- InChI
- InChI=1S/C12H20/c1-2-12-6-9-3-10(7-12)5-11(4-9)8-12/h9-11H,2-8H2,1H3
- InChI Key
- LXTHCCWEYOKFSR-UHFFFAOYSA-N
- Formula
- C12H20
- SMILES
- CCC12CC3CC(CC(C3)C1)C2
- Molecular Weight1
- 164.29
- CAS
- 770-69-4
- Other Names
-
- 1-ethyltricyclo[3.3.1.1(3,7)]decane
- 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).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- 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.
- I : 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 |
|---|---|---|---|
| ΔfG° | 207.11 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -83.87 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 13.91 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 55.30 ± 1.10 | kJ/mol | NIST |
| log10WS | -3.56 | Crippen Calculated Property | |
| logPoct/wat | 3.613 | Crippen Calculated Property | |
| McVol | 147.360 | ml/mol | McGowan Calculated Property |
| Pc | 2648.83 | kPa | Joback Calculated Property |
| Inp | [1234.00; 1309.00] |
|
|
| Inp | 1301.00 | NIST | |
| Inp | 1241.90 | NIST | |
| Inp | 1260.00 | NIST | |
| Inp | 1234.00 | NIST | |
| Inp | 1240.00 | NIST | |
| Inp | 1249.00 | NIST | |
| Inp | 1259.00 | NIST | |
| Inp | 1234.00 | NIST | |
| Inp | Outlier 1309.00 | NIST | |
| Inp | 1240.00 | NIST | |
| Inp | 1249.00 | NIST | |
| Inp | 1259.00 | NIST | |
| Inp | 1260.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | 1286.00 | NIST | |
| Inp | 1301.00 | NIST | |
| Inp | 1235.00 | NIST | |
| Inp | 1260.00 | NIST | |
| Inp | 1260.00 | NIST | |
| I | [1448.00; 1491.00] |
|
|
| I | 1448.00 | NIST | |
| I | 1469.00 | NIST | |
| I | 1491.00 | NIST | |
| Tboil | 494.02 | K | Joback Calculated Property |
| Tc | 710.60 | K | Joback Calculated Property |
| Tfus | 294.96 | K | Joback Calculated Property |
| Vc | 0.568 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [368.00; 479.81] | J/mol×K | [494.02; 710.60] |
|
| Cp,gas | 368.00 | J/mol×K | 494.02 | Joback Calculated Property |
| Cp,gas | 390.28 | J/mol×K | 530.12 | Joback Calculated Property |
| Cp,gas | 410.85 | J/mol×K | 566.21 | Joback Calculated Property |
| Cp,gas | 429.90 | J/mol×K | 602.31 | Joback Calculated Property |
| Cp,gas | 447.62 | J/mol×K | 638.41 | Joback Calculated Property |
| Cp,gas | 464.19 | J/mol×K | 674.50 | Joback Calculated Property |
| Cp,gas | 479.81 | J/mol×K | 710.60 | Joback Calculated Property |
| ΔfusH | 11.28 | kJ/mol | 190.50 | NIST |
| ΔvapH | 49.10 | kJ/mol | 437.50 | NIST |
| ρl | [908.41; 937.11] | kg/m3 | [293.15; 333.15] |
|
| ρl | 937.11 | kg/m3 | 293.15 | Density... |
| ρl | 933.58 | kg/m3 | 298.15 | Density... |
| ρl | 929.99 | kg/m3 | 303.15 | Density... |
| ρl | 926.40 | kg/m3 | 308.15 | Density... |
| ρl | 922.81 | kg/m3 | 313.15 | Density... |
| ρl | 919.21 | kg/m3 | 318.15 | Density... |
| ρl | 915.62 | kg/m3 | 323.15 | Density... |
| ρl | 912.01 | kg/m3 | 328.15 | Density... |
| ρl | 908.41 | kg/m3 | 333.15 | Density... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [359.25; 534.74] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.45208e+01 | |||
| Coefficient B | -4.57869e+03 | |||
| Coefficient C | -3.75610e+01 | |||
| Temperature range, min. | 359.25 | |||
| Temperature range, max. | 534.74 | |||
| Pvap | 1.33 | kPa | 359.25 | Calculated Property |
| Pvap | 3.01 | kPa | 378.75 | Calculated Property |
| Pvap | 6.21 | kPa | 398.25 | Calculated Property |
| Pvap | 11.91 | kPa | 417.75 | Calculated Property |
| Pvap | 21.44 | kPa | 437.25 | Calculated Property |
| Pvap | 36.52 | kPa | 456.74 | Calculated Property |
| Pvap | 59.35 | kPa | 476.24 | Calculated Property |
| Pvap | 92.54 | kPa | 495.74 | Calculated Property |
| Pvap | 139.15 | kPa | 515.24 | Calculated Property |
| Pvap | 202.65 | kPa | 534.74 | Calculated Property |
Similar Compounds
![Spiro[4.5]decane, 7-hexadecyl-.](data:image/png;base64,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)
Find more compounds similar to 1-Ethyladamantane.
Mixtures
Sources
- Crippen Method
- Crippen Method
- Density, Viscosity, Refractive Index, and Surface Tension for Six Binary Systems of Adamantane Derivatives with 1-Heptanol and Cyclohexylmethanol
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.