- InChI
- InChI=1S/C5H12/c1-3-5-4-2/h3-5H2,1-2H3
- InChI Key
- OFBQJSOFQDEBGM-UHFFFAOYSA-N
- Formula
- C5H12
- SMILES
- CCCCC
- Molecular Weight1
- 72.15
- CAS
- 109-66-0
- Other Names
-
- Amyl hydride
- NSC 72415
- PENTYL HYDRIDE
- Pentan
- Pentanen
- Pentani
- Skellysolve A
- n-C5H12
- n-Pentane
- ω : Acentric Factor.
- Tig : Autoignition Temperature (K).
- AP : Aniline Point (K).
- ΔcH°gas : Standard gas enthalpy of combustion (kJ/mol).
- 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.
- ρl : Liquid Density (kg/m3).
- 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).
- ΔvapS : Entropy of vaporization at a given temperature (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tboil : Boiling point at given pressure (K).
- Tc : Critical Temperature (K).
- λ : Gas thermal conductivity (W/m×K).
- λ : Liquid thermal conductivity (W/m×K).
- αdiff : Thermal diffusivity (m2/s).
- 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
- Pressure Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.2510 | KDB | |
| Tig | 557.59 | K | KDB |
| AP | 343.850 | K | KDB |
| ΔcH°gas | [-3536.60; -3535.40] | kJ/mol |
|
| ΔcH°gas | -3535.40 ± 0.96 | kJ/mol | NIST |
| ΔcH°gas | -3536.60 ± 0.88 | kJ/mol | NIST |
| ΔcH°liquid | [-3509.50; -3509.00] | kJ/mol |
|
| ΔcH°liquid | -3509.00 ± 0.46 | kJ/mol | NIST |
| ΔcH°liquid | -3509.50 ± 0.59 | kJ/mol | NIST |
| ΔcH°liquid | -3509.20 ± 0.75 | kJ/mol | NIST |
| μ | 0.00 | debye | KDB |
| LFL | 1.40 | % in Air | KDB |
| UFL | 8.30 | % in Air | KDB |
| Tflash,oc | 223.71 | K | KDB |
| ΔfG° | -8.37 | kJ/mol | KDB |
| Rg | 3.3850 | KDB | |
| Δc,grossH | 3509.41 | kJ/mol | KDB |
| Δc,netH | 3245.361 | kJ/mol | KDB |
| ΔfH°gas | [-147.10; -146.40] | kJ/mol |
|
| ΔfH°gas | -146.50 | kJ/mol | KDB |
| ΔfH°gas | -146.80 ± 0.59 | kJ/mol | NIST |
| ΔfH°gas | -147.10 ± 1.00 | kJ/mol | NIST |
| ΔfH°gas | -146.40 ± 0.67 | kJ/mol | NIST |
| ΔfH°liquid | [-173.50; -173.10] | kJ/mol |
|
| ΔfH°liquid | -173.50 ± 0.59 | kJ/mol | NIST |
| ΔfH°liquid | -173.10 ± 0.67 | kJ/mol | NIST |
| ΔfusH° | 8.71 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [26.20; 27.40] | kJ/mol |
|
| ΔvapH° | 26.75 | kJ/mol | NIST |
| ΔvapH° | 26.20 | kJ/mol | NIST |
| ΔvapH° | 26.40 | kJ/mol | NIST |
| ΔvapH° | 26.60 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 26.40 | kJ/mol | NIST |
| ΔvapH° | 26.40 | kJ/mol | NIST |
| ΔvapH° | 26.70 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 26.40 | kJ/mol | NIST |
| ΔvapH° | 26.42 | kJ/mol | NIST |
| ΔvapH° | Outlier 27.40 | kJ/mol | NIST |
| ΔvapH° | 26.20 | kJ/mol | NIST |
| IE | [10.18; 10.93] | eV |
|
| IE | 10.28 ± 0.10 | eV | NIST |
| IE | 10.37 | eV | NIST |
| IE | 10.43 | eV | NIST |
| IE | 10.22 ± 0.05 | eV | NIST |
| IE | 10.28 ± 0.10 | eV | NIST |
| IE | 10.18 ± 0.15 | eV | NIST |
| IE | Outlier 10.93 | eV | NIST |
| IE | 10.20 ± 0.10 | eV | NIST |
| IE | 10.50 | eV | NIST |
| IE | 10.36 | eV | NIST |
| IE | 10.59 ± 0.05 | eV | NIST |
| IE | 10.37 | eV | NIST |
| IE | 10.35 | eV | NIST |
| IE | Outlier 10.90 ± 0.10 | eV | NIST |
| log10WS | [-3.18; -3.18] |
|
|
| log10WS | -3.18 | Aq. Sol... | |
| log10WS | -3.18 | Estimat... | |
| logPoct/wat | 2.196 | Crippen Calculated Property | |
| McVol | 81.310 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 4 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | 3370.00 | kPa | KDB |
| S°gas | 347.82 ± 0.84 | J/mol×K | NIST |
| S°liquid | [259.40; 263.47] | J/mol×K |
|
| S°liquid | 263.47 | J/mol×K | NIST |
| S°liquid | 262.67 | J/mol×K | NIST |
| S°liquid | 259.40 | J/mol×K | NIST |
| Tboil | [309.21; 309.30] | K |
|
| Tboil | 309.21 | K | KDB |
| Tboil | 309.30 | K | Measure... |
| Tc | 469.70 | K | KDB |
| Tfus | [143.26; 143.40] | K |
|
| Tfus | 143.40 | K | KDB |
| Tfus | 143.26 | K | Aq. Sol... |
| Ttriple | 143.43 | K | KDB |
| Vc | [0.295; 0.315] | m3/kmol |
|
| Vc | 0.311 | m3/kmol | KDB |
