- InChI
- InChI=1S/C6H12/c1-4-5-6(2)3/h4-6H,1-3H3/b5-4-
- InChI Key
- LGAQJENWWYGFSN-PLNGDYQASA-N
- Formula
- C6H12
- SMILES
- CC=CC(C)C
- Molecular Weight1
- 84.16
- CAS
- 691-38-3
- Other Names
-
- (Z)-(CH3)2CHCH=CHCH3
- (Z)-4-methyl-2-pentene
- 2-Pentene, 4-methyl-cis-
- 4-Methyl-2-cis-pentene
- 4-Methyl-2-pentene
- 4-Methyl-2-pentene, cis
- 4-Methylpentene-2, cis-
- 4-methyl-cis-2-pentene
- cis-4-methyl-2-pentene
- cis-4-methylpent-2-ene
- ω : Acentric Factor.
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- Δc,grossH : Heat of Combustion, Gross form (kJ/mol).
- Δc,netH : Heat of Combustion, Net Form (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (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).
- 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).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- 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 | [0.2442; 0.2900] |
|
|
| ω | 0.2442 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.2900 | KDB | |
| μ | 0.22 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | [76.99; 82.19] | kJ/mol |
|
| ΔfG° | 76.99 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | 82.19 | kJ/mol | KDB |
| Δc,grossH | 3989.11 | kJ/mol | KDB |
| Δc,netH | 3725.015 | kJ/mol | KDB |
| ΔfH°gas | [-57.48; -50.33] | kJ/mol |
|
| ΔfH°gas | -50.33 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -57.48 | kJ/mol | KDB |
| ΔfusH° | 7.98 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [29.50; 29.50] | kJ/mol |
|
| ΔvapH° | 29.50 | kJ/mol | NIST |
| ΔvapH° | 29.50 | kJ/mol | NIST |
| ΔvapH° | 29.50 | kJ/mol | NIST |
| IE | [8.98; 8.98] | eV |
|
| IE | 8.98 ± 0.01 | eV | NIST |
| IE | 8.98 ± 0.02 | eV | NIST |
| IE | 8.98 ± 0.01 | eV | NIST |
| logPoct/wat | 2.219 | Crippen Calculated Property | |
| McVol | 91.100 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | [3040.00; 3220.00] | kPa |
|
| Pc | 3220.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 3040.00 | kPa | KDB |
| Ptriple | 2.16e-06 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [553.00; 574.00] |
|
|
| Inp | 567.50 | NIST | |
| Inp | 555.50 | NIST | |
| Inp | 562.00 | NIST | |
| Inp | 563.00 | NIST | |
| Inp | 565.00 | NIST | |
| Inp | 566.00 | NIST | |
| Inp | 566.00 | NIST | |
| Inp | 555.90 | NIST | |
| Inp | 565.60 | NIST | |
| Inp | 566.10 | NIST | |
| Inp | 556.20 | NIST | |
| Inp | 556.60 | NIST | |
| Inp | 567.00 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 556.00 | NIST | |
| Inp | 556.00 | NIST | |
| Inp | 556.10 | NIST | |
| Inp | 557.00 | NIST | |
| Inp | 557.00 | NIST | |
| Inp | 556.00 | NIST | |
| Inp | 560.70 | NIST | |
| Inp | 556.00 | NIST | |
| Inp | 557.00 | NIST | |
| Inp | 555.36 | NIST | |
| Inp | 561.00 | NIST | |
| Inp | 556.00 | NIST | |
| Inp | 556.00 | NIST | |
| Inp | 558.00 | NIST | |
| Inp | 558.00 | NIST | |
| Inp | 556.00 | NIST | |
| Inp | 561.00 | NIST | |
| Inp | 560.00 | NIST | |
| Inp | 558.00 | NIST | |
| Inp | 571.20 | NIST | |
| Inp | 565.90 | NIST | |
| Inp | 559.00 | NIST | |
| Inp | 555.90 | NIST | |
| Inp | 553.00 | NIST | |
| Inp | 556.00 | NIST | |
| Inp | Outlier 572.00 | NIST | |
