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-hexyl-1,4-diaza[2.2.2]bicyclooctanium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography
- 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 for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
- 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
- The effect of the naphthenic ring on the VLE of (carbon dioxide + alkane) mixtures
- 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
- 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
- Activity coefficients at infinite dilution of hydrocarbons in glycols: Experimental data and thermodynamic modeling with the GCA-EoS
- 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
- Excess Molar Volumes for Three and Four Component Mixtures Simulating the Binary Mixture (Cyclohexane+ Hexadecane)
- Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
- Isobaric Vapor Liquid Equilibrium for Nine Binary Systems of Cracking C5 Fraction at 250 kPa
- Correlation of Experimental Liquid Liquid Equilibrium Data for Ternary Systems Using NRTL and GMDH-Type Neural Network
- Activity Coefficients at Infinite Dilution of Various Solutes in Tetrapropylammonium Bromide + 1,6-Hexanediol Deep Eutectic Solvent
- Liquid-Liquid Equilibria for the Binary Systems of N-Formylmorpholine with Cycloalkanes
- Solubility of 1-Alkyl-3-methylimidazolium Hexafluorophosphate in Hydrocarbons
- Saturated Liquid Viscosity of Cyclopentane and Isopentane
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Hexyl-3-methylimidazolium Hexafluorophosphate from Gas-Liquid Chromatography
- Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid 1-Hexyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography at the Temperatures 298.15 K and 323.15 K
- Temperature and Density Dependence of the Viscosity of Cyclopentane
- Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
- Determination of Activity Coefficients at Infinite Dilution of Polar and Nonpolar Solutes in the Ionic Liquid 1-Ethyl-3-methyl- imidazolium Bis(trifluoromethylsulfonyl) Imidate Using Gas-Liquid Chromatography at the Temperature 303.15 K or 318.15 K
- Density, Viscosity, and Speed of Sound of Dialkyl Carbonates with Cyclopentane and Methyl Cyclohexane at Several Temperatures
- Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid 1-Butyl-3-methylimidazolium Octyl Sulfate Using Gas-Liquid Chromatography at a Temperature of 298.15 K, 313.15 K, or 328.15 K
- Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
- Viscosities, Densities, and Speed of Sound of the Cycloalkanes with Secondary Alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO Interaction Parameters
- Infinite Dilution Activity Coefficients for Trihexyltetradecyl Phosphonium Ionic Liquids: Measurements and COSMO-RS Prediction
- Measurement of the Viscosity of Liquid Cyclopentane Obtained with a Vibrating Wire Viscometer at Temperatures between (273 and 353) K and Pressures below 45 MPa
- 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
- Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
- Speed of Sound Measurements and a Fundamental Equation of State for Cyclopentane
- 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
- Densities and Excess Molar Volumes of Cyclopentane (1) + 1-Alkanol (2) Systems at (298.15 and 308.15) K
- Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes and Aromatic Compounds at T = 313.15 K
- Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K
- Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
- Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes with o-Xylene, m-Xylene, p-Xylene, and Mesitylene at T = (298.15 and 313.15) 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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