| Vc | 0.311 | m3/kmol | NIST |
| Vc | 0.310 ± 0.000 | m3/kmol | NIST |
| Vc | 0.295 ± 0.006 | m3/kmol | NIST |
| Vc | 0.315 ± 0.003 | m3/kmol | NIST |
| Zc | 0.2683690 | KDB | |
| Zra | 0.27 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [120.07; 232.90] | J/mol×K | [298.15; 700.00] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 120 140 160 180 200 220 240 400 600 | ||||
| Cp,gas | 120.07 ± 0.24 | J/mol×K | 298.15 | NIST |
| Cp,gas | 127.84 ± 0.26 | J/mol×K | 323.15 | NIST |
| Cp,gas | 135.90 ± 0.27 | J/mol×K | 348.15 | NIST |
| Cp,gas | 143.95 ± 0.29 | J/mol×K | 373.15 | NIST |
| Cp,gas | 151.92 ± 0.30 | J/mol×K | 398.15 | NIST |
| Cp,gas | 159.67 ± 0.32 | J/mol×K | 423.15 | NIST |
| Cp,gas | 167.37 ± 0.33 | J/mol×K | 448.15 | NIST |
| Cp,gas | 168.11 | J/mol×K | 450.00 | NIST |
| Cp,gas | 174.75 ± 0.35 | J/mol×K | 473.15 | NIST |
| Cp,gas | 181.98 ± 0.36 | J/mol×K | 498.15 | NIST |
| Cp,gas | 182.39 | J/mol×K | 500.00 | NIST |
| Cp,gas | 189.08 ± 0.38 | J/mol×K | 523.15 | NIST |
| Cp,gas | 195.96 | J/mol×K | 550.00 | NIST |
| Cp,gas | 209.23 | J/mol×K | 600.00 | NIST |
| Cp,gas | 221.93 | J/mol×K | 650.00 | NIST |
| Cp,gas | 232.90 | J/mol×K | 700.00 | NIST |
| Cp,liquid | [163.20; 168.60] | J/mol×K | [290.00; 298.15] |
|
| Cp,liquid | 167.99 | J/mol×K | 290.00 | NIST |
| Cp,liquid | 163.20 | J/mol×K | 290.00 | NIST |
| Cp,liquid | 168.60 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 167.19 | J/mol×K | 298.15 | NIST |
| η | [0.0002100; 0.0036563] | Pa×s | [146.11; 313.80] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 3.50e-3 4.00e-3 150 200 250 300 | ||||
| η | 0.0036563 | Pa×s | 146.11 | Joback Calculated Property |
| η | 0.0015494 | Pa×s | 174.06 | Joback Calculated Property |
| η | 0.0008327 | Pa×s | 202.01 | Joback Calculated Property |
| η | 0.0005204 | Pa×s | 229.96 | Joback Calculated Property |
| η | 0.0003601 | Pa×s | 257.90 | Joback Calculated Property |
| η | 0.0002678 | Pa×s | 285.85 | Joback Calculated Property |
| η | 0.0002100 | Pa×s | 313.80 | Joback Calculated Property |
| ΔfusH | [8.38; 8.41] | kJ/mol | [143.40; 143.50] |
|
|
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 8.38 8.39 8.4 8.41 143.4 143.45 143.5 | ||||
| ΔfusH | 8.38 | kJ/mol | 143.40 | NIST |
| ΔfusH | 8.41 | kJ/mol | 143.46 | NIST |
| ΔfusH | 8.40 | kJ/mol | 143.47 | NIST |
| ΔfusH | 8.40 | kJ/mol | 143.50 | NIST |
| ΔfusH | 8.40 | kJ/mol | 143.50 | NIST |
| ΔsubH | 42.00 | kJ/mol | 143.00 | NIST |
| ΔvapH | [8.50; 32.30] | kJ/mol | [183.00; 460.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 10 15 20 25 30 200 300 400 | ||||
| ΔvapH | 32.30 | kJ/mol | 183.00 | NIST |
| ΔvapH | 29.80 | kJ/mol | 287.50 | NIST |
| ΔvapH | 26.20 | kJ/mol | 298.15 | NIST |
| ΔvapH | 27.90 | kJ/mol | 305.00 | NIST |
| ΔvapH | 25.79 | kJ/mol | 309.20 | NIST |
| ΔvapH | 25.77 | kJ/mol | 309.20 | KDB |
| ΔvapH | 25.50 | kJ/mol | 310.00 | NIST |
| ΔvapH | 23.00 | kJ/mol | 350.00 | NIST |
| ΔvapH | 26.70 | kJ/mol | 365.50 | NIST |
| ΔvapH | 26.10 | kJ/mol | 386.00 | NIST |
| ΔvapH | 19.70 | kJ/mol | 390.00 | NIST |
| ΔvapH | 15.10 | kJ/mol | 430.00 | NIST |
| ΔvapH | 26.20 | kJ/mol | 444.00 | NIST |
| ΔvapH | 8.50 | kJ/mol | 460.00 | NIST |
| Pvap | [48.00; 3286.00] | kPa | [288.25; 468.15] |
|
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 300 350 400 450 | ||||
| Pvap | 48.00 | kPa | 288.25 | Isother... |
| Pvap | 66.00 | kPa | 296.24 | Isother... |
| Pvap | 101.32 | kPa | 309.30 | Measure... |
| Pvap | 101.73 | kPa | 309.32 | Vapour ... |
| Pvap | 118.39 | kPa | 313.85 | Vapour ... |
| Pvap | 145.30 | kPa | 320.20 | Vapour ... |
| Pvap | 169.71 | kPa | 325.22 | Vapour ... |
| Pvap | 200.67 | kPa | 330.84 | Vapour ... |
| Pvap | 215.21 | kPa | 333.15 | Vapor L... |
| Pvap | 227.66 | kPa | 335.22 | Vapour ... |
| Pvap | 256.78 | kPa | 339.51 | Vapour ... |
| Pvap | 284.81 | kPa | 343.32 | Vapour ... |
