- InChI
- InChI=1S/C4H8S/c1-2-4-5-3-1/h1-4H2
- InChI Key
- RAOIDOHSFRTOEL-UHFFFAOYSA-N
- Formula
- C4H8S
- SMILES
- C1CCSC1
- Molecular Weight1
- 88.17
- CAS
- 110-01-0
- Other Names
-
- NSC 5272
- Pennodorant 1013
- TETRAHYDROTHIOPHENE
- TETRAMETHYLENE SULFIDE
- THIOLANE
- THT
- Tetrahydrothiofen
- Tetrahydrothiophen
- Tetramethylene sulphide
- Thiacyclopentane
- Thilane
- Thiofan
- Thiolan
- Thiophane
- UN 2412
- 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).
- 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 | 849.10 | kJ/mol | NIST |
| BasG | 819.30 | kJ/mol | NIST |
| ΔcH°liquid | [-3246.80; -3246.20] | kJ/mol |
|
| ΔcH°liquid | -3246.80 ± 1.00 | kJ/mol | NIST |
| ΔcH°liquid | -3246.20 ± 1.30 | kJ/mol | NIST |
| ΔfG° | 66.92 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-34.50; -33.60] | kJ/mol |
|
| ΔfH°gas | -33.60 ± 1.20 | kJ/mol | NIST |
| ΔfH°gas | -34.50 ± 1.50 | kJ/mol | NIST |
| ΔfH°liquid | [-73.10; -72.80] | kJ/mol |
|
| ΔfH°liquid | -72.80 ± 1.20 | kJ/mol | NIST |
| ΔfH°liquid | -73.10 ± 1.50 | kJ/mol | NIST |
| ΔfusH° | 2.64 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [38.60; 39.46] | kJ/mol |
|
| ΔvapH° | 39.46 | kJ/mol | NIST |
| ΔvapH° | 38.80 | kJ/mol | NIST |
| ΔvapH° | 39.20 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 39.20 | kJ/mol | NIST |
| ΔvapH° | 38.60 | kJ/mol | NIST |
| ΔvapH° | 38.80 | kJ/mol | NIST |
| IE | [8.38; 8.62] | eV |
|
| IE | 8.38 | eV | NIST |
| IE | 8.38 | eV | NIST |
| IE | 8.62 ± 0.05 | eV | NIST |
| IE | 8.62 | eV | NIST |
| IE | 8.57 ± 0.15 | eV | NIST |
| IE | 8.40 | eV | NIST |
| log10WS | -1.28 | Crippen Calculated Property | |
| logPoct/wat | 1.513 | Crippen Calculated Property | |
| McVol | 72.710 | ml/mol | McGowan Calculated Property |
| Pc | 5138.68 | kPa | Joback Calculated Property |
| Inp | [772.00; 839.00] |
|
|
| Inp | 821.00 | NIST | |
| Inp | 832.50 | NIST | |
| Inp | 806.30 | NIST | |
| Inp | 812.60 | NIST | |
| Inp | 834.00 | NIST | |
| Inp | 805.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 775.00 | NIST | |
| Inp | 772.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 775.00 | NIST | |
| Inp | 772.00 | NIST | |
| Inp | 821.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 813.00 | NIST | |
| Inp | 838.00 | NIST | |
| Inp | 779.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 801.00 | NIST | |
| Inp | 775.00 | NIST | |
| Inp | 775.00 | NIST | |
| Inp | 778.00 | NIST | |
| Inp | 775.00 | NIST | |
| Inp | 775.00 | NIST | |
| Inp | 778.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 801.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 821.00 | NIST | |
| Inp | 805.00 | NIST | |
| Inp | 775.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 838.00 | NIST | |
| Inp | 778.00 | NIST | |
| I | [1107.00; 1130.00] |
|
|