| Inp | Outlier 574.00 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 558.00 | NIST | |
| Inp | 566.00 | NIST | |
| Inp | 557.00 | NIST | |
| Inp | 569.00 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 559.00 | NIST | |
| Inp | 567.50 | NIST | |
| Inp | 566.00 | NIST | |
| Inp | 556.20 | NIST | |
| Inp | 556.00 | NIST | |
| Inp | 560.70 | NIST | |
| Inp | 561.00 | NIST | |
| Inp | 555.90 | NIST | |
| Inp | 557.00 | NIST | |
| Tboil | [327.85; 331.20] | K |
|
| Tboil | 329.53 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 329.60 | K | KDB |
| Tboil | 330.70 | K | NIST |
| Tboil | 330.50 ± 0.50 | K | NIST |
| Tboil | 329.50 | K | NIST |
| Tboil | 329.45 ± 0.50 | K | NIST |
| Tboil | 329.56 ± 0.50 | K | NIST |
| Tboil | 329.55 ± 0.50 | K | NIST |
| Tboil | 329.65 ± 1.00 | K | NIST |
| Tboil | 329.15 ± 1.50 | K | NIST |
| Tboil | 327.85 ± 1.00 | K | NIST |
| Tboil | 327.95 ± 1.50 | K | NIST |
| Tboil | 328.15 ± 4.00 | K | NIST |
| Tboil | 329.15 ± 2.00 | K | NIST |
| Tboil | 331.20 ± 2.00 | K | NIST |
| Tboil | 327.85 ± 0.60 | K | NIST |
| Tc | [490.00; 499.00] | K |
|
| Tc | 496.30 | K | Gas-Liquid Critical Temperatures of Some Alkenes, Amines, and Cyclic Hydrocarbons |
| Tc | 499.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 490.00 | K | KDB |
| Tfus | [138.72; 139.00] | K |
|
| Tfus | 138.72 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 139.00 | K | KDB |
| Ttriple | 138.30 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 3.64 | ChemSep v8.3 pure component data Compiled value | |
| URi | 4.27 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.346; 0.360] | m3/kmol |
|
| Vc | 0.346 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.360 | m3/kmol | KDB |
| Zc | [0.2686230; 0.2690000] |
|
|
| Zc | 0.2690000 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.2686230 | KDB | |
| Zra | 0.27 | ChemSep v8.3 pure component data Compiled value |
Cheméo can also estimate Log10 of Water solubility in mol/l for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [27.57; 30.80] | kJ/mol | [298.50; 329.60] |
|
| ΔvapH | 30.80 | kJ/mol | 298.50 | NIST |
| ΔvapH | 27.57 | kJ/mol | 329.60 | KDB |
| n0 | 1.38498 | 298.15 | KDB | |
| ρl | 669.00 | kg/m3 | 293.00 | KDB |
| γ | 0.02 | N/m | 298.20 | KDB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [109.57; 352.63] | J/mol×K | [200.00; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 1.01130e+02 | |||
| Coefficient B | -8.61950e+02 | |||
| Coefficient C | 6.55524e+00 | |||
| Coefficient D | -6.05290e-04 | |||
| Coefficient E | 2.02120e-07 | |||
| Temperature range, min. | 200.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 109.57 | J/mol×K | 200.00 | Calculated Property |
| Cp,gas | 148.99 | J/mol×K | 344.44 | Calculated Property |
| Cp,gas | 195.25 | J/mol×K | 488.89 | Calculated Property |
| Cp,gas | 234.35 | J/mol×K | 633.33 | Calculated Property |
| Cp,gas | 264.91 | J/mol×K | 777.78 | Calculated Property |
| Cp,gas | 288.73 | J/mol×K | 922.22 | Calculated Property |
| Cp,gas | 307.88 | J/mol×K | 1066.67 | Calculated Property |
| Cp,gas | 324.08 | J/mol×K | 1211.11 | Calculated Property |
| Cp,gas | 338.66 | J/mol×K | 1355.56 | Calculated Property |
