- 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
- Di-n-propyl thioether
- Dipropyl sulfide
- Dipropyl sulphide
- Dipropyl thioether
- NSC 78429
- Propane, 1,1'-thiobis-
- Propyl monosulfide
- Sulfide, n-propyl-
- di-n-Propyl sulfide
- di-n-propylsulfide
- n-Propyl sulfide
- ω : Acentric Factor.
- 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).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- 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).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid 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).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λ : Gas thermal conductivity (W/m×K).
- λ : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3740 | ChemSep v8.3 pure component data | |
| PAff | 864.70 | kJ/mol | NIST |
| BasG | 834.90 | kJ/mol | NIST |
| ΔcH°liquid | -4794.28 ± 0.75 | kJ/mol | NIST |
| μ | 1.65 | debye | ChemSep v8.3 pure component data |
| ΔfG° | 21.50 | kJ/mol | ChemSep v8.3 pure component data |
| ΔfH°gas | [-125.40; -125.20] | kJ/mol |
|
| ΔfH°gas | -125.40 | kJ/mol | ChemSep v8.3 pure component data |
| 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. Solubility Prediction | |
| log10WS | -2.58 | Estimated Solubility | |
| logPoct/wat | 2.540 | Crippen Calculated Property | |
| McVol | 111.750 | ml/mol | McGowan Calculated Property |
| Pc | 3080.00 | kPa | ChemSep v8.3 pure component data |
| Ptriple | 4.40e-07 | kPa | ChemSep v8.3 pure component data |
| 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 | 415.98 | K | ChemSep v8.3 pure component data |
| 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 | 608.00 | K | ChemSep v8.3 pure component data |
| Tfus | [170.55; 170.65] | K |
|
| Tfus | 170.55 | K | ChemSep v8.3 pure component data |
| Tfus | 170.65 | K | Aq. Solubility Prediction |
| Ttriple | [170.43; 170.44] | K |
|
| Ttriple | 170.44 | K | ChemSep v8.3 pure component data |
| Ttriple | 170.43 ± 0.05 | K | NIST |
| Ttriple | 170.44 ± 0.03 | K | NIST |
| Ttriple | 170.43 ± 0.05 | K | NIST |
| Ttriple | 170.44 ± 0.03 | K | NIST |
| UQi | 4.38 | ChemSep v8.3 pure component data | |
| URi | 5.21 | ChemSep v8.3 pure component data | |
| Vc | 0.412 | m3/kmol | ChemSep v8.3 pure component data |
| Zc | 0.2510000 | ChemSep v8.3 pure component data | |
| Zra | 0.25 | ChemSep v8.3 pure component data |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| 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 |
| 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; 71.24] | J/mol×K | [170.44; 170.44] |
|
| ΔfusS | 71.24 | J/mol×K | 170.44 | NIST |
| ΔfusS | 71.24 | J/mol×K | 170.44 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [151.81; 397.87] | J/mol×K | [273.15; 1500.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 1.05470e+02 | |||
| Coefficient B | -6.59930e+02 | |||
| Coefficient C | 6.29124e+00 | |||
| Coefficient D | -1.50000e-04 | |||
| Coefficient E | 2.30410e-08 | |||
| Comment | ChemSep eq 16, IdealGasHeatCapacityCp | |||
| Temperature range, min. | 273.15 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 151.81 | J/mol×K | 273.15 | Calculated Property |
| Cp,gas | 207.17 | J/mol×K | 409.47 | Calculated Property |
| Cp,gas | 254.94 | J/mol×K | 545.78 | Calculated Property |
| Cp,gas | 292.67 | J/mol×K | 682.10 | Calculated Property |
| Cp,gas | 321.96 | J/mol×K | 818.42 | Calculated Property |
| Cp,gas | 344.79 | J/mol×K | 954.73 | Calculated Property |
| Cp,gas | 362.75 | J/mol×K | 1091.05 | Calculated Property |
| Cp,gas | 377.03 | J/mol×K | 1227.37 | Calculated Property |
| Cp,gas | 388.52 | J/mol×K | 1363.68 | Calculated Property |
| Cp,gas | 397.87 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [203.79; 255.42] | J/mol×K | [170.44; 375.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 1.65300e+02 | |||
| Coefficient B | 3.30450e+02 | |||
| Coefficient C | -4.56155e-01 | |||
| Coefficient D | 1.42600e-02 | |||
| Coefficient E | -9.04100e-06 | |||
| Comment | ChemSep eq 16, LiquidHeatCapacityCp | |||
| Temperature range, min. | 170.44 | |||
| Temperature range, max. | 375.00 | |||
| Cp,liquid | 203.79 | J/mol×K | 170.44 | Calculated Property |
| Cp,liquid | 204.62 | J/mol×K | 193.17 | Calculated Property |
| Cp,liquid | 207.05 | J/mol×K | 215.90 | Calculated Property |
| Cp,liquid | 210.75 | J/mol×K | 238.63 | Calculated Property |
| Cp,liquid | 215.58 | J/mol×K | 261.36 | Calculated Property |
| Cp,liquid | 221.47 | J/mol×K | 284.08 | Calculated Property |