| I | 1107.00 | NIST | |
| I | 1109.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1107.00 | NIST | |
| S°liquid | 207.82 | J/mol×K | NIST |
| Tboil | 394.05 | K | KDB |
| Tc | [632.00; 632.00] | K |
|
| Tc | 632.00 | K | NIST |
| Tc | 632.00 ± 1.00 | K | NIST |
| Tfus | 174.35 ± 1.00 | K | NIST |
| Ttriple | 176.98 ± 0.06 | K | NIST |
| Vc | 0.247 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [108.58; 165.58] | J/mol×K | [358.70; 576.06] |
|
| Cp,gas | 108.58 | J/mol×K | 358.70 | Joback Calculated Property |
| Cp,gas | 119.69 | J/mol×K | 394.93 | Joback Calculated Property |
| Cp,gas | 130.11 | J/mol×K | 431.15 | Joback Calculated Property |
| Cp,gas | 139.88 | J/mol×K | 467.38 | Joback Calculated Property |
| Cp,gas | 149.03 | J/mol×K | 503.61 | Joback Calculated Property |
| Cp,gas | 157.58 | J/mol×K | 539.83 | Joback Calculated Property |
| Cp,gas | 165.58 | J/mol×K | 576.06 | Joback Calculated Property |
| Cp,liquid | 140.16 | J/mol×K | 298.15 | NIST |
| ΔfusH | [7.35; 7.35] | kJ/mol | [176.98; 177.00] |
|
| ΔfusH | 7.35 | kJ/mol | 176.98 | NIST |
| ΔfusH | 7.35 | kJ/mol | 177.00 | NIST |
| ΔfusH | 7.35 | kJ/mol | 177.00 | NIST |
| ΔvapH | [34.66; 37.70] | kJ/mol | [366.00; 394.30] |
|
| ΔvapH | 37.70 | kJ/mol | 366.00 | NIST |
| ΔvapH | 37.10 | kJ/mol | 388.50 | NIST |
| ΔvapH | 34.66 | kJ/mol | 394.30 | NIST |
| Pvap | [2.10; 102.02] | kPa | [293.97; 394.05] |
|
| Pvap | 2.10 | kPa | 293.97 | Infinit... |
| Pvap | 5.90 | kPa | 312.87 | Infinit... |
| Pvap | 7.30 | kPa | 318.34 | Vapor-L... |
| Pvap | 6.70 | kPa | 318.35 | Vapor-L... |
| Pvap | 6.90 | kPa | 318.35 | Vapor-L... |
| Pvap | 20.39 | kPa | 344.79 | Vapor l... |
| Pvap | 21.40 | kPa | 346.14 | Vapor-L... |
| Pvap | 22.20 | kPa | 346.97 | Vapor-L... |
| Pvap | 22.50 | kPa | 346.97 | Vapor-L... |
| Pvap | 22.20 | kPa | 347.07 | Vapor-L... |
| Pvap | 32.09 | kPa | 357.27 | Vapor l... |
| Pvap | 42.29 | kPa | 365.30 | Vapor l... |
| Pvap | 52.61 | kPa | 372.09 | Vapor l... |
| Pvap | 63.09 | kPa | 377.89 | Vapor l... |
| Pvap | 71.89 | kPa | 382.18 | Vapor l... |
| Pvap | 81.18 | kPa | 386.25 | Vapor l... |
| Pvap | 91.67 | kPa | 390.38 | Vapor l... |
| Pvap | 102.02 | kPa | 394.05 | Vapor l... |
| ΔfusS | 41.54 | J/mol×K | 176.98 | NIST |
| λ | [0.11; 0.12] | W/m×K | [273.15; 333.15] |
|
| λ | 0.12 | W/m×K | 273.15 | Liquid ... |
| λ | 0.12 | W/m×K | 288.15 | Liquid ... |
| λ | 0.12 | W/m×K | 303.15 | Liquid ... |
| λ | 0.11 | W/m×K | 318.15 | Liquid ... |
| λ | 0.11 | W/m×K | 333.15 | Liquid ... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [286.00; 419.50] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.44868e+01 | |||
| Coefficient B | -3.46209e+03 | |||
| Coefficient C | -4.21760e+01 | |||
| Temperature range, min. | 286.00 | |||
| Temperature range, max. | 419.50 | |||
