- InChI
- InChI=1S/C4H10S/c1-3-5-4-2/h3-4H2,1-2H3
- InChI Key
- LJSQFQKUNVCTIA-UHFFFAOYSA-N
- Formula
- C4H10S
- SMILES
- CCSCC
- Molecular Weight1
- 90.19
- CAS
- 352-93-2
- Other Names
-
- (C2H5)2S
- 1,1'-Thiobisethane
- 3-Thiapentane
- Diethyl sulphide
- Diethyl thioether
- Diethylsulfid
- Ethane, 1,1'-thiobis-
- Ethyl monosulfide
- Ethyl sulfide
- Ethyl thioether
- Ethylthioethane
- NSC 75157
- Sulfodor
- Thioethyl ether
- UN 2375
- 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).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- 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).
- λ : Liquid thermal conductivity (W/m×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 | 856.70 | kJ/mol | NIST |
| BasG | 827.00 | kJ/mol | NIST |
| ΔcH°liquid | [-3486.10; -3471.00] | kJ/mol |
|
| ΔcH°liquid | -3486.10 ± 0.67 | kJ/mol | NIST |
| ΔcH°liquid | -3471.00 | kJ/mol | NIST |
| ΔfG° | 15.92 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-83.50; -82.72] | kJ/mol |
|
| ΔfH°gas | -83.50 ± 2.30 | kJ/mol | NIST |
| ΔfH°gas | -82.72 ± 0.79 | kJ/mol | NIST |
| ΔfH°liquid | [-119.40; -119.30] | kJ/mol |
|
| ΔfH°liquid | -119.30 ± 2.00 | kJ/mol | NIST |
| ΔfH°liquid | -119.40 ± 0.84 | kJ/mol | NIST |
| ΔfusH° | 10.25 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 31.32 | kJ/mol | Joback Calculated Property |
| IE | [8.40; 8.46] | eV |
|
| IE | 8.42 ± 0.01 | eV | NIST |
| IE | 8.41 | eV | NIST |
| IE | 8.42 ± 0.01 | eV | NIST |
| IE | 8.43 ± 0.01 | eV | NIST |
| IE | 8.40 | eV | NIST |
| IE | 8.46 | eV | NIST |
| IE | 8.44 | eV | NIST |
| IE | 8.44 | eV | NIST |
| log10WS | [-1.34; -1.34] |
|
|
| log10WS | -1.34 | Aq. Sol... | |
| log10WS | -1.34 | Estimat... | |
| logPoct/wat | 1.759 | Crippen Calculated Property | |
| McVol | 83.570 | ml/mol | McGowan Calculated Property |
| Pc | 3960.00 ± 40.53 | kPa | NIST |
| ρc | 284.18 ± 1.80 | kg/m3 | NIST |
| Inp | [683.00; 720.00] |
|
|
| Inp | 708.50 | NIST | |
| Inp | Outlier 717.90 | NIST | |
| Inp | 700.40 | NIST | |
| Inp | 703.70 | NIST | |
| Inp | 698.00 | NIST | |
| Inp | 698.00 | NIST | |
| Inp | 698.00 | NIST | |
| Inp | 699.00 | NIST | |
| Inp | 696.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 696.00 | NIST | |
| Inp | 693.00 | NIST | |
| Inp | 693.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 698.00 | NIST | |
| Inp | 704.00 | NIST | |
| Inp | 708.00 | NIST | |
| Inp | 700.00 | NIST | |
| Inp | 704.00 | NIST | |
| Inp | Outlier 720.00 | NIST | |
| Inp | 704.00 | NIST | |
| Inp | 699.00 | NIST | |
| Inp | 699.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 698.00 | NIST | |
| Inp | 693.00 | NIST | |
| Inp | 704.00 | NIST | |
| Inp | Outlier 683.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 704.00 | NIST | |
| Inp | 708.00 | NIST | |
| I | [895.00; 927.00] |
|
|
| I | 903.00 | NIST | |
| I | Outlier 927.00 | NIST | |
| I | 904.00 | NIST | |
| I | 895.00 | NIST | |
| I | 899.00 | NIST | |
| I | 895.00 | NIST | |
| I | 899.00 | NIST | |
| I | 903.00 | NIST | |
| I | 904.00 | NIST | |
| S°liquid | 269.28 | J/mol×K | NIST |