| Cp,gas | 352.63 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [112.81; 194.71] | J/mol×K | [138.30; 329.53] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | -5.98030e+01 | |||
| Coefficient B | -1.62030e+01 | |||
| Coefficient C | 4.86524e+00 | |||
| Coefficient D | 3.43330e-03 | |||
| Coefficient E | -3.75810e-06 | |||
| Temperature range, min. | 138.30 | |||
| Temperature range, max. | 329.53 | |||
| Cp,liquid | 112.81 | J/mol×K | 138.30 | Calculated Property |
| Cp,liquid | 124.36 | J/mol×K | 159.55 | Calculated Property |
| Cp,liquid | 135.30 | J/mol×K | 180.80 | Calculated Property |
| Cp,liquid | 145.67 | J/mol×K | 202.04 | Calculated Property |
| Cp,liquid | 155.48 | J/mol×K | 223.29 | Calculated Property |
| Cp,liquid | 164.69 | J/mol×K | 244.54 | Calculated Property |
| Cp,liquid | 173.26 | J/mol×K | 265.79 | Calculated Property |
| Cp,liquid | 181.16 | J/mol×K | 287.03 | Calculated Property |
| Cp,liquid | 188.33 | J/mol×K | 308.28 | Calculated Property |
| Cp,liquid | 194.71 | J/mol×K | 329.53 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0058519; 0.0001231] | Pa×s | [138.30; 405.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.17520e+01 | |||
| Coefficient B | 8.20420e+02 | |||
| Coefficient C | 1.40560e-01 | |||
| Coefficient D | -7.34350e-07 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 138.30 | |||
| Temperature range, max. | 405.00 | |||
| η | 0.0058519 | Pa×s | 138.30 | Calculated Property |
| η | 0.0020972 | Pa×s | 167.93 | Calculated Property |
| η | 0.0010230 | Pa×s | 197.57 | Calculated Property |
| η | 0.0006014 | Pa×s | 227.20 | Calculated Property |
| η | 0.0003991 | Pa×s | 256.83 | Calculated Property |
| η | 0.0002878 | Pa×s | 286.47 | Calculated Property |
| η | 0.0002202 | Pa×s | 316.10 | Calculated Property |
| η | 0.0001760 | Pa×s | 345.73 | Calculated Property |
| η | 0.0001453 | Pa×s | 375.37 | Calculated Property |
| η | 0.0001231 | Pa×s | 405.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [39.14; 11.74] | kJ/mol | [138.30; 480.02] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 5.42270e+01 | |||
| Coefficient B | 1.56280e+00 | |||
| Coefficient C | -2.61710e+00 | |||
| Coefficient D | 2.42980e+00 | |||
| Coefficient E | -9.27580e-01 | |||
| Critical temperature, Tc (K) | 4.99000e+02 | |||
| Temperature range, min. | 138.30 | |||
| Temperature range, max. | 480.02 | |||
| ΔvapH | 39.14 | kJ/mol | 138.30 | Calculated Property |
| ΔvapH | 36.62 | kJ/mol | 176.27 | Calculated Property |
| ΔvapH | 34.36 | kJ/mol | 214.24 | Calculated Property |
| ΔvapH | 32.18 | kJ/mol | 252.21 | Calculated Property |
| ΔvapH | 29.98 | kJ/mol | 290.18 | Calculated Property |
| ΔvapH | 27.64 | kJ/mol | 328.14 | Calculated Property |
| ΔvapH | 25.03 | kJ/mol | 366.11 | Calculated Property |
| ΔvapH | 21.97 | kJ/mol | 404.08 | Calculated Property |
| ΔvapH | 18.07 | kJ/mol | 442.05 | Calculated Property |
| ΔvapH | 11.74 | kJ/mol | 480.02 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.68] | kPa | [237.28; 352.77] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.40679e+01 | |||
| Coefficient B | -2.77368e+03 | |||
| Coefficient C | -3.60040e+01 | |||