| Pvap | 312.35 | kPa | 346.78 | Vapour ... |
| Pvap | 338.98 | kPa | 349.92 | Vapour ... |
| Pvap | 371.25 | kPa | 353.48 | Vapour ... |
| Pvap | 403.22 | kPa | 356.79 | Vapour ... |
| Pvap | 436.34 | kPa | 360.01 | Vapour ... |
| Pvap | 471.57 | kPa | 363.24 | Vapour ... |
| Pvap | 507.70 | kPa | 366.37 | Vapour ... |
| Pvap | 551.11 | kPa | 369.92 | Vapour ... |
| Pvap | 600.00 | kPa | 373.15 | In Situ... |
| Pvap | 648.59 | kPa | 377.19 | Vapour ... |
| Pvap | 754.18 | kPa | 384.19 | Vapour ... |
| Pvap | 895.85 | kPa | 392.52 | Vapour ... |
| Pvap | 917.75 | kPa | 393.15 | Vapor L... |
| Pvap | 995.29 | kPa | 397.80 | Vapour ... |
| Pvap | 1092.40 | kPa | 402.59 | Vapour ... |
| Pvap | 1185.12 | kPa | 406.87 | Vapour ... |
| Pvap | 1300.00 | kPa | 406.90 | Experim... |
| Pvap | 1317.45 | kPa | 412.57 | Vapour ... |
| Pvap | 1405.53 | kPa | 416.13 | Vapour ... |
| Pvap | 1450.02 | kPa | 417.87 | Vapour ... |
| Pvap | 1508.64 | kPa | 420.09 | Vapour ... |
| Pvap | 1620.00 | kPa | 423.15 | In Situ... |
| Pvap | 1608.88 | kPa | 423.75 | Vapour ... |
| Pvap | 1633.21 | kPa | 424.62 | Vapour ... |
| Pvap | 1704.41 | kPa | 427.09 | Vapour ... |
| Pvap | 1804.83 | kPa | 430.44 | Vapour ... |
| Pvap | 1812.00 | kPa | 430.68 | Vapour ... |
| Pvap | 1903.73 | kPa | 433.61 | Vapour ... |
| Pvap | 2033.22 | kPa | 437.57 | Vapour ... |
| Pvap | 2143.72 | kPa | 440.81 | Vapour ... |
| Pvap | 2242.61 | kPa | 443.59 | Vapour ... |
| Pvap | 2355.20 | kPa | 446.65 | Vapour ... |
| Pvap | 2451.91 | kPa | 449.18 | Vapour ... |
| Pvap | 2559.30 | kPa | 451.90 | Vapour ... |
| Pvap | 2562.84 | kPa | 451.99 | Vapour ... |
| Pvap | 2658.58 | kPa | 454.33 | Vapour ... |
| Pvap | 2727.72 | kPa | 455.99 | Vapour ... |
| Pvap | 3286.00 | kPa | 468.15 | Isother... |
| n0 | [1.35230; 1.35870] | [293.15; 303.15] |
|
|
|
T(K) Refractive Index 1.35 1.35 1.35 1.36 1.36 1.36 1.36 1.36 295 300 | ||||
| n0 | 1.35780 | 293.15 | Isobari... | |
| n0 | 1.35870 | 298.10 | Excess ... | |
| n0 | 1.35472 | 298.15 | KDB | |
| n0 | 1.35450 | 298.15 | Multipr... | |
| n0 | 1.35470 | 298.15 | Improve... | |
| n0 | 1.35230 | 303.15 | Phase e... | |
| ρl | [611.01; 645.50] | kg/m3 | [273.15; 308.15] |
|
|
T(K) Liquid Density (kg/m3) 610 615 620 625 630 635 640 645 280 290 300 | ||||
| ρl | 645.50 | kg/m3 | 273.15 | Experim... |
| ρl | 640.70 | kg/m3 | 278.15 | Experim... |
| ρl | 635.90 | kg/m3 | 283.15 | Experim... |
| ρl | 631.04 | kg/m3 | 288.15 | Experim... |
| ρl | 627.86 | kg/m3 | 291.15 | Experim... |
| ρl | 626.00 | kg/m3 | 293.00 | KDB |
| ρl | 626.23 | kg/m3 | 293.15 | Surface... |
| ρl | 626.12 | kg/m3 | 293.15 | Experim... |
| ρl | 626.00 | kg/m3 | 293.15 | Total P... |
| ρl | 627.00 | kg/m3 | 293.15 | Experim... |
| ρl | 621.14 | kg/m3 | 298.15 | Experim... |
| ρl | 621.30 | kg/m3 | 298.15 | Liquid-... |
| ρl | 621.32 | kg/m3 | 298.15 | Viscosi... |
| ρl | 620.89 | kg/m3 | 298.15 | Experim... |
| ρl | 624.93 | kg/m3 | 298.20 | Apparen... |
| ρl | 616.11 | kg/m3 | 303.15 | Experim... |
| ρl | 611.01 | kg/m3 | 308.15 | Experim... |
| ΔfusS | [58.41; 58.66] | J/mol×K | [143.40; 143.47] |
|
| ΔfusS | 58.41 | J/mol×K | 143.40 | NIST |
| ΔfusS | 58.66 | J/mol×K | 143.46 | NIST |
| ΔfusS | 58.56 | J/mol×K | 143.47 | NIST |
| γ | [0.01; 0.02] | N/m | [293.15; 323.15] |
|
|
T(K) Surface Tension (N/m) 0.01 0.01 0.01 0.02 0.02 300 310 320 | ||||
| γ | 0.02 | N/m | 293.15 | Experim... |
| γ | 0.02 | N/m | 293.20 | KDB |
| γ | 0.02 | N/m | 298.15 | Experim... |
| γ | 0.01 | N/m | 305.15 | Experim... |
| γ | 0.01 | N/m | 318.15 | Experim... |
| γ | 0.01 | N/m | 323.15 | Experim... |
| ΔvapS | 87.88 | J/mol×K | 298.15 | NIST |
| αdiff | [2.59e-08; 7.18e-08] | m2/s | [306.16; 466.37] |
|
|
T(K) Thermal diffusivity (m2/s) 3.00e-8 4.00e-8 5.00e-8 6.00e-8 7.00e-8 350 400 450 | ||||
| αdiff | 7.18e-08 | m2/s | 306.16 | Thermal... |
| αdiff | 6.84e-08 | m2/s | 323.16 | Thermal... |
