- InChI
- InChI=1S/C6H14S/c1-3-5-7-6-4-2/h3-6H2,1-2H3
- InChI Key
- ZERULLAPCVRMCO-UHFFFAOYSA-N
- Formula
- C6H14S
- SMILES
- CCCSCCC
- Molecular Weight1
- 118.24
- CAS
- 111-47-7
- Other Names
-
- (n-C3H7)2S
- 1,1'-Thiobispropane
- 4-THIAHEPTANE
- DIPROPYL THIOETHER
- Di-n-propyl thioether
- Dipropyl sulfide
- Dipropyl sulphide
- NSC 78429
- Propane, 1,1'-thiobis-
- Propyl monosulfide
- Sulfide, n-propyl-
- di-n-Propyl sulfide
- di-n-propylsulfide
- n-Propyl sulfide
- 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).
- Cp,liquid : Liquid phase 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).
- 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.
- I : 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).
- 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 | 864.70 | kJ/mol | NIST |
| BasG | 834.90 | kJ/mol | NIST |
| ΔcH°liquid | -4794.28 ± 0.75 | kJ/mol | NIST |
| ΔfG° | 32.76 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -125.20 | kJ/mol | NIST |
| ΔfH°liquid | -169.80 ± 0.88 | kJ/mol | NIST |
| ΔfusH° | 15.43 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [39.50; 44.70] | kJ/mol |
|
| ΔvapH° | 44.23 | kJ/mol | NIST |
| ΔvapH° | 44.20 | kJ/mol | NIST |
| ΔvapH° | 44.50 | kJ/mol | NIST |
| ΔvapH° | Outlier 39.50 | kJ/mol | NIST |
| ΔvapH° | 44.70 ± 0.80 | kJ/mol | NIST |
| ΔvapH° | 44.60 | kJ/mol | NIST |
| IE | [8.30; 10.90] | eV |
|
| IE | 8.45 ± 0.05 | eV | NIST |
| IE | 10.90 | eV | NIST |
| IE | 8.30 ± 0.02 | eV | NIST |
| IE | 8.34 | eV | NIST |
| IE | 8.34 | eV | NIST |
| log10WS | [-2.58; -2.58] |
|
|
| log10WS | -2.58 | Aq. Sol... | |
| log10WS | -2.58 | Estimat... | |
| logPoct/wat | 2.540 | Crippen Calculated Property | |
| McVol | 111.750 | ml/mol | McGowan Calculated Property |
| Pc | 3166.83 | kPa | Joback Calculated Property |
| Inp | [872.00; 897.00] |
|
|
| Inp | 891.20 | NIST | |
| Inp | 896.70 | NIST | |
| Inp | 884.80 | NIST | |
| Inp | 887.40 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 894.00 | NIST | |
| Inp | 891.00 | NIST | |
| Inp | 897.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 894.00 | NIST | |
| Inp | Outlier 872.00 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | 891.20 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 888.00 | NIST | |
| I | [1069.00; 1101.00] |
|
|
| I | 1080.50 | NIST | |
| I | 1091.00 | NIST | |
| I | 1101.00 | NIST | |
| I | 1093.00 | NIST | |
| I | 1069.00 | NIST | |
| I | 1069.00 | NIST | |
| S°liquid | 338.28 | J/mol×K | NIST |
| Tboil | [412.00; 416.00] | K |
|
| Tboil | 415.60 | K | NIST |
| Tboil | 416.00 | K | NIST |
| Tboil | 415.85 ± 0.20 | K | NIST |
| Tboil | 416.00 ± 0.40 | K | NIST |
| Tboil | 414.70 ± 0.50 | K | NIST |
| Tboil | 414.65 ± 0.50 | K | NIST |
| Tboil | 415.60 ± 0.50 | K | NIST |
| Tboil | 415.00 ± 2.00 | K | NIST |
| Tboil | Outlier 412.00 ± 2.00 | K | NIST |
| Tboil | 414.00 ± 0.50 | K | NIST |
| Tboil | 414.00 ± 0.50 | K | NIST |
| Tc | 594.29 | K | Joback Calculated Property |
| Tfus | 170.65 | K | Aq. Sol... |
| Ttriple | [170.43; 170.44] | K |
|
| Ttriple | 170.43 ± 0.05 | K | NIST |
| Ttriple | 170.44 ± 0.03 | K | NIST |
| Vc | 0.425 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [206.46; 268.89] | J/mol×K | [405.46; 594.29] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 210 220 230 240 250 260 270 450 500 550 | ||||