| Temperature range, min. | 237.28 | |||
| Temperature range, max. | 352.77 | |||
| Pvap | 1.33 | kPa | 237.28 | Calculated Property |
| Pvap | 3.04 | kPa | 250.11 | Calculated Property |
| Pvap | 6.33 | kPa | 262.94 | Calculated Property |
| Pvap | 12.18 | kPa | 275.78 | Calculated Property |
| Pvap | 21.92 | kPa | 288.61 | Calculated Property |
| Pvap | 37.28 | kPa | 301.44 | Calculated Property |
| Pvap | 60.36 | kPa | 314.27 | Calculated Property |
| Pvap | 93.66 | kPa | 327.11 | Calculated Property |
| Pvap | 140.04 | kPa | 339.94 | Calculated Property |
| Pvap | 202.68 | kPa | 352.77 | Calculated Property |
| Pvap | [2.06e-06; 3220.40] | kPa | [138.30; 499.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 7.66652e+01 | |||
| Coefficient B | -5.99390e+03 | |||
| Coefficient C | -9.45010e+00 | |||
| Coefficient D | 8.56860e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 138.30 | |||
| Temperature range, max. | 499.00 | |||
| Pvap | 2.06e-06 | kPa | 138.30 | Calculated Property |
| Pvap | 3.51e-03 | kPa | 178.38 | Calculated Property |
| Pvap | 0.28 | kPa | 218.46 | Calculated Property |
| Pvap | 4.75 | kPa | 258.53 | Calculated Property |
| Pvap | 33.09 | kPa | 298.61 | Calculated Property |
| Pvap | 134.72 | kPa | 338.69 | Calculated Property |
| Pvap | 389.65 | kPa | 378.77 | Calculated Property |
| Pvap | 900.46 | kPa | 418.84 | Calculated Property |
| Pvap | 1790.98 | kPa | 458.92 | Calculated Property |
| Pvap | 3220.40 | kPa | 499.00 | Calculated Property |
| Pvap | [2.16e-06; 3223.80] | kPa | [138.30; 499.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 7.59746e+01 | |||
| Coefficient B | -5.96255e+03 | |||
| Coefficient C | -9.34598e+00 | |||
| Coefficient D | 8.49625e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 138.30 | |||
| Temperature range, max. | 499.00 | |||
| Pvap | 2.16e-06 | kPa | 138.30 | Calculated Property |
| Pvap | 3.59e-03 | kPa | 178.38 | Calculated Property |
| Pvap | 0.28 | kPa | 218.46 | Calculated Property |
| Pvap | 4.77 | kPa | 258.53 | Calculated Property |
| Pvap | 33.13 | kPa | 298.61 | Calculated Property |
| Pvap | 134.74 | kPa | 338.69 | Calculated Property |
| Pvap | 389.63 | kPa | 378.77 | Calculated Property |
| Pvap | 900.61 | kPa | 418.84 | Calculated Property |
| Pvap | 1792.06 | kPa | 458.92 | Calculated Property |
| Pvap | 3223.80 | kPa | 499.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [798.67; 405.01] | kg/m3 | [138.30; 480.02] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 6.54702e+01 | |||
| Coefficient B | 2.70170e-01 | |||
| Coefficient C | 4.99000e+02 | |||
| Coefficient D | 2.86100e-01 | |||
| Temperature range, min. | 138.30 | |||
| Temperature range, max. | 480.02 | |||
| ρl | 798.67 | kg/m3 | 138.30 | Calculated Property |
| ρl | 769.39 | kg/m3 | 176.27 | Calculated Property |
| ρl | 738.75 | kg/m3 | 214.24 | Calculated Property |
| ρl | 706.44 | kg/m3 | 252.21 | Calculated Property |
| ρl | 672.03 | kg/m3 | 290.18 | Calculated Property |
| ρl | 634.85 | kg/m3 | 328.14 | Calculated Property |
| ρl | 593.82 | kg/m3 | 366.11 | Calculated Property |
| ρl | 546.93 | kg/m3 | 404.08 | Calculated Property |
