- InChI
- InChI=1S/C5H12S/c1-3-5-6-4-2/h3-5H2,1-2H3
- InChI Key
- ZDDDFDQTSXYYSE-UHFFFAOYSA-N
- Formula
- C5H12S
- SMILES
- CCCSCC
- Molecular Weight1
- 104.22
- CAS
- 4110-50-3
- Other Names
-
- 1-(Ethylthio)propane
- 3-Thiahexane
- ETHYL PROPYL THIO ETHER
- Ethyl n-propyl sulfide
- Ethyl propyl sulfide
- Ethyl propyl sulphide
- Ethyl propyl thioether
- Propyl ethyl sulfide
- Sulfide, ethyl propyl
- n-C3H7SC2H5
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- 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).
- 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).
- 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).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- VCOSTALD : COSTALD Characteristic Volume (m3/kmol).
- ωSRK : SRK acentric factor.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | [-4139.90; -4139.50] | kJ/mol |
|
| ΔcH°liquid | -4139.90 ± 0.59 | kJ/mol | NIST |
| ΔcH°liquid | -4139.50 ± 0.59 | kJ/mol | NIST |
| ΔfH°gas | [-104.70; -104.50] | kJ/mol |
|
| ΔfH°gas | -104.70 ± 0.79 | kJ/mol | NIST |
| ΔfH°gas | -104.50 | kJ/mol | NIST |
| ΔfH°liquid | [-144.80; -144.60] | kJ/mol |
|
| ΔfH°liquid | -144.80 ± 0.79 | kJ/mol | NIST |
| ΔfH°liquid | -144.60 ± 0.75 | kJ/mol | NIST |
| ΔfusH° | 12.84 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [39.50; 40.10] | kJ/mol |
|
| ΔvapH° | 40.01 | kJ/mol | NIST |
| ΔvapH° | Outlier 39.50 | kJ/mol | NIST |
| ΔvapH° | 40.00 | kJ/mol | NIST |
| ΔvapH° | 40.10 ± 0.04 | kJ/mol | NIST |
| ΔvapH° | 40.10 | kJ/mol | NIST |
| ΔvapH° | 40.08 | kJ/mol | NIST |
| IE | [8.37; 8.50] | eV |
|
| IE | 8.37 | eV | NIST |
| IE | 8.50 ± 0.05 | eV | NIST |
| log10WS | -2.16 | Relay (1.0) Calculated Property | |
| logPoct/wat | 2.150 | Crippen Calculated Property | |
| McVol | 97.660 | ml/mol | McGowan Calculated Property |
| Pc | 3538.87 | kPa | Joback Calculated Property |
| Inp | [782.00; 801.00] |
|
|
| Inp | 794.00 | NIST | |
| Inp | 794.00 | NIST | |
| Inp | 801.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 783.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 794.00 | NIST | |
| Ip | [1017.00; 1017.00] |
|
|
| Ip | 1017.00 | NIST | |
| Ip | 1017.00 | NIST | |
| S°liquid | 309.53 | J/mol×K | NIST |
| Tboil | [389.00; 391.70] | K |
|
| Tboil | 391.70 | K | NIST |
| Tboil | 391.70 | K | NIST |
| Tboil | 391.70 ± 0.30 | K | NIST |
| Tboil | 389.00 ± 3.00 | K | NIST |
| Tc | 583.21 | K | Relay (1.0) Calculated Property |
| Tfus | [156.11; 156.15] | K |
|
| Tfus | 156.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 156.11 ± 0.10 | K | NIST |
| Ttriple | [156.10; 156.11] | K |
|
| Ttriple | 156.11 | K | Staveley, Lobo and Calado (1981), triple points Compiled value |
| Ttriple | 156.10 ± 0.04 | K | NIST |
| Ttriple | 156.10 ± 0.03 | K | NIST |
| Ttriple | 156.10 ± 0.04 | K | NIST |
| Ttriple | 156.10 ± 0.03 | K | NIST |
| VCOSTALD | 0.37 | m3/kmol | Hankinson and Thomson (1979), COSTALD parameters Compiled value |
| ωSRK | 0.33 | Hankinson and Thomson (1979), COSTALD parameters Compiled value | |
| Zra | 0.26 | Hankinson and Thomson (1979), COSTALD parameters Compiled value |
Cheméo can also estimate Critical Volume, Standard Gibbs free energy of formation, Acentric Factor for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | 198.41 | J/mol×K | 298.15 | NIST |
| ΔfusH | [10.58; 10.58] | kJ/mol | [156.10; 156.10] |
|
| ΔfusH | 10.58 | kJ/mol | 156.10 | NIST |
| ΔfusH | 10.58 | kJ/mol | 156.10 | NIST |
| ΔfusH | 10.58 | kJ/mol | 156.10 | NIST |
| ΔfusH | 10.58 | kJ/mol | 156.10 | NIST |
| ΔvapH | [34.24; 39.80] | kJ/mol | [355.50; 391.70] |
|
| ΔvapH | 39.80 | kJ/mol | 355.50 | NIST |
| ΔvapH | 37.80 | kJ/mol | 364.50 | NIST |