| αdiff | 6.42e-08 | m2/s | 338.39 | Thermal... |
| αdiff | 6.19e-08 | m2/s | 353.16 | Thermal... |
| αdiff | 6.07e-08 | m2/s | 358.13 | Thermal... |
| αdiff | 5.91e-08 | m2/s | 362.37 | Thermal... |
| αdiff | 5.79e-08 | m2/s | 368.18 | Thermal... |
| αdiff | 5.74e-08 | m2/s | 373.47 | Thermal... |
| αdiff | 5.69e-08 | m2/s | 378.20 | Thermal... |
| αdiff | 5.53e-08 | m2/s | 383.42 | Thermal... |
| αdiff | 5.45e-08 | m2/s | 388.15 | Thermal... |
| αdiff | 5.40e-08 | m2/s | 393.32 | Thermal... |
| αdiff | 5.35e-08 | m2/s | 396.29 | Thermal... |
| αdiff | 5.24e-08 | m2/s | 399.16 | Thermal... |
| αdiff | 5.16e-08 | m2/s | 403.33 | Thermal... |
| αdiff | 5.12e-08 | m2/s | 408.63 | Thermal... |
| αdiff | 5.01e-08 | m2/s | 413.33 | Thermal... |
| αdiff | 4.93e-08 | m2/s | 418.39 | Thermal... |
| αdiff | 4.84e-08 | m2/s | 423.61 | Thermal... |
| αdiff | 4.69e-08 | m2/s | 428.17 | Thermal... |
| αdiff | 4.58e-08 | m2/s | 433.29 | Thermal... |
| αdiff | 4.49e-08 | m2/s | 436.19 | Thermal... |
| αdiff | 4.43e-08 | m2/s | 439.21 | Thermal... |
| αdiff | 4.38e-08 | m2/s | 442.35 | Thermal... |
| αdiff | 4.34e-08 | m2/s | 445.16 | Thermal... |
| αdiff | 4.20e-08 | m2/s | 448.08 | Thermal... |
| αdiff | 4.08e-08 | m2/s | 451.38 | Thermal... |
| αdiff | 3.84e-08 | m2/s | 455.20 | Thermal... |
| αdiff | 3.55e-08 | m2/s | 458.40 | Thermal... |
| αdiff | 3.37e-08 | m2/s | 460.10 | Thermal... |
| αdiff | 3.04e-08 | m2/s | 463.41 | Thermal... |
| αdiff | 2.59e-08 | m2/s | 466.37 | Thermal... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil | 309.15 | K | 96.60 | Low cos... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 293.21 | 2000.00 | 628.05 |
| 293.21 | 3998.00 | 630.31 |
| 293.21 | 6000.00 | 632.63 |
| 293.21 | 8003.00 | 634.89 |
| 293.22 | 10008.00 | 636.91 |
| 293.21 | 13008.00 | 640.02 |
| 293.22 | 16007.00 | 643.0 |
| 293.22 | 19009.00 | 645.81 |
| 293.22 | 22010.00 | 648.59 |
| 293.22 | 25002.00 | 651.19 |
| 293.22 | 28002.00 | 653.72 |
| 293.21 | 30000.00 | 655.38 |
| 313.10 | 2005.00 | 608.49 |
| 313.11 | 4002.00 | 611.31 |
| 313.10 | 6001.00 | 613.99 |
| 313.10 | 7999.00 | 616.58 |
| 313.10 | 10005.00 | 619.09 |
| 313.10 | 13001.00 | 622.65 |
| 313.10 | 16005.00 | 626.03 |
| 313.10 | 19002.00 | 629.28 |
| 313.10 | 22002.00 | 632.38 |
| 313.10 | 25004.00 | 635.4 |
| 313.10 | 28002.00 | 638.2 |
| 313.10 | 30005.00 | 640.09 |
| 333.01 | 2009.00 | 587.87 |
| 333.01 | 3997.00 | 591.4 |
| 333.01 | 6002.00 | 594.59 |
| 333.01 | 8008.00 | 597.69 |
| 333.01 | 10001.00 | 600.61 |
| 333.01 | 12998.00 | 604.82 |
| 333.01 | 15996.00 | 608.78 |
| 333.01 | 19000.00 | 612.5 |
| 333.01 | 21997.00 | 616.1 |
| 333.01 | 25000.00 | 619.39 |
| 333.01 | 27997.00 | 622.68 |
| 333.01 | 30006.00 | 624.71 |
| 353.12 | 2006.00 | 565.77 |
| 353.12 | 3997.00 | 570.01 |
| 353.12 | 6002.00 | 574.02 |
| 353.12 | 8003.00 | 577.79 |
| 353.12 | 10008.00 | 581.28 |
| 353.12 | 13000.00 | 586.31 |
| 353.12 | 16001.00 | 590.9 |
| 353.12 | 18997.00 | 595.21 |
| 353.13 | 22000.00 | 599.29 |
| 353.12 | 25002.00 | 603.1 |
| 353.12 | 28005.00 | 606.77 |
| 353.12 | 30001.00 | 609.1 |
| Reference | ||
Thermal conductivity, W/m/K
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Gas | Pressure, kPa - Gas | Thermal conductivity, W/m/K - Gas |
| 342.97 | 100.00 | 0.0189 |
| 366.02 | 100.00 | 0.0217 |
| 380.86 | 100.00 | 0.0237 |
| 407.37 | 100.00 | 0.0272 |
| 342.97 | 200.00 | 0.0190 |
| 366.02 | 200.00 | 0.0218 |
| 380.86 | 200.00 | 0.0238 |
| 407.37 | 200.00 | 0.0273 |
| 342.97 | 500.00 | 0.0192 |
| 366.02 | 500.00 | 0.0220 |
| 380.86 | 500.00 | 0.0240 |
| 407.37 | 500.00 | 0.0275 |
| Reference | ||
Thermal conductivity, W/m/K
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Thermal conductivity, W/m/K - Liquid |
| 309.04 | 260.00 | 0.1090 |
| 309.04 | 261.00 | 0.1092 |
| 309.04 | 1000.00 | 0.1095 |
| 309.04 | 2000.00 | 0.1101 |