| ρl | 489.62 | kg/m3 | 442.05 | Calculated Property |
| ρl | 405.01 | kg/m3 | 480.02 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 7.21e-04] | N/m | [138.30; 480.02] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K | |||
| Coefficient A | -1.15980e-02 | |||
| Coefficient B | 2.01020e+01 | |||
| Coefficient C | -3.09080e+00 | |||
| Coefficient D | -3.86660e-04 | |||
| Coefficient E | -5.04320e-06 | |||
| Temperature range, min. | 138.30 | |||
| Temperature range, max. | 480.02 | |||
| γ | 0.03 | N/m | 138.30 | Calculated Property |
| γ | 0.03 | N/m | 176.27 | Calculated Property |
| γ | 0.02 | N/m | 214.24 | Calculated Property |
| γ | 0.02 | N/m | 252.21 | Calculated Property |
| γ | 0.02 | N/m | 290.18 | Calculated Property |
| γ | 0.01 | N/m | 328.14 | Calculated Property |
| γ | 0.01 | N/m | 366.11 | Calculated Property |
| γ | 0.01 | N/m | 404.08 | Calculated Property |
| γ | 0.00 | N/m | 442.05 | Calculated Property |
| γ | 7.21e-04 | N/m | 480.02 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.00; 0.10] | W/m×K | [138.30; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | 5.25160e-05 | |||
| Coefficient B | 1.09780e+00 | |||
| Coefficient C | -6.08830e+01 | |||
| Coefficient D | 1.28130e+05 | |||
| Temperature range, min. | 138.30 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.00 | W/m×K | 138.30 | Calculated Property |
| λgas | 0.01 | W/m×K | 234.04 | Calculated Property |
| λgas | 0.02 | W/m×K | 329.79 | Calculated Property |
| λgas | 0.03 | W/m×K | 425.53 | Calculated Property |
| λgas | 0.04 | W/m×K | 521.28 | Calculated Property |
| λgas | 0.05 | W/m×K | 617.02 | Calculated Property |
| λgas | 0.06 | W/m×K | 712.77 | Calculated Property |
| λgas | 0.07 | W/m×K | 808.51 | Calculated Property |
| λgas | 0.08 | W/m×K | 904.26 | Calculated Property |
| λgas | 0.10 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.15; 0.10] | W/m×K | [138.30; 329.53] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K | |||
| Coefficient A | -5.08680e-02 | |||
| Coefficient B | 4.05530e+00 | |||
| Coefficient C | -1.55400e+00 | |||
| Coefficient D | -4.59680e-04 | |||
| Coefficient E | -1.98100e-06 | |||
| Temperature range, min. | 138.30 | |||
| Temperature range, max. | 329.53 | |||
| λliquid | 0.15 | W/m×K | 138.30 | Calculated Property |
| λliquid | 0.14 | W/m×K | 159.55 | Calculated Property |
| λliquid | 0.14 | W/m×K | 180.80 | Calculated Property |
| λliquid | 0.13 | W/m×K | 202.04 | Calculated Property |
| λliquid | 0.13 | W/m×K | 223.29 | Calculated Property |
| λliquid | 0.12 | W/m×K | 244.54 | Calculated Property |
| λliquid | 0.11 | W/m×K | 265.79 | Calculated Property |
| λliquid | 0.11 | W/m×K | 287.03 | Calculated Property |
| λliquid | 0.10 | W/m×K | 308.28 | Calculated Property |
| λliquid | 0.10 | W/m×K | 329.53 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Pentene, 4-methyl-, (Z)-.
Sources
- KDB Vapor Pressure Data
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- Crippen Method
- Crippen Method
- Gas-Liquid Critical Temperatures of Some Alkenes, Amines, and Cyclic Hydrocarbons
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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