- InChI
- InChI=1S/C6H14O2S/c1-3-5-9(7,8)6-4-2/h3-6H2,1-2H3
- InChI Key
- JEXYCADTAFPULN-UHFFFAOYSA-N
- Formula
- C6H14O2S
- SMILES
- CCCS(=O)(=O)CCC
- Molecular Weight1
- 150.24
- CAS
- 598-03-8
- Other Names
-
- 1,1'-Sulphonylbispropane
- Di-n-propyl sulfone
- Dipropyl sulfone
- Dipropyl sulphone
- Propyl sulfone
- n-Propyl sulfone
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas 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).
- ΔvapH° : Enthalpy of vaporization at standard conditions (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).
- Pvap : Vapor pressure (kPa).
- Tboil : Normal Boiling Point Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | -4416.00 ± 0.63 | kJ/mol | NIST |
| ΔfH°gas | -468.30 ± 2.60 | kJ/mol | NIST |
| ΔfH°liquid | -548.19 ± 0.84 | kJ/mol | NIST |
| ΔfusH° | 22.67 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 80.00 ± 2.00 | kJ/mol | NIST |
| IE | 9.59 | eV | Relay (1.0) Calculated Property |
| log10WS | -1.70 | Relay (1.0) Calculated Property | |
| logPoct/wat | 1.221 | Crippen Calculated Property | |
| McVol | 123.490 | ml/mol | McGowan Calculated Property |
| Tboil | 542.00 ± 3.00 | K | NIST |
| Tfus | [299.60; 303.20] | K |
|
| Tfus | 299.60 ± 0.80 | K | NIST |
| Tfus | 302.70 ± 1.50 | K | NIST |
| Tfus | 301.90 ± 0.80 | K | NIST |
| Tfus | 301.20 ± 0.50 | K | NIST |
| Tfus | 303.20 ± 2.00 | K | NIST |
| Tfus | 302.20 ± 5.00 | K | NIST |
Cheméo can also estimate Critical Temperature, Critical Pressure, 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,gas | [229.09; 291.75] | J/mol×K | [384.66; 547.62] |
|
| Cp,gas | 229.09 | J/mol×K | 384.66 | Joback Calculated Property |
| Cp,gas | 240.42 | J/mol×K | 411.82 | Joback Calculated Property |
| Cp,gas | 251.40 | J/mol×K | 438.98 | Joback Calculated Property |
| Cp,gas | 262.02 | J/mol×K | 466.14 | Joback Calculated Property |
| Cp,gas | 272.29 | J/mol×K | 493.30 | Joback Calculated Property |
| Cp,gas | 282.19 | J/mol×K | 520.46 | Joback Calculated Property |
| Cp,gas | 291.75 | J/mol×K | 547.62 | Joback Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [409.40; 574.25] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.49813e+01 | |||
| Coefficient B | -4.66224e+03 | |||
| Coefficient C | -9.21040e+01 | |||
| Temperature range, min. | 409.40 | |||
| Temperature range, max. | 574.25 | |||
| Pvap | 1.33 | kPa | 409.40 | Calculated Property |
| Pvap | 2.97 | kPa | 427.72 | Calculated Property |
| Pvap | 6.10 | kPa | 446.03 | Calculated Property |
| Pvap | 11.67 | kPa | 464.35 | Calculated Property |
| Pvap | 20.99 | kPa | 482.67 | Calculated Property |
| Pvap | 35.83 | kPa | 500.98 | Calculated Property |
| Pvap | 58.42 | kPa | 519.30 | Calculated Property |
| Pvap | 91.50 | kPa | 537.62 | Calculated Property |
| Pvap | 138.33 | kPa | 555.93 | Calculated Property |
| Pvap | 202.65 | kPa | 574.25 | Calculated Property |
| Pvap | [9.76e-04; 3095.64] | kPa | [303.00; 763.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.02832e+02 | |||
| Coefficient B | -1.22739e+04 | |||
| Coefficient C | -1.21800e+01 | |||
| Coefficient D | 3.66502e-06 | |||
| Temperature range, min. | 303.00 | |||
| Temperature range, max. | 763.00 | |||
| Pvap | 9.76e-04 | kPa | 303.00 | Calculated Property |
| Pvap | 0.06 | kPa | 354.11 | Calculated Property |
| Pvap | 1.01 | kPa | 405.22 | Calculated Property |
| Pvap | 8.31 | kPa | 456.33 | Calculated Property |
| Pvap | 41.03 | kPa | 507.44 | Calculated Property |
| Pvap | 142.38 | kPa | 558.56 | Calculated Property |
| Pvap | 384.94 | kPa | 609.67 | Calculated Property |
| Pvap | 869.35 | kPa | 660.78 | Calculated Property |
| Pvap | 1721.65 | kPa | 711.89 | Calculated Property |
| Pvap | 3095.64 | kPa | 763.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Propane, 1,1'-sulfonylbis-.
Sources
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- Cheméo Relay (1.0, beta) Beta: served but experimental, data-limited and below our cross-validation release bar; the Joback value is recommended where available.
- Crippen Method
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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