- InChI
- InChI=1S/C14H28/c1-3-5-7-9-11-13-14-12-10-8-6-4-2/h3H,1,4-14H2,2H3
- InChI Key
- HFDVRLIODXPAHB-UHFFFAOYSA-N
- Formula
- C14H28
- SMILES
- C=CCCCCCCCCCCCC
- Molecular Weight1
- 196.37
- CAS
- 1120-36-1
- Other Names
-
- Neodene 14
- Tetradec-1-ene
- Tetradecene-1
- n-Tetradec-1-ene
- «alpha»-Tetradecene
- 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).
- 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).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- λ : Gas thermal conductivity (W/m×K).
- λ : 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.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.6440; 0.6503] |
|
|
| ω | 0.6503 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.6440 | KDB | |
| μ | 0.51 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | [154.90; 154.90] | kJ/mol |
|
| ΔfG° | 154.90 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | 154.90 | kJ/mol | KDB |
| ΔfH°gas | [-206.80; -206.70] | kJ/mol |
|
| ΔfH°gas | -206.80 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -206.70 | kJ/mol | KDB |
| ΔfusH° | 30.74 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 70.20 | kJ/mol | NIST |
| IE | 9.45 | eV | Relay (1.0) Calculated Property |
| log10WS | -6.66 | Relay (1.0) Calculated Property | |
| logPoct/wat | 5.483 | Crippen Calculated Property | |
| McVol | 203.820 | ml/mol | McGowan Calculated Property |
| Pc | [1560.00; 1627.00] | kPa |
|
| Pc | 1627.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 1560.00 | kPa | KDB |
| Ptriple | 3.87e-05 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [238.00; 1400.00] |
|
|
| Inp | 1383.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1390.00 | NIST | |
| Inp | 1390.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1387.90 | NIST | |
| Inp | 1390.00 | NIST | |
| Inp | 1383.40 | NIST | |
| Inp | 1383.00 | NIST | |
| Inp | 1384.00 | NIST | |
| Inp | 1390.00 | NIST | |
| Inp | 1390.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1393.00 | NIST | |
| Inp | 1393.00 | NIST | |
| Inp | 1391.00 | NIST | |
| Inp | 1391.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1385.00 | NIST | |
| Inp | 1391.70 | NIST | |
| Inp | 1391.40 | NIST | |
| Inp | 1392.20 | NIST | |
| Inp | 1391.20 | NIST | |
| Inp | 1392.00 | NIST | |
| Inp | 1398.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1390.00 | NIST | |
| Inp | 1391.70 | NIST | |
| Inp | 1391.40 | NIST | |
| Inp | 1392.20 | NIST | |
| Inp | 1390.00 | NIST | |
| Inp | 1389.08 | NIST | |
| Inp | 1389.35 | NIST | |
| Inp | 1389.46 | NIST | |
| Inp | 1392.25 | NIST | |
| Inp | 1392.49 | NIST | |
| Inp | 1392.68 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1390.00 | NIST | |
| Inp | 1391.00 | NIST | |
| Inp | 1392.00 | NIST | |
| Inp | 1393.00 | NIST | |
| Inp | 1392.00 | NIST | |
| Inp | 1392.00 | NIST | |
| Inp | 1394.00 | NIST | |
| Inp | 1396.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1390.00 | NIST | |
| Inp | 1390.00 | NIST | |
| Inp | 1393.50 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1391.00 | NIST | |
| Inp | 1392.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1394.00 | NIST | |
| Inp | 1395.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1396.00 | NIST | |
| Inp | 1400.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1395.00 | NIST | |
| Inp | 1394.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1387.00 | NIST | |
| Inp | 1397.00 | NIST | |
| Inp | 1397.00 | NIST | |
| Inp | 1392.00 | NIST | |
| Inp | 1392.00 | NIST | |
| Inp | 1391.00 | NIST | |
| Inp | 1394.00 | NIST | |
| Inp | 1383.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | Outlier 238.00 | NIST | |
| Inp | 1390.00 | NIST | |