| Cp,gas | 206.46 | J/mol×K | 405.46 | Joback Calculated Property |
| Cp,gas | 217.94 | J/mol×K | 436.93 | Joback Calculated Property |
| Cp,gas | 228.97 | J/mol×K | 468.40 | Joback Calculated Property |
| Cp,gas | 239.58 | J/mol×K | 499.87 | Joback Calculated Property |
| Cp,gas | 249.77 | J/mol×K | 531.34 | Joback Calculated Property |
| Cp,gas | 259.54 | J/mol×K | 562.82 | Joback Calculated Property |
| Cp,gas | 268.89 | J/mol×K | 594.29 | Joback Calculated Property |
| Cp,liquid | [225.48; 237.90] | J/mol×K | [298.15; 300.00] |
|
| Cp,liquid | 225.48 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 237.90 | J/mol×K | 300.00 | NIST |
| ΔfusH | [12.13; 12.14] | kJ/mol | [170.40; 170.44] |
|
| ΔfusH | 12.13 | kJ/mol | 170.40 | NIST |
| ΔfusH | 12.14 | kJ/mol | 170.40 | NIST |
| ΔfusH | 12.14 | kJ/mol | 170.44 | NIST |
| ΔvapH | [36.60; 42.90] | kJ/mol | [362.00; 416.00] |
|
| ΔvapH | 42.90 | kJ/mol | 362.00 | NIST |
| ΔvapH | 40.60 | kJ/mol | 390.00 | NIST |
| ΔvapH | 36.60 | kJ/mol | 416.00 | NIST |
| ΔfusS | 71.24 | J/mol×K | 170.44 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [308.78; 440.91] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.48928e+01 | |||
| Coefficient B | -3.68038e+03 | |||
| Coefficient C | -5.67920e+01 | |||
| Temperature range, min. | 308.78 | |||
| Temperature range, max. | 440.91 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 | ||||
| Pvap | 1.33 | kPa | 308.78 | Calculated Property |
| Pvap | 2.98 | kPa | 323.46 | Calculated Property |
| Pvap | 6.12 | kPa | 338.14 | Calculated Property |
| Pvap | 11.71 | kPa | 352.82 | Calculated Property |
| Pvap | 21.07 | kPa | 367.50 | Calculated Property |
| Pvap | 35.95 | kPa | 382.19 | Calculated Property |
| Pvap | 58.59 | kPa | 396.87 | Calculated Property |
| Pvap | 91.69 | kPa | 411.55 | Calculated Property |
| Pvap | 138.47 | kPa | 426.23 | Calculated Property |
| Pvap | 202.63 | kPa | 440.91 | Calculated Property |
| Pvap | [0.13; 3207.58] | kPa | [270.15; 609.73] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.02676e+02 | |||
| Coefficient B | -8.82408e+03 | |||
| Coefficient C | -1.29840e+01 | |||
| Coefficient D | 8.43544e-06 | |||
| Temperature range, min. | 270.15 | |||
| Temperature range, max. | 609.73 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 300 400 500 600 | ||||
| Pvap | 0.13 | kPa | 270.15 | Calculated Property |
| Pvap | 1.52 | kPa | 307.88 | Calculated Property |
| Pvap | 9.55 | kPa | 345.61 | Calculated Property |
| Pvap | 38.70 | kPa | 383.34 | Calculated Property |
| Pvap | 116.24 | kPa | 421.07 | Calculated Property |
| Pvap | 282.82 | kPa | 458.81 | Calculated Property |
| Pvap | 592.42 | kPa | 496.54 | Calculated Property |
| Pvap | 1114.75 | kPa | 534.27 | Calculated Property |
| Pvap | 1942.89 | kPa | 572.00 | Calculated Property |
| Pvap | 3207.58 | kPa | 609.73 | Calculated Property |
Similar Compounds
![2-[Propylthio]ethanal.](data:image/png;base64,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)
![Propane, 1-[(1-methylethyl)thio]-.](data:image/png;base64,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)
Find more compounds similar to Propyl sulfide.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.