- InChI
- InChI=1S/C14H29I/c1-2-3-4-5-6-7-8-9-10-11-12-13-14-15/h2-14H2,1H3
- InChI Key
- FHQCFGPKNSSISL-UHFFFAOYSA-N
- Formula
- C14H29I
- SMILES
- CCCCCCCCCCCCCCI
- Molecular Weight1
- 324.29
- CAS
- 19218-94-1
- Other Names
-
- 1-Iodotetradecane
- Tetradecyl iodide
- ω : Acentric Factor.
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- 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).
- Pvap : Vapor pressure (kPa).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.6859 | Relay (1.0) Calculated Property | |
| ΔfG° | 125.12 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -274.31 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 36.42 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 90.00 | kJ/mol | NIST |
| IE | 9.21 | eV | Relay (1.0) Calculated Property |
| log10WS | -7.24 | Relay (1.0) Calculated Property | |
| logPoct/wat | 6.123 | Crippen Calculated Property | |
| McVol | 233.940 | ml/mol | McGowan Calculated Property |
| Pc | 1497.67 | kPa | Joback Calculated Property |
| Tboil | 583.56 | K | Relay (1.0) Calculated Property |
| Tc | 767.34 | K | Relay (1.0) Calculated Property |
| Tfus | 287.69 | K | Relay (1.0) Calculated Property |
| Vc | 0.913 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 68.60 | kJ/mol | 562.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [319.55; 750.77] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 1.85300e+00 | |||
| Coefficient B | 1.37282e+00 | |||
| Coefficient C | -8.19200e-04 | |||
| Coefficient D | 1.95300e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 319.55 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 393.64 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 459.75 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 518.49 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 570.47 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 616.33 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 656.67 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 692.11 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 723.27 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 750.77 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0042625; 0.0002273] | Pa×s | [305.60; 557.19] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.19504e+01 | |||
| Coefficient B | 1.98410e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 305.60 | |||
| Temperature range, max. | 557.19 | |||
| η | 0.0042625 | Pa×s | 305.60 | Calculated Property |
| η | 0.0024738 | Pa×s | 333.55 | Calculated Property |
| η | 0.0015617 | Pa×s | 361.51 | Calculated Property |
| η | 0.0010532 | Pa×s | 389.46 | Calculated Property |
| η | 0.0007488 | Pa×s | 417.42 | Calculated Property |
| η | 0.0005556 | Pa×s | 445.37 | Calculated Property |
| η | 0.0004271 | Pa×s | 473.32 | Calculated Property |
| η | 0.0003381 | Pa×s | 501.28 | Calculated Property |
| η | 0.0002743 | Pa×s | 529.23 | Calculated Property |
| η | 0.0002273 | Pa×s | 557.19 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [457.52; 612.25] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.66330e+01 | |||
| Coefficient B | -5.69956e+03 | |||
| Coefficient C | -1.08826e+02 | |||
| Temperature range, min. | 457.52 | |||
| Temperature range, max. | 612.25 | |||
| Pvap | 1.33 | kPa | 457.52 | Calculated Property |
| Pvap | 2.87 | kPa | 474.71 | Calculated Property |
| Pvap | 5.78 | kPa | 491.90 | Calculated Property |
| Pvap | 10.95 | kPa | 509.10 | Calculated Property |
| Pvap | 19.69 | kPa | 526.29 | Calculated Property |
| Pvap | 33.79 | kPa | 543.48 | Calculated Property |
| Pvap | 55.65 | kPa | 560.67 | Calculated Property |
| Pvap | 88.36 | kPa | 577.87 | Calculated Property |
| Pvap | 135.79 | kPa | 595.06 | Calculated Property |
| Pvap | 202.64 | kPa | 612.25 | Calculated Property |
Similar Compounds
Find more compounds similar to Tetradecane, 1-iodo-.
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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