| Inp | 1393.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1391.20 | NIST | |
| Inp | 1391.70 | NIST | |
| Inp | 1389.35 | NIST | |
| Inp | 1392.00 | NIST | |
| Inp | 1396.00 | NIST | |
| Inp | 1395.00 | NIST | |
| Inp | 1387.00 | NIST | |
| Inp | 1397.00 | NIST | |
| Inp | 1394.00 | NIST | |
| I | [1428.00; 1474.00] |
|
|
| I | 1436.30 | NIST | |
| I | 1443.60 | NIST | |
| I | 1444.30 | NIST | |
| I | Outlier 1474.00 | NIST | |
| I | 1454.00 | NIST | |
| I | 1434.00 | NIST | |
| I | 1441.00 | NIST | |
| I | 1442.00 | NIST | |
| I | 1442.00 | NIST | |
| I | 1435.00 | NIST | |
| I | 1442.00 | NIST | |
| I | 1443.00 | NIST | |
| I | 1443.00 | NIST | |
| I | 1436.00 | NIST | |
| I | 1443.00 | NIST | |
| I | 1443.00 | NIST | |
| I | 1451.00 | NIST | |
| I | 1452.00 | NIST | |
| I | 1452.00 | NIST | |
| I | 1453.00 | NIST | |
| I | 1454.00 | NIST | |
| I | 1447.00 | NIST | |
| I | 1448.00 | NIST | |
| I | 1448.00 | NIST | |
| I | 1449.00 | NIST | |
| I | 1449.00 | NIST | |
| I | 1431.90 | NIST | |
| I | 1442.10 | NIST | |
| I | 1433.90 | NIST | |
| I | 1442.60 | NIST | |
| I | 1428.70 | NIST | |
| I | 1433.50 | NIST | |
| I | 1440.90 | NIST | |
| I | 1441.90 | NIST | |
| I | 1431.40 | NIST | |
| I | 1434.70 | NIST | |
| I | 1441.70 | NIST | |
| I | 1442.90 | NIST | |
| I | 1451.00 | NIST | |
| I | 1452.00 | NIST | |
| I | 1453.00 | NIST | |
| I | 1454.00 | NIST | |
| I | 1428.00 | NIST | |
| I | 1444.00 | NIST | |
| I | 1446.00 | NIST | |
| I | 1429.00 | NIST | |
| I | 1433.00 | NIST | |
| I | 1454.00 | NIST | |
| I | 1443.00 | NIST | |
| I | 1443.00 | NIST | |
| I | 1428.00 | NIST | |
| I | 1436.30 | NIST | |
| I | 1434.00 | NIST | |
| I | 1442.00 | NIST | |
| I | 1443.00 | NIST | |
| I | 1454.00 | NIST | |
| I | 1449.00 | NIST | |
| I | 1428.70 | NIST | |
| I | 1434.70 | NIST | |
| I | 1453.00 | NIST | |
| Tboil | [524.00; 524.30] | K |
|
| Tboil | 524.25 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 524.30 | K | KDB |
| Tboil | 524.20 | K | NIST |
| Tboil | 524.00 | K | NIST |
| Tc | [689.00; 691.00] | K |
|
| Tc | 691.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 689.00 | K | KDB |
| Tfus | [260.00; 260.30] | K |
|
| Tfus | 260.30 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | Outlier 260.00 | K | KDB |
| Tfus | 260.23 ± 0.06 | K | NIST |
| Tfus | 260.23 ± 0.06 | K | NIST |
| Tfus | 260.30 ± 0.04 | K | NIST |
| Tfus | 260.23 ± 0.05 | K | NIST |
| Tfus | 260.30 ± 0.03 | K | NIST |
| Ttriple | 260.30 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 7.96 | ChemSep v8.3 pure component data Compiled value | |
| URi | 9.66 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.800; 0.865] | m3/kmol |
|
| Vc | 0.865 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.800 | m3/kmol | KDB |
| Zc | [0.2179870; 0.2450000] |
|
|
| Zc | 0.2450000 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.2179870 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [46.90; 56.50] | kJ/mol | [478.50; 524.30] |
|
| ΔvapH | 56.50 | kJ/mol | 478.50 | NIST |
| ΔvapH | 46.90 | kJ/mol | 524.30 | KDB |
| ρl | 786.00 | kg/m3 | 273.00 | KDB |
| γ | 0.03 | N/m | 298.20 | KDB |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 398.20 | K | 2.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [284.63; 815.35] | J/mol×K | [260.30; 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 | 1.89945e+02 | |||
| Coefficient B | -6.10915e+02 | |||
| Coefficient C | 6.91204e+00 | |||
| Coefficient D | -5.81323e-05 | |||
| Coefficient E | 9.25678e-09 | |||
| Comment | ChemSep eq 16, IdealGasHeatCapacityCp | |||
| Temperature range, min. | 260.30 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 284.63 | J/mol×K | 260.30 | Calculated Property |