| Tboil | 359.70 | K | Joback Calculated Property |
| Tc | [557.00; 557.00] | K |
|
| Tc | 557.00 | K | NIST |
| Tc | 557.00 ± 0.50 | K | NIST |
| Tfus | [169.18; 169.85] | K |
|
| Tfus | 169.18 | K | Aq. Sol... |
| Tfus | 169.85 ± 0.60 | K | NIST |
| Tfus | 169.24 ± 0.10 | K | NIST |
| Tfus | 169.85 ± 0.40 | K | NIST |
| Ttriple | 169.21 ± 0.02 | K | NIST |
| Vc | 0.314 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [135.44; 182.04] | J/mol×K | [359.70; 550.75] |
|
| Cp,gas | 135.44 | J/mol×K | 359.70 | Joback Calculated Property |
| Cp,gas | 143.93 | J/mol×K | 391.54 | Joback Calculated Property |
| Cp,gas | 152.12 | J/mol×K | 423.38 | Joback Calculated Property |
| Cp,gas | 160.03 | J/mol×K | 455.23 | Joback Calculated Property |
| Cp,gas | 167.65 | J/mol×K | 487.07 | Joback Calculated Property |
| Cp,gas | 174.99 | J/mol×K | 518.91 | Joback Calculated Property |
| Cp,gas | 182.04 | J/mol×K | 550.75 | Joback Calculated Property |
| Cp,liquid | 171.42 | J/mol×K | 298.15 | NIST |
| ΔfusH | [11.90; 11.92] | kJ/mol | [169.20; 169.21] |
|
| ΔfusH | 11.92 | kJ/mol | 169.20 | NIST |
| ΔfusH | 11.90 | kJ/mol | 169.20 | NIST |
| ΔfusH | 11.90 | kJ/mol | 169.21 | NIST |
| ΔvapH | [31.77; 37.50] | kJ/mol | [297.00; 365.30] |
|
| ΔvapH | 37.50 | kJ/mol | 297.00 | NIST |
| ΔvapH | 34.90 | kJ/mol | 327.00 | NIST |
| ΔvapH | 34.80 | kJ/mol | 340.00 | NIST |
| ΔvapH | 34.40 | kJ/mol | 357.00 | NIST |
| ΔvapH | 33.50 | kJ/mol | 364.00 | NIST |
| ΔvapH | 31.77 | kJ/mol | 365.30 | NIST |
| Pvap | [13.30; 18.80] | kPa | [307.94; 317.62] |
|
| Pvap | 13.30 | kPa | 307.94 | Vapour ... |
| Pvap | 15.00 | kPa | 312.58 | Vapour ... |
| Pvap | 15.20 | kPa | 312.58 | Vapour ... |
| Pvap | 15.10 | kPa | 312.59 | Vapour ... |
| Pvap | 18.50 | kPa | 317.46 | Vapour ... |
| Pvap | 18.80 | kPa | 317.62 | Vapour ... |
| n0 | [1.43998; 1.44000] | [298.15; 298.15] |
|
|
| n0 | 1.44000 | 298.15 | Vapor l... | |
| n0 | 1.44000 | 298.15 | Vapor-L... | |
| n0 | 1.44000 | 298.15 | Vapor-L... | |
| n0 | 1.44000 | 298.15 | Vapor-L... | |
| n0 | 1.43998 | 298.15 | Vapor L... | |
| ΔfusS | 70.35 | J/mol×K | 169.21 | NIST |
| λ | [0.13; 0.14] | W/m×K | [273.15; 333.15] |
|
| λ | 0.14 | W/m×K | 273.15 | Liquid ... |
| λ | 0.14 | W/m×K | 293.15 | Liquid ... |
| λ | 0.14 | W/m×K | 313.15 | Liquid ... |
| λ | 0.13 | W/m×K | 333.15 | Liquid ... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [265.45; 389.55] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.45990e+01 | |||
| Coefficient B | -3.28325e+03 | |||
| Coefficient C | -3.60380e+01 | |||
| Temperature range, min. | 265.45 | |||
| Temperature range, max. | 389.55 | |||
| Pvap | 1.33 | kPa | 265.45 | Calculated Property |
| Pvap | 3.00 | kPa | 279.24 | Calculated Property |
| Pvap | 6.19 | kPa | 293.03 | Calculated Property |
| Pvap | 11.87 | kPa | 306.82 | Calculated Property |
| Pvap | 21.35 | kPa | 320.61 | Calculated Property |
| Pvap | 36.40 | kPa | 334.39 | Calculated Property |
| Pvap | 59.18 | kPa | 348.18 | Calculated Property |
| Pvap | 92.35 | kPa | 361.97 | Calculated Property |