| ΔvapH | 34.24 | kJ/mol | 391.70 | NIST |
| ΔfusS | [67.78; 67.78] | J/mol×K | [156.10; 156.10] |
|
| ΔfusS | 67.78 | J/mol×K | 156.10 | NIST |
| ΔfusS | 67.78 | J/mol×K | 156.10 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [132.05; 303.87] | 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 | 1.79430e+01 | |||
| Coefficient B | 4.73230e-01 | |||
| Coefficient C | -2.08000e-04 | |||
| Coefficient D | 2.07000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 132.05 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 160.24 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 186.01 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 209.41 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 230.51 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 249.39 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 266.09 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 280.70 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 293.27 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 303.87 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [287.68; 417.73] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.42227e+01 | |||
| Coefficient B | -3.21450e+03 | |||
| Coefficient C | -5.70070e+01 | |||
| Temperature range, min. | 287.68 | |||
| Temperature range, max. | 417.73 | |||
| Pvap | 1.33 | kPa | 287.68 | Calculated Property |
| Pvap | 3.03 | kPa | 302.13 | Calculated Property |
| Pvap | 6.29 | kPa | 316.58 | Calculated Property |
| Pvap | 12.08 | kPa | 331.03 | Calculated Property |
| Pvap | 21.75 | kPa | 345.48 | Calculated Property |
| Pvap | 37.00 | kPa | 359.93 | Calculated Property |
| Pvap | 59.99 | kPa | 374.38 | Calculated Property |
| Pvap | 93.25 | kPa | 388.83 | Calculated Property |
| Pvap | 139.70 | kPa | 403.28 | Calculated Property |
| Pvap | 202.63 | kPa | 417.73 | Calculated Property |
| Pvap | [1.37; 3391.50] | kPa | [287.15; 584.00] |
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 | 9.12345e+01 | |||
| Coefficient B | -7.82974e+03 | |||
| Coefficient C | -1.13601e+01 | |||
| Coefficient D | 7.81191e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 287.15 | |||
| Temperature range, max. | 584.00 | |||
| Pvap | 1.37 | kPa | 287.15 | Calculated Property |
| Pvap | 7.72 | kPa | 320.13 | Calculated Property |
| Pvap | 29.60 | kPa | 353.12 | Calculated Property |
| Pvap | 86.33 | kPa | 386.10 | Calculated Property |
| Pvap | 206.53 | kPa | 419.08 | Calculated Property |
| Pvap | 427.27 | kPa | 452.07 | Calculated Property |
| Pvap | 793.63 | kPa | 485.05 | Calculated Property |
| Pvap | 1360.34 | kPa | 518.03 | Calculated Property |
| Pvap | 2196.17 | kPa | 551.02 | Calculated Property |
| Pvap | 3391.50 | kPa | 584.00 | Calculated Property |
Similar Compounds
![Propane, 1-[(1-methylethyl)thio]-.](data:image/png;base64,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)
![2-[Propylthio]ethanal.](data:image/png;base64,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)
Find more compounds similar to Propane, 1-(ethylthio)-.
Sources
- KDB Vapor Pressure Data
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- Hankinson and Thomson (1979), COSTALD parameters ChEDL chemicals 1.5.2, from Hankinson, R. W.; Thomson, G. H. A New Correlation for Saturated Densities of Liquids and Their Mixtures. AIChE J. 1979, 25, 653-663.
- Staveley, Lobo and Calado (1981), triple points ChEDL chemicals 1.5.2, from Staveley, L. A. K.; Lobo, L. Q.; Calado, J. C. G. Triple-Points of Low Melting Substances and Their Use in Cryogenic Work. Cryogenics 1981, 21, 131-144.
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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