| Cp,gas | 401.73 | J/mol×K | 398.04 | Calculated Property |
| Cp,gas | 502.05 | J/mol×K | 535.79 | Calculated Property |
| Cp,gas | 581.47 | J/mol×K | 673.53 | Calculated Property |
| Cp,gas | 643.88 | J/mol×K | 811.28 | Calculated Property |
| Cp,gas | 693.39 | J/mol×K | 949.02 | Calculated Property |
| Cp,gas | 733.24 | J/mol×K | 1086.77 | Calculated Property |
| Cp,gas | 765.79 | J/mol×K | 1224.51 | Calculated Property |
| Cp,gas | 792.74 | J/mol×K | 1362.26 | Calculated Property |
| Cp,gas | 815.35 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [400.80; 603.57] | J/mol×K | [260.30; 553.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 2.80190e+02 | |||
| Coefficient B | 3.55370e-01 | |||
| Coefficient C | 4.14840e-04 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 100, LiquidHeatCapacityCp | |||
| Temperature range, min. | 260.30 | |||
| Temperature range, max. | 553.00 | |||
| Cp,liquid | 400.80 | J/mol×K | 260.30 | Calculated Property |
| Cp,liquid | 419.82 | J/mol×K | 292.82 | Calculated Property |
| Cp,liquid | 439.72 | J/mol×K | 325.34 | Calculated Property |
| Cp,liquid | 460.49 | J/mol×K | 357.87 | Calculated Property |
| Cp,liquid | 482.15 | J/mol×K | 390.39 | Calculated Property |
| Cp,liquid | 504.68 | J/mol×K | 422.91 | Calculated Property |
| Cp,liquid | 528.08 | J/mol×K | 455.43 | Calculated Property |
| Cp,liquid | 552.37 | J/mol×K | 487.96 | Calculated Property |
| Cp,liquid | 577.53 | J/mol×K | 520.48 | Calculated Property |
| Cp,liquid | 603.57 | J/mol×K | 553.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0041367; 0.0001547] | Pa×s | [260.30; 552.80] |
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 | -1.16980e+01 | |||
| Coefficient B | 1.61650e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 101, LiquidViscosity | |||
| Temperature range, min. | 260.30 | |||
| Temperature range, max. | 552.80 | |||
| η | 0.0041367 | Pa×s | 260.30 | Calculated Property |
| η | 0.0020763 | Pa×s | 292.80 | Calculated Property |
| η | 0.0011960 | Pa×s | 325.30 | Calculated Property |
| η | 0.0007616 | Pa×s | 357.80 | Calculated Property |
| η | 0.0005228 | Pa×s | 390.30 | Calculated Property |
| η | 0.0003803 | Pa×s | 422.80 | Calculated Property |
| η | 0.0002894 | Pa×s | 455.30 | Calculated Property |
| η | 0.0002285 | Pa×s | 487.80 | Calculated Property |
| η | 0.0001857 | Pa×s | 520.30 | Calculated Property |
| η | 0.0001547 | Pa×s | 552.80 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [71.65; 0.00] | kJ/mol | [260.30; 691.00] |
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 | 9.38100e+01 | |||
| Coefficient B | 6.91450e-01 | |||
| Coefficient C | -3.45440e-01 | |||
| Coefficient D | 6.09460e-02 | |||
| Coefficient E | 1.00000e-03 | |||
| Critical temperature, Tc (K) | 6.91000e+02 | |||
| Comment | ChemSep eq 106, HeatOfVaporization | |||
| Temperature range, min. | 260.30 | |||
| Temperature range, max. | 691.00 | |||
| ΔvapH | 71.65 | kJ/mol | 260.30 | Calculated Property |
| ΔvapH | 67.81 | kJ/mol | 308.16 | Calculated Property |
| ΔvapH | 63.92 | kJ/mol | 356.01 | Calculated Property |
| ΔvapH | 59.91 | kJ/mol | 403.87 | Calculated Property |
| ΔvapH | 55.68 | kJ/mol | 451.72 | Calculated Property |
| ΔvapH | 51.05 | kJ/mol | 499.58 | Calculated Property |
| ΔvapH | 45.78 | kJ/mol | 547.43 | Calculated Property |
| ΔvapH | 39.33 | kJ/mol | 595.29 | Calculated Property |
| ΔvapH | 30.28 | kJ/mol | 643.14 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 691.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [392.67; 556.48] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.47321e+01 | |||
| Coefficient B | -4.43698e+03 | |||
