- InChI
- InChI=1S/C6H11I/c1-2-3-4-5-6-7/h5-6H,2-4H2,1H3
- InChI Key
- TUAPXMNNQGXDDV-WAYWQWQTSA-N
- Formula
- C6H11I
- SMILES
- CCCC/C=C\I
- Molecular Weight1
- 210.06
- CAS
- 16538-47-9
- Other Names
-
- cis-1-Iodo-1-Hexene
- cis-1-Iodohexene
- 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).
- 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 | 0.2731 | Relay (1.0) Calculated Property | |
| ΔfG° | 137.98 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | 22.62 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 15.90 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 48.72 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 8.92 | eV | Relay (1.0) Calculated Property |
| log10WS | -4.41 | Relay (1.0) Calculated Property | |
| logPoct/wat | 3.125 | Crippen Calculated Property | |
| McVol | 116.920 | ml/mol | McGowan Calculated Property |
| Pc | 3213.68 | kPa | Joback Calculated Property |
| Tboil | 436.79 | K | Relay (1.0) Calculated Property |
| Tc | 651.70 | K | Relay (1.0) Calculated Property |
| Tfus | 164.87 | K | Relay (1.0) Calculated Property |
| Vc | 0.412 | m3/kmol | Relay (1.0) Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [135.84; 307.46] | 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 | -5.05700e+00 | |||
| Coefficient B | 6.32820e-01 | |||
| Coefficient C | -4.67800e-04 | |||
| Coefficient D | 1.47500e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 135.84 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 166.80 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 193.70 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 217.01 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 237.19 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 254.70 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 270.02 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 283.61 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 295.93 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 307.46 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0058545; 0.0002732] | Pa×s | [210.36; 451.54] |
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 | -1.08786e+01 | |||
| Coefficient B | 1.20706e+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. | 210.36 | |||
| Temperature range, max. | 451.54 | |||
| η | 0.0058545 | Pa×s | 210.36 | Calculated Property |
| η | 0.0030613 | Pa×s | 237.16 | Calculated Property |
| η | 0.0018260 | Pa×s | 263.96 | Calculated Property |
| η | 0.0011980 | Pa×s | 290.75 | Calculated Property |
| η | 0.0008439 | Pa×s | 317.55 | Calculated Property |
| η | 0.0006278 | Pa×s | 344.35 | Calculated Property |
| η | 0.0004874 | Pa×s | 371.15 | Calculated Property |
| η | 0.0003916 | Pa×s | 397.94 | Calculated Property |
| η | 0.0003234 | Pa×s | 424.74 | Calculated Property |
| η | 0.0002732 | Pa×s | 451.54 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [337.32; 444.28] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.81197e+01 | |||
| Coefficient B | -4.86276e+03 | |||
| Coefficient C | -6.46240e+01 | |||
| Temperature range, min. | 337.32 | |||
| Temperature range, max. | 444.28 | |||
| Pvap | 1.33 | kPa | 337.32 | Calculated Property |
| Pvap | 2.81 | kPa | 349.20 | Calculated Property |
| Pvap | 5.57 | kPa | 361.09 | Calculated Property |
| Pvap | 10.48 | kPa | 372.97 | Calculated Property |
| Pvap | 18.82 | kPa | 384.86 | Calculated Property |
| Pvap | 32.40 | kPa | 396.74 | Calculated Property |
| Pvap | 53.73 | kPa | 408.63 | Calculated Property |
| Pvap | 86.14 | kPa | 420.51 | Calculated Property |
| Pvap | 133.96 | kPa | 432.40 | Calculated Property |
| Pvap | 202.64 | kPa | 444.28 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Hexene, 1-iodo-, (Z)-.
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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