| Pvap | 1.33 | kPa | 286.00 | Calculated Property |
| Pvap | 3.01 | kPa | 300.83 | Calculated Property |
| Pvap | 6.22 | kPa | 315.67 | Calculated Property |
| Pvap | 11.93 | kPa | 330.50 | Calculated Property |
| Pvap | 21.47 | kPa | 345.33 | Calculated Property |
| Pvap | 36.58 | kPa | 360.17 | Calculated Property |
| Pvap | 59.42 | kPa | 375.00 | Calculated Property |
| Pvap | 92.61 | kPa | 389.83 | Calculated Property |
| Pvap | 139.20 | kPa | 404.67 | Calculated Property |
| Pvap | 202.64 | kPa | 419.50 | Calculated Property |
| Pvap | [19.22; 5184.65] | kPa | [343.15; 631.95] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.59655e+01 | |||
| Coefficient B | -6.72563e+03 | |||
| Coefficient C | -7.52404e+00 | |||
| Coefficient D | 4.38631e-06 | |||
| Temperature range, min. | 343.15 | |||
| Temperature range, max. | 631.95 | |||
| Pvap | 19.22 | kPa | 343.15 | Calculated Property |
| Pvap | 57.99 | kPa | 375.24 | Calculated Property |
| Pvap | 143.32 | kPa | 407.33 | Calculated Property |
| Pvap | 304.75 | kPa | 439.42 | Calculated Property |
| Pvap | 577.69 | kPa | 471.51 | Calculated Property |
| Pvap | 1002.05 | kPa | 503.59 | Calculated Property |
| Pvap | 1621.85 | kPa | 535.68 | Calculated Property |
| Pvap | 2486.16 | kPa | 567.77 | Calculated Property |
| Pvap | 3651.36 | kPa | 599.86 | Calculated Property |
| Pvap | 5184.65 | kPa | 631.95 | Calculated Property |
Similar Compounds
![2-[Butylthio]ethanal.](data:image/png;base64,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)
Find more compounds similar to Thiophene, tetrahydro-.
Mixtures
- Thiophene, tetrahydro- + o-Xylene
- Toluene + Thiophene, tetrahydro-
- Propane + Thiophene, tetrahydro-
- Butane + Thiophene, tetrahydro-
- Thiophene, tetrahydro- + Isobutane
- 1-Propene, 2-methyl- + Thiophene, tetrahydro-
- Thiophene, tetrahydro- + 2-Butene, (E)-
- Thiophene, tetrahydro- + Pentane, 2,2,4-trimethyl-
- 1-Pentene, 2,4,4-trimethyl- + Thiophene, tetrahydro-
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Vapor liquid equilibrium for the binary systems tetrahydrothiophene + toluene and tetrahydrothiophene + o-xylene at 368.15 K and 383.15 K
- Vapor liquid equilibrium for binary system of tetrahydrothiophene + 2,2,4-trimethylpentane and tetrahydrothiophene + 2,4,4-trimethyl-1-pentene at 358.15 and 368.15 K
- Infinite dilution activity coefficient and vapour liquid equilibrium measurements for dimethylsulphide and tetrahydrothiophene with hydrocarbons
- Liquid Thermal Conductivities of Acetonitrile, Diethyl Sulfide, Hexamethyleneimine, Tetrahydrothiophene, and Tetramethylethylenediamine
- Vapor-Liquid Equilibrium for Tetrahydrothiophene + n-Butane, + trans-2-Butene, + 2-Methylpropane, and + 2-Methylpropene
- Joback Method
- KDB
- 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.