| Coefficient C | -8.54930e+01 | |||
| Temperature range, min. | 392.67 | |||
| Temperature range, max. | 556.48 | |||
| Pvap | 1.33 | kPa | 392.67 | Calculated Property |
| Pvap | 2.99 | kPa | 410.87 | Calculated Property |
| Pvap | 6.16 | kPa | 429.07 | Calculated Property |
| Pvap | 11.80 | kPa | 447.27 | Calculated Property |
| Pvap | 21.23 | kPa | 465.47 | Calculated Property |
| Pvap | 36.20 | kPa | 483.68 | Calculated Property |
| Pvap | 58.92 | kPa | 501.88 | Calculated Property |
| Pvap | 92.06 | kPa | 520.08 | Calculated Property |
| Pvap | 138.77 | kPa | 538.28 | Calculated Property |
| Pvap | 202.66 | kPa | 556.48 | Calculated Property |
| Pvap | [3.87e-05; 1626.98] | kPa | [260.30; 691.00] |
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 | 8.78172e+01 | |||
| Coefficient B | -1.11780e+04 | |||
| Coefficient C | -9.89510e+00 | |||
| Coefficient D | 4.12770e-18 | |||
| Coefficient E | 6.00000e+00 | |||
| Comment | ChemSep eq 101, VaporPressure | |||
| Temperature range, min. | 260.30 | |||
| Temperature range, max. | 691.00 | |||
| Pvap | 3.87e-05 | kPa | 260.30 | Calculated Property |
| Pvap | 5.75e-03 | kPa | 308.16 | Calculated Property |
| Pvap | 0.18 | kPa | 356.01 | Calculated Property |
| Pvap | 2.17 | kPa | 403.87 | Calculated Property |
| Pvap | 13.70 | kPa | 451.72 | Calculated Property |
| Pvap | 55.74 | kPa | 499.58 | Calculated Property |
| Pvap | 167.07 | kPa | 547.43 | Calculated Property |
| Pvap | 404.74 | kPa | 595.29 | Calculated Property |
| Pvap | 848.75 | kPa | 643.14 | Calculated Property |
| Pvap | 1626.98 | kPa | 691.00 | Calculated Property |
| Pvap | [2.41e-05; 1671.79] | kPa | [260.30; 692.00] |
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 | 1.63674e+02 | |||
| Coefficient B | -1.45730e+04 | |||
| Coefficient C | -2.13939e+01 | |||
| Coefficient D | 9.84515e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 260.30 | |||
| Temperature range, max. | 692.00 | |||
| Pvap | 2.41e-05 | kPa | 260.30 | Calculated Property |
| Pvap | 5.13e-03 | kPa | 308.27 | Calculated Property |
| Pvap | 0.19 | kPa | 356.23 | Calculated Property |
| Pvap | 2.28 | kPa | 404.20 | Calculated Property |
| Pvap | 14.21 | kPa | 452.17 | Calculated Property |
| Pvap | 56.69 | kPa | 500.13 | Calculated Property |
| Pvap | 167.89 | kPa | 548.10 | Calculated Property |
| Pvap | 406.84 | kPa | 596.07 | Calculated Property |
| Pvap | 861.87 | kPa | 644.03 | Calculated Property |
| Pvap | 1671.79 | kPa | 692.00 | Calculated Property |
| Pvap | [6.92; 102.82] | kPa | [431.61; 524.90] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.41493e+01 | |||
| Coefficient B | -4.01801e+03 | |||
| Coefficient C | -1.02675e+02 | |||
| Reference | Camin and Rossini, 1955 | |||
| Temperature range, min. | 431.61 | |||
| Temperature range, max. | 524.90 | |||
| Pvap | 6.92 | kPa | 431.61 | Calculated Property |
| Pvap | 10.05 | kPa | 441.98 | Calculated Property |
| Pvap | 14.27 | kPa | 452.34 | Calculated Property |
| Pvap | 19.87 | kPa | 462.71 | Calculated Property |
| Pvap | 27.15 | kPa | 473.07 | Calculated Property |
| Pvap | 36.48 | kPa | 483.44 | Calculated Property |
| Pvap | 48.25 | kPa | 493.80 | Calculated Property |
| Pvap | 62.90 | kPa | 504.17 | Calculated Property |
| Pvap | 80.92 | kPa | 514.53 | Calculated Property |
| Pvap | 102.82 | kPa | 524.90 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [793.71; 226.96] | kg/m3 | [260.30; 691.00] |
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 | 5.41496e+01 | |||
| Coefficient B | 2.38590e-01 | |||
| Coefficient C | 6.91000e+02 | |||
| Coefficient D | 2.85710e-01 | |||
| Comment | ChemSep eq 105, LiquidDensity | |||