| 309.04 | 3012.00 | 0.1108 |
| 309.04 | 4151.00 | 0.1118 |
| 309.04 | 4297.00 | 0.1117 |
| 309.04 | 5604.00 | 0.1123 |
| 309.04 | 6001.00 | 0.1125 |
| 309.04 | 7000.00 | 0.1130 |
| 309.04 | 8108.00 | 0.1137 |
| 309.04 | 9011.00 | 0.1142 |
| 309.04 | 10008.00 | 0.1154 |
| 309.04 | 11054.00 | 0.1161 |
| 309.04 | 12000.00 | 0.1167 |
| 309.04 | 12504.00 | 0.1168 |
| 309.04 | 13000.00 | 0.1171 |
| 309.04 | 14742.00 | 0.1181 |
| 309.04 | 19800.00 | 0.1207 |
| 309.04 | 19908.00 | 0.1205 |
| 309.04 | 20004.00 | 0.1206 |
| 309.04 | 24000.00 | 0.1231 |
| 309.04 | 25000.00 | 0.1233 |
| 309.04 | 28000.00 | 0.1241 |
| 309.04 | 29100.00 | 0.1253 |
| 309.04 | 29300.00 | 0.1256 |
| 309.04 | 34000.00 | 0.1281 |
| 309.04 | 35000.00 | 0.1286 |
| 309.04 | 38000.00 | 0.1298 |
| 309.04 | 39100.00 | 0.1299 |
| 309.04 | 39176.00 | 0.1300 |
| 309.04 | 39350.00 | 0.1304 |
| 309.04 | 49940.00 | 0.1352 |
| 309.04 | 50230.00 | 0.1353 |
| 309.04 | 50800.00 | 0.1352 |
| 331.20 | 2097.00 | 0.1035 |
| 331.20 | 3000.00 | 0.1041 |
| 331.20 | 3500.00 | 0.1045 |
| 331.20 | 4000.00 | 0.1046 |
| 331.20 | 5000.00 | 0.1053 |
| 331.20 | 6000.00 | 0.1061 |
| 331.20 | 7000.00 | 0.1068 |
| 331.20 | 8000.00 | 0.1069 |
| 331.20 | 9000.00 | 0.1072 |
| 331.20 | 9500.00 | 0.1077 |
| 331.20 | 10000.00 | 0.1078 |
| 331.20 | 11000.00 | 0.1085 |
| 331.20 | 12000.00 | 0.1090 |
| 331.20 | 13000.00 | 0.1094 |
| 331.20 | 15000.00 | 0.1109 |
| 331.20 | 16000.00 | 0.1115 |
| 331.20 | 17000.00 | 0.1122 |
| 331.20 | 18000.00 | 0.1126 |
| 331.20 | 19000.00 | 0.1131 |
| 331.20 | 20000.00 | 0.1139 |
| 331.20 | 21000.00 | 0.1141 |
| 331.20 | 22000.00 | 0.1148 |
| 331.20 | 24000.00 | 0.1158 |
| 331.20 | 25482.00 | 0.1167 |
| 331.20 | 26404.00 | 0.1172 |
| 331.20 | 27000.00 | 0.1176 |
| 331.20 | 30000.00 | 0.1188 |
| 331.20 | 31040.00 | 0.1193 |
| 331.20 | 31081.00 | 0.1193 |
| 331.20 | 32500.00 | 0.1202 |
| 331.20 | 32500.00 | 0.1202 |
| 331.20 | 33500.00 | 0.1209 |
| 331.20 | 34477.00 | 0.1211 |
| 331.20 | 35500.00 | 0.1216 |
| 331.20 | 36500.00 | 0.1224 |
| 331.20 | 37885.00 | 0.1229 |
| 331.20 | 38500.00 | 0.1231 |
| 331.20 | 39000.00 | 0.1237 |
| 331.20 | 39500.00 | 0.1239 |
| 331.20 | 40000.00 | 0.1241 |
| 331.20 | 41000.00 | 0.1242 |
| 331.20 | 42000.00 | 0.1246 |
| 331.20 | 43500.00 | 0.1255 |
| 331.20 | 44500.00 | 0.1261 |
| 331.20 | 45500.00 | 0.1266 |
| 331.20 | 47000.00 | 0.1272 |
| 331.20 | 48000.00 | 0.1273 |
| 331.20 | 49500.00 | 0.1283 |
| 331.20 | 50000.00 | 0.1278 |
| 386.00 | 5061.00 | 0.0901 |
| 386.00 | 10175.00 | 0.0945 |
| 386.00 | 18875.00 | 0.0996 |
| 386.00 | 20275.00 | 0.1023 |
| 386.00 | 30275.00 | 0.1082 |
| 386.00 | 34475.00 | 0.1107 |
| 386.00 | 40275.00 | 0.1122 |
| 386.00 | 49975.00 | 0.1184 |
| 386.00 | 53475.00 | 0.1203 |
| 399.60 | 2900.00 | 0.0846 |
| 399.60 | 3000.00 | 0.0849 |
| 399.60 | 4000.00 | 0.0852 |
| 399.60 | 4500.00 | 0.0860 |
| 399.60 | 5000.00 | 0.0869 |
| 399.60 | 6000.00 | 0.0880 |
| 399.60 | 7000.00 | 0.0890 |
| 399.60 | 7500.00 | 0.0895 |
| 399.60 | 8000.00 | 0.0899 |
| 399.60 | 9500.00 | 0.0913 |
| 399.60 | 10000.00 | 0.0917 |
| 399.60 | 11000.00 | 0.0924 |
| 399.60 | 12000.00 | 0.0932 |
| 399.60 | 13000.00 | 0.0937 |
| 399.60 | 14000.00 | 0.0946 |
| 399.60 | 15000.00 | 0.0952 |
| 399.60 | 16000.00 | 0.0960 |
| 399.60 | 17000.00 | 0.0967 |
| 399.60 | 18000.00 | 0.0974 |
| 399.60 | 19000.00 | 0.0984 |
| 399.60 | 20000.00 | 0.0989 |
| 399.60 | 21000.00 | 0.0995 |
| 399.60 | 22000.00 | 0.1001 |
| 399.60 | 23500.00 | 0.1011 |
| 399.60 | 25000.00 | 0.1022 |
| 399.60 | 26000.00 | 0.1026 |
| 399.60 | 27000.00 | 0.1031 |
| 399.60 | 28000.00 | 0.1037 |
| 399.60 | 29000.00 | 0.1047 |
| 399.60 | 30000.00 | 0.1051 |
| 399.60 | 31000.00 | 0.1056 |
| 399.60 | 33000.00 | 0.1066 |
| 399.60 | 34000.00 | 0.1071 |
| 399.60 | 35000.00 | 0.1076 |
| 399.60 | 35301.00 | 0.1079 |
| 421.85 | 1640.00 | 0.0757 |
| 421.85 | 1650.00 | 0.0757 |
| 421.85 | 1660.00 | 0.0757 |
