- InChI
- InChI=1S/C8H17N/c1-9(2)8-6-4-3-5-7-8/h8H,3-7H2,1-2H3
- InChI Key
- SVYKKECYCPFKGB-UHFFFAOYSA-N
- Formula
- C8H17N
- SMILES
- CN(C)C1CCCCC1
- Molecular Weight1
- 127.23
- CAS
- 98-94-2
- Other Names
-
- (Dimethylamino)cyclohexane
- Cyclohexylamine, N,N-dimethyl-
- Cyclohexyldimethylamine
- Dimethylcyclohexylamine
- N,N-Dimethyl-N-cyclohexylamine
- N,N-Dimethylaminocyclohexane
- N,N-Dimethylcyclohexanamine
- N,N-Dimethylcyclohexylamine
- N-Cyclohexyldimethylamine
- NSC 163904
- Polycat 8
- UN 2264
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- ΔfG° : Standard Gibbs free energy of formation (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).
- 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).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- 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 |
|---|---|---|---|
| PAff | 983.60 | kJ/mol | NIST |
| BasG | 952.60 | kJ/mol | NIST |
| ΔcH°liquid | -5442.80 ± 2.00 | kJ/mol | NIST |
| ΔfG° | 151.71 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -86.60 | kJ/mol | Joback Calculated Property |
| ΔfH°liquid | -134.80 ± 2.00 | kJ/mol | NIST |
| ΔfusH° | 11.33 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 35.87 | kJ/mol | Joback Calculated Property |
| IE | [7.50; 8.09] | eV |
|
| IE | 7.50 | eV | NIST |
| IE | 8.09 | eV | NIST |
| log10WS | -1.75 | Crippen Calculated Property | |
| logPoct/wat | 1.881 | Crippen Calculated Property | |
| McVol | 122.700 | ml/mol | McGowan Calculated Property |
| Pc | 3145.56 | kPa | Joback Calculated Property |
| Inp | [994.00; 995.00] |
|
|
| Inp | 995.00 | NIST | |
| Inp | 994.00 | NIST | |
| Inp | 995.00 | NIST | |
| Tboil | 431.70 | K | NIST |
| Tc | 613.03 | K | Joback Calculated Property |
| Tfus | 219.77 | K | Joback Calculated Property |
| Vc | 0.434 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [243.24; 341.20] | J/mol×K | [414.43; 613.03] |
|
| Cp,gas | 243.24 | J/mol×K | 414.43 | Joback Calculated Property |
| Cp,gas | 261.82 | J/mol×K | 447.53 | Joback Calculated Property |
| Cp,gas | 279.47 | J/mol×K | 480.63 | Joback Calculated Property |
| Cp,gas | 296.20 | J/mol×K | 513.73 | Joback Calculated Property |
| Cp,gas | 312.04 | J/mol×K | 546.83 | Joback Calculated Property |
| Cp,gas | 327.04 | J/mol×K | 579.93 | Joback Calculated Property |
| Cp,gas | 341.20 | J/mol×K | 613.03 | Joback Calculated Property |
| Pvap | [0.09; 1.11] | kPa | [275.30; 314.30] |
|
| Pvap | 0.09 | kPa | 275.30 | Thermod... |
| Pvap | 0.09 | kPa | 275.30 | Thermod... |
| Pvap | 0.09 | kPa | 275.40 | Thermod... |
| Pvap | 0.11 | kPa | 278.30 | Thermod... |
| Pvap | 0.15 | kPa | 281.20 | Thermod... |
| Pvap | 0.18 | kPa | 284.20 | Thermod... |
| Pvap | 0.21 | kPa | 287.20 | Thermod... |
| Pvap | 0.26 | kPa | 290.30 | Thermod... |
| Pvap | 0.32 | kPa | 293.20 | Thermod... |
| Pvap | 0.38 | kPa | 296.20 | Thermod... |
| Pvap | 0.47 | kPa | 299.20 | Thermod... |
| Pvap | 0.57 | kPa | 302.20 | Thermod... |
| Pvap | 0.66 | kPa | 305.30 | Thermod... |
| Pvap | 0.81 | kPa | 308.30 | Thermod... |
| Pvap | 0.91 | kPa | 311.20 | Thermod... |
| Pvap | 1.11 | kPa | 314.30 | Thermod... |
| ρl | [844.00; 856.40] | kg/m3 | [283.15; 308.15] |
|
| ρl | 856.40 | kg/m3 | 283.15 | Physico... |
| ρl | 854.00 | kg/m3 | 288.15 | Physico... |
| ρl | 851.50 | kg/m3 | 293.15 | Physico... |
| ρl | 849.10 | kg/m3 | 298.15 | Physico... |
| ρl | 846.50 | kg/m3 | 303.15 | Physico... |
| ρl | 844.00 | kg/m3 | 308.15 | Physico... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [321.12; 458.81] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.47617e+01 | |||
| Coefficient B | -3.74877e+03 | |||
| Coefficient C | -6.21220e+01 | |||
| Temperature range, min. | 321.12 | |||
| Temperature range, max. | 458.81 | |||
| Pvap | 1.33 | kPa | 321.12 | Calculated Property |
| Pvap | 2.99 | kPa | 336.42 | Calculated Property |
| Pvap | 6.15 | kPa | 351.72 | Calculated Property |
| Pvap | 11.78 | kPa | 367.02 | Calculated Property |
| Pvap | 21.20 | kPa | 382.32 | Calculated Property |
| Pvap | 36.15 | kPa | 397.61 | Calculated Property |
| Pvap | 58.86 | kPa | 412.91 | Calculated Property |
| Pvap | 91.99 | kPa | 428.21 | Calculated Property |
| Pvap | 138.72 | kPa | 443.51 | Calculated Property |
| Pvap | 202.66 | kPa | 458.81 | Calculated Property |
Similar Compounds
![9-Azabicyclo[3.3.1]nonane,9-methyl-.](data:image/png;base64,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)
Find more compounds similar to Cyclohexanamine, N,N-dimethyl-.
Mixtures
- Carbon dioxide + Cyclohexanamine, N,N-dimethyl- + Water
- Toluene + Cyclohexanamine, N,N-dimethyl- + Water
Sources
- Crippen Method
- Crippen Method
- Non-random two-liquid modelling of switchable-hydrophilicity solvent systems: N,N-Dimethylcyclohexanamine, water, and toluene
- Physicochemical properties of switchable-hydrophilicity solvent systems: N,N-Dimethylcyclohexylamine, water and carbon dioxide
- Thermodynamic properties of cyclohexanamines: Experimental and theoretical study
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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