| Temperature range, min. | 260.30 | |||
| Temperature range, max. | 691.00 | |||
| ρl | 793.71 | kg/m3 | 260.30 | Calculated Property |
| ρl | 761.50 | kg/m3 | 308.16 | Calculated Property |
| ρl | 727.77 | kg/m3 | 356.01 | Calculated Property |
| ρl | 692.13 | kg/m3 | 403.87 | Calculated Property |
| ρl | 654.05 | kg/m3 | 451.72 | Calculated Property |
| ρl | 612.66 | kg/m3 | 499.58 | Calculated Property |
| ρl | 566.48 | kg/m3 | 547.43 | Calculated Property |
| ρl | 512.55 | kg/m3 | 595.29 | Calculated Property |
| ρl | 442.76 | kg/m3 | 643.14 | Calculated Property |
| ρl | 226.96 | kg/m3 | 691.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 0.00] | N/m | [260.30; 691.00] |
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 γ in N/m, T in K | |||
| Coefficient A | 5.61270e-02 | |||
| Coefficient B | 1.33930e+00 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 1.00000e-07 | |||
| Critical temperature, Tc (K) | 6.91000e+02 | |||
| Comment | ChemSep eq 106, SurfaceTension | |||
| Temperature range, min. | 260.30 | |||
| Temperature range, max. | 691.00 | |||
| γ | 0.03 | N/m | 260.30 | Calculated Property |
| γ | 0.03 | N/m | 308.16 | Calculated Property |
| γ | 0.02 | N/m | 356.01 | Calculated Property |
| γ | 0.02 | N/m | 403.87 | Calculated Property |
| γ | 0.01 | N/m | 451.72 | Calculated Property |
| γ | 0.01 | N/m | 499.58 | Calculated Property |
| γ | 0.01 | N/m | 547.43 | Calculated Property |
| γ | 0.00 | N/m | 595.29 | Calculated Property |
| γ | 0.00 | N/m | 643.14 | Calculated Property |
| γ | 0.00 | N/m | 691.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.02; 0.08] | W/m×K | [524.25; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λ in W/m×K, T in K | |||
| Coefficient A | 4.29410e-05 | |||
| Coefficient B | 1.18080e+00 | |||
| Coefficient C | 8.84430e+02 | |||
| Coefficient D | 9.90600e+04 | |||
| Comment | ChemSep eq 102, VaporThermalConductivity | |||
| Temperature range, min. | 524.25 | |||
| Temperature range, max. | 1000.00 | |||
| λ | 0.02 | W/m×K | 524.25 | Calculated Property |
| λ | 0.03 | W/m×K | 577.11 | Calculated Property |
| λ | 0.03 | W/m×K | 629.97 | Calculated Property |
| λ | 0.04 | W/m×K | 682.83 | Calculated Property |
| λ | 0.04 | W/m×K | 735.69 | Calculated Property |
| λ | 0.05 | W/m×K | 788.56 | Calculated Property |
| λ | 0.06 | W/m×K | 841.42 | Calculated Property |
| λ | 0.06 | W/m×K | 894.28 | Calculated Property |
| λ | 0.07 | W/m×K | 947.14 | Calculated Property |
| λ | 0.08 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.15; 0.10] | W/m×K | [260.30; 524.25] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λ in W/m×K, T in K | |||
| Coefficient A | 1.94390e-01 | |||
| Coefficient B | -1.84130e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 100, LiquidThermalConductivity | |||
| Temperature range, min. | 260.30 | |||
| Temperature range, max. | 524.25 | |||
| λ | 0.15 | W/m×K | 260.30 | Calculated Property |
| λ | 0.14 | W/m×K | 289.63 | Calculated Property |
| λ | 0.14 | W/m×K | 318.96 | Calculated Property |
| λ | 0.13 | W/m×K | 348.28 | Calculated Property |
| λ | 0.12 | W/m×K | 377.61 | Calculated Property |
| λ | 0.12 | W/m×K | 406.94 | Calculated Property |
| λ | 0.11 | W/m×K | 436.27 | Calculated Property |
| λ | 0.11 | W/m×K | 465.59 | Calculated Property |
| λ | 0.10 | W/m×K | 494.92 | Calculated Property |
| λ | 0.10 | W/m×K | 524.25 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Tetradecene.
Sources
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- 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
- Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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