- InChI
- InChI=1S/C4H10OS/c1-3-6(5)4-2/h3-4H2,1-2H3
- InChI Key
- CCAFPWNGIUBUSD-UHFFFAOYSA-N
- Formula
- C4H10OS
- SMILES
- CCS(=O)CC
- Molecular Weight1
- 106.19
- Other Names
-
- 1,1'-sulfinylbis(ethane)
- 1,1'-sulfinylbisethane
- diethyl sulphoxide
- ethyl sulfoxide
- 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).
- ΔvapH° : Enthalpy of vaporization at standard conditions (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).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- γ : Surface Tension (N/m).
- 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.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfG° | -234.91 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -331.63 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 13.87 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 37.22 | kJ/mol | Joback Calculated Property |
| log10WS | -0.13 | Crippen Calculated Property | |
| logPoct/wat | 0.775 | Crippen Calculated Property | |
| McVol | 89.440 | ml/mol | McGowan Calculated Property |
| Pc | 4351.13 | kPa | Joback Calculated Property |
| Tboil | 349.20 | K | Joback Calculated Property |
| Tc | 525.53 | K | Joback Calculated Property |
| Tfus | 171.32 | K | Joback Calculated Property |
| Vc | 0.349 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [147.03; 194.52] | J/mol×K | [349.20; 525.53] | 
|
|
T(K) Ideal gas heat capacity (J/mol×K) 150 160 170 180 190 350 400 450 500 | ||||
| Cp,gas | 147.03 | J/mol×K | 349.20 | Joback Calculated Property |
| Cp,gas | 155.60 | J/mol×K | 378.59 | Joback Calculated Property |
| Cp,gas | 163.91 | J/mol×K | 407.98 | Joback Calculated Property |
| Cp,gas | 171.96 | J/mol×K | 437.36 | Joback Calculated Property |
| Cp,gas | 179.75 | J/mol×K | 466.75 | Joback Calculated Property |
| Cp,gas | 187.27 | J/mol×K | 496.14 | Joback Calculated Property |
| Cp,gas | 194.52 | J/mol×K | 525.53 | Joback Calculated Property |
| Pvap | [0.02; 0.09] | kPa | [298.15; 318.15] |
|
|
T(K) Vapor pressure (kPa) 0.02 0.03 0.04 0.05 0.06 0.07 0.08 0.09 300 305 310 315 | ||||
| Pvap | 0.02 ± 0.00 | kPa | 298.15 | Vapor P... |
| Pvap | 0.03 ± 0.00 | kPa | 303.15 | Vapor P... |
| Pvap | 0.04 ± 0.00 | kPa | 308.15 | Vapor P... |
| Pvap | 0.07 ± 0.00 | kPa | 313.15 | Vapor P... |
| Pvap | 0.09 ± 0.00 | kPa | 318.15 | Vapor P... |
| n0 | [1.46400; 1.46800] | [298.15; 308.15] |
|
|
| n0 | 1.46800 ± 0.00050 | 298.15 | Surface... | |
| n0 | 1.46600 ± 0.00050 | 303.15 | Surface... | |
| n0 | 1.46400 ± 0.00050 | 308.15 | Surface... | |
| ρl | [970.60; 1010.20] | kg/m3 | [298.15; 343.15] |
|
|
T(K) Liquid Density (kg/m3) 970 980 990 1000 1010 300 320 340 | ||||
| ρl | 1010.20 | kg/m3 | 298.15 | Volumet... |
| ρl | 1009.51 | kg/m3 | 298.15 | Surface... |
| ρl | 1005.80 | kg/m3 | 303.15 | Volumet... |
| ρl | 1005.14 | kg/m3 | 303.15 | Surface... |
| ρl | 1001.40 | kg/m3 | 308.15 | Volumet... |
| ρl | 1000.77 | kg/m3 | 308.15 | Surface... |
| ρl | 997.00 | kg/m3 | 313.15 | Volumet... |
| ρl | 996.40 | kg/m3 | 313.15 | Surface... |
| ρl | 992.60 | kg/m3 | 318.15 | Volumet... |
| ρl | 988.20 | kg/m3 | 323.15 | Volumet... |
| ρl | 983.90 | kg/m3 | 328.15 | Volumet... |
| ρl | 979.50 | kg/m3 | 333.15 | Volumet... |
| ρl | 975.10 | kg/m3 | 338.15 | Volumet... |
| ρl | 970.60 | kg/m3 | 343.15 | Volumet... |
| γ | [0.03; 0.03] | N/m | [298.15; 328.15] |
|
|
T(K) Surface Tension (N/m) 0.03 0.03 0.03 0.03 0.03 0.03 300 310 320 | ||||
| γ | 0.03 | N/m | 298.15 | Surface... |
| γ | 0.03 ± 0.00 | N/m | 298.15 | Surface... |
| γ | 0.03 | N/m | 303.15 | Surface... |
| γ | 0.03 ± 0.00 | N/m | 303.15 | Surface... |
| γ | 0.03 | N/m | 308.15 | Surface... |
| γ | 0.03 ± 0.00 | N/m | 308.15 | Surface... |
| γ | 0.03 | N/m | 313.15 | Surface... |
| γ | 0.03 ± 0.00 | N/m | 313.15 | Surface... |
| γ | 0.03 ± 0.00 | N/m | 318.15 | Surface... |
| γ | 0.03 ± 0.00 | N/m | 323.15 | Surface... |
| γ | 0.03 ± 0.00 | N/m | 328.15 | Surface... |
Similar Compounds
![2-[Ethylthio]ethanal.](data:image/png;base64,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)
Find more compounds similar to diethyl sulfoxide.
Sources
- Crippen Method
- Crippen Method
- Volumetric properties of aqueous solutions of diethylsulfoxide at temperatures from 298.15 K to 343.15 K
- Surface and bulk behavior of (dialkylsulfoxides + carbon tetrachloride) mixtures
- Vapor Pressures of Pure Diethyl Sulfoxide from (298.15 to 318.15) K and Vapor-Liquid Equilibria of Binary Mixtures of Diethyl Sulfoxide with Water
- Surface Tension and Refractive Index of Dialkylsulfoxide + Water Mixtures at Several Temperatures
- Joback Method
- McGowan Method
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.