| Pvap | 139.00 | kPa | 375.76 | Calculated Property |
| Pvap | 202.64 | kPa | 389.55 | Calculated Property |
| Pvap | [4.25e-05; 3818.68] | kPa | [169.20; 557.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.58385e+01 | |||
| Coefficient B | -6.29676e+03 | |||
| Coefficient C | -7.56818e+00 | |||
| Coefficient D | 5.03613e-06 | |||
| Temperature range, min. | 169.20 | |||
| Temperature range, max. | 557.15 | |||
| Pvap | 4.25e-05 | kPa | 169.20 | Calculated Property |
| Pvap | 0.02 | kPa | 212.31 | Calculated Property |
| Pvap | 0.65 | kPa | 255.41 | Calculated Property |
| Pvap | 7.88 | kPa | 298.52 | Calculated Property |
| Pvap | 46.70 | kPa | 341.62 | Calculated Property |
| Pvap | 175.43 | kPa | 384.73 | Calculated Property |
| Pvap | 487.31 | kPa | 427.83 | Calculated Property |
| Pvap | 1101.72 | kPa | 470.94 | Calculated Property |
| Pvap | 2157.77 | kPa | 514.04 | Calculated Property |
| Pvap | 3818.68 | kPa | 557.15 | Calculated Property |
Similar Compounds
![2-[Ethylthio]ethanal.](data:image/png;base64,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)
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- Diethyl sulfide + Cyclohexane
- Propane, 2-ethoxy-2-methyl- + Diethyl sulfide
- 1-Butene + Diethyl sulfide
- 2-Butene, (Z)- + Diethyl sulfide
- Diethyl sulfide + Isobutane
- 1-Propene, 2-methyl- + Diethyl sulfide
- Butane + Diethyl sulfide
- 2-Butene, (E)- + Diethyl sulfide
- Ethanol + Diethyl sulfide
- 1-Propanol + Diethyl sulfide
- n-Propyl acetate + Diethyl sulfide
- Toluene + Diethyl sulfide
- Heptane + Diethyl sulfide
- Pentane, 2,2,4-trimethyl- + Diethyl sulfide
- n-Hexane + Diethyl sulfide
- 1-Hexene + Diethyl sulfide
- Dimethyl ether + Diethyl sulfide
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Vapor liquid equilibrium for binary system of diethyl sulfide + cyclohexane at 353.15 and 343.15 K and diethyl sulfide + 2-ethoxy-2-methylpropane at 343.15 and 333.15 K
- Vapour liquid equilibrium for the systems diethyl sulphide + 1-butene, +cis-2-butene, +2-methylpropane, +2-methylpropene, +n-butane, +trans-2-butene
- Phase equilibria on binary systems containing diethyl sulfide
- An improved static-analytic apparatus for vapor-liquid equilibrium (PTxy) measurement using modified in-situ samplers
- Liquid Thermal Conductivities of Acetonitrile, Diethyl Sulfide, Hexamethyleneimine, Tetrahydrothiophene, and Tetramethylethylenediamine
- Vapor-Liquid Equilibrium for Binary System of 1-Propanethiol, Thiophene, and Diethyl Sulfide with Toluene at 90.03 kPa
- Vapor-Liquid Equilibrium for Binary System of Diethyl Sulfide + n-Heptane and Diethyl Sulfide + 2,2,4-Trimethylpentane at (363.15 and 353.15) K
- Vapor-Liquid Equilibrium for Binary System of Diethyl Sulfide + n-Hexane at (338.15 and 323.15) K and Diethyl Sulfide + 1-Hexene at (333.15 and 323.15) K
- Vapor Liquid Equilibrium for Methoxymethane + Thiophene, + Diethylsulfide, + 2-Methyl-2-propanethiol and 1-Hexene, + 1-Propanethiol
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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