| 421.85 | 1680.00 | 0.0757 |
| 421.85 | 1700.00 | 0.0757 |
| 421.85 | 1710.00 | 0.0757 |
| 421.85 | 1720.00 | 0.0757 |
| 421.85 | 1730.00 | 0.0760 |
| 421.85 | 1750.00 | 0.0757 |
| 421.85 | 1764.00 | 0.0757 |
| 421.85 | 1772.00 | 0.0758 |
| 421.85 | 1910.00 | 0.0762 |
| 421.85 | 1946.00 | 0.0762 |
| 421.85 | 1954.00 | 0.0762 |
| 422.20 | 2518.00 | 0.0771 |
| 422.20 | 5041.00 | 0.0809 |
| 422.20 | 10475.00 | 0.0868 |
| 422.20 | 18675.00 | 0.0935 |
| 422.20 | 18775.00 | 0.0935 |
| 422.20 | 20475.00 | 0.0941 |
| 422.20 | 30575.00 | 0.1002 |
| 422.20 | 30675.00 | 0.1007 |
| 422.20 | 40275.00 | 0.1061 |
| 422.20 | 48075.00 | 0.1104 |
| 422.20 | 52975.00 | 0.1123 |
| 465.40 | 9497.00 | 0.0779 |
| 465.40 | 9610.00 | 0.0779 |
| 465.40 | 9891.00 | 0.0781 |
| 467.36 | 11000.00 | 0.0807 |
| 467.36 | 11500.00 | 0.0813 |
| 467.36 | 12000.00 | 0.0818 |
| 467.36 | 13000.00 | 0.0828 |
| 467.36 | 13800.00 | 0.0836 |
| 467.36 | 15200.00 | 0.0849 |
| 467.36 | 16000.00 | 0.0855 |
| 467.36 | 16500.00 | 0.0859 |
| 467.36 | 17000.00 | 0.0864 |
| 467.36 | 17500.00 | 0.0867 |
| 467.36 | 18000.00 | 0.0872 |
| 467.36 | 18500.00 | 0.0876 |
| 467.36 | 19000.00 | 0.0880 |
| 467.36 | 19500.00 | 0.0884 |
| 467.36 | 20000.00 | 0.0888 |
| 467.36 | 20500.00 | 0.0892 |
| 467.36 | 21000.00 | 0.0896 |
| 467.36 | 21500.00 | 0.0899 |
| 467.36 | 22000.00 | 0.0903 |
| 467.36 | 22500.00 | 0.0907 |
| 467.36 | 23000.00 | 0.0911 |
| 467.36 | 23500.00 | 0.0914 |
| 467.36 | 24000.00 | 0.0918 |
| 467.36 | 24500.00 | 0.0922 |
| 467.36 | 25000.00 | 0.0926 |
| 467.36 | 25500.00 | 0.0929 |
| 467.36 | 26000.00 | 0.0932 |
| 467.36 | 26500.00 | 0.0936 |
| 467.36 | 27000.00 | 0.0939 |
| 467.36 | 27500.00 | 0.0942 |
| 467.36 | 28000.00 | 0.0946 |
| 467.36 | 28500.00 | 0.0949 |
| 467.36 | 29000.00 | 0.0952 |
| 467.36 | 29500.00 | 0.0955 |
| 467.36 | 30000.00 | 0.0958 |
| 467.36 | 30500.00 | 0.0961 |
| 467.36 | 31000.00 | 0.0963 |
| 467.36 | 31280.00 | 0.0964 |
| 467.36 | 31300.00 | 0.0965 |
| 467.36 | 31340.00 | 0.0966 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [223.22; 330.82] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.41236e+01 | |||
| Coefficient B | -2.61147e+03 | |||
| Coefficient C | -3.44720e+01 | |||
| Temperature range, min. | 223.22 | |||
| Temperature range, max. | 330.82 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 | ||||
| Pvap | 1.33 | kPa | 223.22 | Calculated Property |
| Pvap | 3.04 | kPa | 235.18 | Calculated Property |
| Pvap | 6.32 | kPa | 247.13 | Calculated Property |
| Pvap | 12.15 | kPa | 259.09 | Calculated Property |
| Pvap | 21.86 | kPa | 271.04 | Calculated Property |
| Pvap | 37.18 | kPa | 283.00 | Calculated Property |
| Pvap | 60.22 | kPa | 294.95 | Calculated Property |
| Pvap | 93.51 | kPa | 306.91 | Calculated Property |
| Pvap | 139.91 | kPa | 318.86 | Calculated Property |
| Pvap | 202.65 | kPa | 330.82 | Calculated Property |
| Pvap | [5.24e-05; 3383.57] | kPa | [143.42; 469.65] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 8.19246e+01 | |||
| Coefficient B | -5.77802e+03 | |||
| Coefficient C | -1.04184e+01 | |||
| Coefficient D | 1.17821e-05 | |||
| Temperature range, min. | 143.42 | |||
| Temperature range, max. | 469.65 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 200 300 400 | ||||
| Pvap | 5.24e-05 | kPa | 143.42 | Calculated Property |
| Pvap | 0.02 | kPa | 179.67 | Calculated Property |
| Pvap | 0.75 | kPa | 215.92 | Calculated Property |
| Pvap | 8.55 | kPa | 252.16 | Calculated Property |
| Pvap | 47.31 | kPa | 288.41 | Calculated Property |
| Pvap | 167.67 | kPa | 324.66 | Calculated Property |
| Pvap | 445.64 | kPa | 360.91 | Calculated Property |
| Pvap | 979.81 | kPa | 397.15 | Calculated Property |
| Pvap | 1898.63 | kPa | 433.40 | Calculated Property |
| Pvap | 3383.57 | kPa | 469.65 | Calculated Property |
Similar Compounds
Find more compounds similar to Pentane.
Mixtures
- Pentane + Butane, 2-methyl-
- Methyl formate + Pentane
- Ethyl formate + Pentane
- Formic acid, propyl ester + Pentane
- Formic acid, butyl ester + Pentane
- Acetic acid + Pentane + Thiophene, tetrahydro-, 1,1-dioxide
- Pentane + Propanoic acid + Thiophene, tetrahydro-, 1,1-dioxide
- Butanoic acid + Pentane + Thiophene, tetrahydro-, 1,1-dioxide
- Pentane + Propanoic acid, 2-methyl- + Thiophene, tetrahydro-, 1,1-dioxide
- Pentane + Pentanoic acid + Thiophene, tetrahydro-, 1,1-dioxide
- Butanoic acid, 3-methyl- + Pentane + Thiophene, tetrahydro-, 1,1-dioxide
- n-Hexane + Pentane
- Heptane + Pentane
- Toluene + Pentane
- Hexane, tetradecafluoro- + Pentane
- Ethanol, 2,2'-oxybis- + Pentane
- Triethylene glycol + Pentane
- 1,2-Ethanediol + Pentane
- Benzene, 1,3-dimethyl- + Pentane
- Acetone + Pentane
Find more mixtures with Pentane.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Thermal Diffusivity and Speed of Sound of Saturated Pentane from Light Scattering
- 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 liquid liquid equilibria of 1-methylimidazole with hydrocarbons and ethers
- Measurement and modeling of hydrocarbon dew points for five synthetic natural gas mixtures
- Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, tributylmethylphosphonium methylsulphate by gas liquid chromatography
- Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
- High-pressure vapor liquid equilibria in the nitrogen n-pentane system
- A simple apparatus for data solubility determination
- Thermal conductivity of polyurethane foam cell gases: Improved transient hot wire cell data of isopentane + n-pentane mixtures Extended Wassiljewa-model
- 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)
- Gas-liquid chromatography measurements of activity coefficients at infinite dilution of hydrocarbons and alkanols in 1-alkyl-3-methylimidazolium bis(oxalato)borate
- Liquid liquid equilibria of imidazolium based ionic liquid + pyridine + hydrocarbon at 298.15 K: Experiments and correlations
- Validation of a new apparatus using the dynamic method for determining the critical properties of binary mixtures containing CO2 and a n-alkane
- Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
- Experimentation and thermodynamic representations of binaries containing compounds of low boiling points: Pentane and alkylmethanoates
- Study of critical and maximum temperatures of coexistence of liquid and gas phase in hydrocarbons binary mixtures of aromatic hydrocarbons with alkanes and cycloalkanes
- Phase equilibria measurements of ternary mixtures (sulfolane + a carboxylic acid + pentane) at 303.15 K
- Anomalous nucleation near a fluid phase boundary created by a rapid heat pulse
- 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
- Surface tension, density and composition in the methane-pentane system at high pressure
- Thermal conductivity of gaseous and liquid n-pentane
- Plotting of phase (vapor-liquid) transition surface near the critical point out of data from isochoric experiment. Experimental procedure
- New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
- Solubility of cinnamic acid in supercritical carbon dioxide and subcritical 1,1,1,2-tetrafluoroethane: Experimental data and modelling
- 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
- 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
- Liquid phase behaviour of 1-hexyloxymethyl-3-methyl-imidazolium-based ionic liquids with hydrocarbons: The influence of anion
- 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)
- Vapour pressures of n-pentane determined by comparative ebulliometry
- Experimental measurements and prediction of liquid densities for n-alkane mixtures
- 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
- Thermodynamic study of (perfluoroalkane + alkane) mixtures: Excess and solvation enthalpies
- 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
- 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
- Experimental and theoretical study of surface tension of n-pentane, n-heptane, and some of their mixtures at different temperatures
- 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
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate [EMIM][TCB] using gas liquid chromatography
- Activity coefficients at infinite dilution of organic solutes in N-alkylpyridinium bis(trifluoromethylsulfonyl)imide ([CnPY][NTf2], n = 2, 4, 5) using gas liquid chromatography
- 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
- 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
- Solubilities of evodiamine in twelve organic solvents from T = (283.2 to 323.2) K
- 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
- 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
- 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
- Use of water in aiding olefin/paraffin (liquid + liquid) extraction via complexation with a silver bis(trifluoromethylsulfonyl)imide salt
- 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
- Activity coefficients at infinite dilution of alkanes, alkenes, alkyl benzenes in dimethylphosphate based ionic liquids using gas liquid chromatography
- 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 activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-hexyl-2,3-dimethylimidazolium 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
- PVTx measurements and other derived volumetric properties of the binary ((1-propanol + n-pentane)) mixtures in the critical and supercritical regions
- Surface tension and density of mixtures of m-xylene + n-alkane at 293.15 K: Analysis under the extended Langmuir and Shereshefsky models
- 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 based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
- Separation of binary mixtures based on gamma infinity data using [OMMIM][BF4] ionic liquid and modelling of thermodynamic functions
- Low cost apparatus for rapid boiling point determination of small air sensitive samples under inert atmosphere
- Isobaric specific heat capacities of emulsified kerosene at high temperature and pressure
- Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
- Solubility of Mercury in Liquid Hydrocarbons and Hydrocarbon Mixtures
- Isobaric Vapor Liquid Equilibrium for Nine Binary Systems of Cracking C5 Fraction at 250 kPa
- Simultaneous Measurement of Dynamic Viscosity and Density of n-Alkanes at High Pressures
- Isothermal Vapor-Liquid Equilibrium Data for Binary Mixtures of Hexafluoroethane (R116) + n-Pentane or n-Hexane at Two Temperatures, 288 and 296 K
- Experimental Phase Equilibrium for the Binary System of n-Pentane +2-Propanol Using a New Equilibrium Cell and the Static Total Pressure Method
- Determination of Activity Coefficients at Infinite Dilution of Organic Solutes in the Ionic Liquid 1-(2-Hydroxyethyl)-3-methylimidazolium Nonafluoro-1-butanesulfonate Using Gas-Liquid Chromatography
- Solubilities of Organic Semiconductors and Nonsteroidal Anti-inflammatory Drugs in Pure and Mixed Organic Solvents: Measurement and Modeling with Hansen Solubility Parameter
- Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
- Measurement and Prediction of Hydrocarbon Dew Points of Synthetic Natural Gas Mixtures
- Total Pressure Phase Equilibrium Measurements for the Binary Systems of n-Pentane + Cyclohexane and 1-Hexene + 2-Propanol
- Parametric Analysis of Mandelic Acid Separation from Aqueous Solutions by Using Secondary Amine Mixture (Amberlite LA-2) in Various Diluents
- Experimental High-Pressure Isochoric/Isoplethic Equilibrium for the Systems Propane + n-Pentane and Propane + Diethyl Ether
- Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
- Liquid-Liquid Equilibrium Data for Ternary Systems Containing Alkanes (n-Pentane, n-Hexane, n-Heptane, and n-Octane) + Alcohol (Methanol and Ethanol) + Protic Ionic Liquid (2-HEAF)
- Thermodynamic Properties of Mixtures Containing Precursors of Vitamin B5
- Solubility of 1-Alkyl-3-methylimidazolium Hexafluorophosphate in Hydrocarbons
- 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
- Phase Behavior, Densities, and Isothermal Compressibility of CO2 + Pentane and CO2 + Acetone Systems in Various Phase Regions
- Phase Behavior, Densities and Isothermal Compressibility of CO2 + Pentane + Acetone Ternary System in Various Phase Regions
- Isothermal Vapor-Liquid Equilibria for the n-Pentane + 1-Butanol and n-Pentane + 2-Butanol Systems near the Critical Region of the Mixtures
- 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
- 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
- Viscosities and Excess Molar Volumes of the Ternary System Toluene (1) + Cyclohexane (2) + Pentane (3) at 298.15 K
- 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
- Vapor-Liquid Equilibria for the n-Pentane + 1-Propanol and n-Pentane + 2-Methyl-1-propanol Systems near the Critical Region
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Infinite Dilution Activity Coefficients for Trihexyltetradecyl Phosphonium Ionic Liquids: Measurements and COSMO-RS Prediction
- Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
- Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
- PVTx Measurements of Water-n-Pentane Mixtures in Critical and Supercritical Regions
- Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
- Solubility of Benzoic Acid in Pure Solvents and Binary Mixtures
- Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Decyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Measurement and Correlation for the Solubilities of Dihydrocapsaicin in n-Heptane, n-Hexane, n-Pentane, Ethyl Acetate, Acetone, Ethanol, and Water
- Equilibrium Phase Densities, Interfacial Tensions for the Ethane + n-Pentane System at 294.15 K
- Vapor-Liquid Equilibria Measurements of the Methane + Pentane and Methane + Hexane Systems at Temperatures from (173 to 330) K and Pressures to 14 MPa
- Solubilities of 1-Hexyl-3-methylimidazole Nitrate and 1-Octyl-3-methylimidazole Nitrate in Selected Solvents
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Ethyl-3-methylimidazolium Diethylphosphate Using Gas Liquid Chromatography
- Equilibrium Phase Densities, Vapor Phase Compositions, and Interfacial Tensions for the Methane + Ethane + n-Pentane System at 294.15 K
- Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
- Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
- Activity Coefficients at Infinite Dilution by GLC in Alkanediamines as Stationary Phases
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Dibutylphosphate Using Gas Liquid Chromatography
- Phase Equilibria of H2S-Hydrocarbons (Propane, n-Butane, and n-Pentane) Binary Systems at Low Temperatures
- Multiproperty Correlation of Experimental Data of the Binaries Propyl Ethanoate + Alkanes (Pentane to Decane). New Experimental Information for Vapor Liquid Equilibrium and Mixing Properties
- Solubilities of Rutaecarpine in Twelve Organic Solvents from (283.2 to 323.2) K
- Bubble-Point Measurements of Eight Binary Mixtures for Organic Rankine Cycle Applications
- Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
- Improvements in the Experimentation and the Representation of Thermodynamic Properties (iso-p VLE and yE) of Alkyl Propanoate + Alkane Binaries
- New Vapor Liquid Liquid Equilibrium Solubility Data for iso-Butane, n-Butane, n-Pentane, and n-Hexane in Alkanolamine Aqueous Solutions
- Enhancing liquid-phase olefin-paraffin separations using novel silver-based ionic liquids
- Liquid Liquid Equilibrium in Mixtures Containing Propane-1,2,3-triol and Mixtures Containing Vegetable Oils at Atmospheric Pressure
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Liquid - Liquid Equilibria for the Binary Systems of Sulfolane with Alkanes
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
- Excess Enthalpies and Thermal Conductivity Coefficients for Binary Mixtures of Carbon Tetrachloride and Four Alkanes (C5 to C8) at a Temperature of 298.15 K
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Hexyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
- 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 of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Liquid-Liquid Equilibria in Ternary Systems 2-Methylbutane + 2-Methyl-2-propanol + Water and Pentane + 2-Methyl-2-propanol + Water at 293.15 K
- In Situ Determination of Phase Equilibria of Methyl Benzoate + Alkane Mixtures Using an Infrared Absorption Method. Comparison with Polar GC-SAFT Predictions
- Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tris(pentafluoroethyl)trifluorophosphate [EMIM][FAP] Using Gas-Liquid Chromatography
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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