| Cp,liquid | 228.42 | J/mol×K | 306.81 | Calculated Property |
| Cp,liquid | 236.40 | J/mol×K | 329.54 | Calculated Property |
| Cp,liquid | 245.41 | J/mol×K | 352.27 | Calculated Property |
| Cp,liquid | 255.42 | J/mol×K | 375.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0123859; 0.0001334] | Pa×s | [170.44; 508.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.02850e+01 | |||
| Coefficient B | 1.15090e+03 | |||
| Coefficient C | -1.70640e-01 | |||
| Coefficient D | 6.22810e-07 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | ChemSep eq 101, LiquidViscosity | |||
| Temperature range, min. | 170.44 | |||
| Temperature range, max. | 508.00 | |||
| η | 0.0123859 | Pa×s | 170.44 | Calculated Property |
| η | 0.0035734 | Pa×s | 207.95 | Calculated Property |
| η | 0.0015070 | Pa×s | 245.45 | Calculated Property |
| η | 0.0007998 | Pa×s | 282.96 | Calculated Property |
| η | 0.0004934 | Pa×s | 320.47 | Calculated Property |
| η | 0.0003376 | Pa×s | 357.97 | Calculated Property |
| η | 0.0002490 | Pa×s | 395.48 | Calculated Property |
| η | 0.0001943 | Pa×s | 432.99 | Calculated Property |
| η | 0.0001583 | Pa×s | 470.49 | Calculated Property |
| η | 0.0001334 | Pa×s | 508.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [50.50; 16.79] | kJ/mol | [170.44; 584.97] |
ChemSep v8.3 pure component data
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 5.75750e+01 | |||
| Coefficient B | 3.83340e-01 | |||
| Coefficient C | 9.83970e-02 | |||
| Coefficient D | -1.72330e-01 | |||
| Coefficient E | 6.51590e-02 | |||
| Critical temperature, Tc (K) | 6.08000e+02 | |||
| Comment | ChemSep eq 106, HeatOfVaporization | |||
| Temperature range, min. | 170.44 | |||
| Temperature range, max. | 584.97 | |||
| ΔvapH | 50.50 | kJ/mol | 170.44 | Calculated Property |
| ΔvapH | 48.29 | kJ/mol | 216.50 | Calculated Property |
| ΔvapH | 45.95 | kJ/mol | 262.56 | Calculated Property |
| ΔvapH | 43.45 | kJ/mol | 308.62 | Calculated Property |
| ΔvapH | 40.74 | kJ/mol | 354.68 | Calculated Property |
| ΔvapH | 37.76 | kJ/mol | 400.73 | Calculated Property |
| ΔvapH | 34.38 | kJ/mol | 446.79 | Calculated Property |
| ΔvapH | 30.36 | kJ/mol | 492.85 | Calculated Property |
| ΔvapH | 25.17 | kJ/mol | 538.91 | Calculated Property |
| ΔvapH | 16.79 | kJ/mol | 584.97 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [308.78; 440.91] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| 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 | |||
| 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 | [9.93e-08; 4646.41] | kPa | [170.44; 608.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.42730e+02 | |||
| Coefficient B | -1.02516e+04 | |||
| Coefficient C | -1.93067e+01 | |||
| Coefficient D | 1.71365e-05 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | ChemSep eq 101, VaporPressure | |||
| Temperature range, min. | 170.44 | |||
| Temperature range, max. | 608.00 | |||
| Pvap | 9.93e-08 | kPa | 170.44 | Calculated Property |
| Pvap | 6.78e-04 | kPa | 219.06 | Calculated Property |
| Pvap | 0.10 | kPa | 267.68 | Calculated Property |
| Pvap | 2.44 | kPa | 316.29 | Calculated Property |
| Pvap | 20.40 | kPa | 364.91 | Calculated Property |
| Pvap | 94.82 | kPa | 413.53 | Calculated Property |
| Pvap | 312.13 | kPa | 462.15 | Calculated Property |
| Pvap | 840.75 | kPa | 510.76 | Calculated Property |
| Pvap | 2028.11 | kPa | 559.38 | Calculated Property |
| Pvap | 4646.41 | kPa | 608.00 | Calculated Property |
| Pvap | [0.13; 3207.58] | kPa | [270.15; 609.73] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.02676e+02 | |||
| Coefficient B | -8.82408e+03 | |||
| Coefficient C | -1.29840e+01 | |||
| Coefficient D | 8.43544e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 270.15 | |||
| Temperature range, max. | 609.73 | |||
| 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 |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [932.94; 472.53] | kg/m3 | [170.44; 584.97] |
ChemSep v8.3 pure component data
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 7.83887e+01 | |||
| Coefficient B | 2.73130e-01 | |||
| Coefficient C | 6.08000e+02 | |||
| Coefficient D | 2.92240e-01 | |||
| Comment | ChemSep eq 105, LiquidDensity | |||
| Temperature range, min. | 170.44 | |||
| Temperature range, max. | 584.97 | |||
| ρl | 932.94 | kg/m3 | 170.44 | Calculated Property |
| ρl | 898.42 | kg/m3 | 216.50 | Calculated Property |
| ρl | 862.34 | kg/m3 | 262.56 | Calculated Property |
| ρl | 824.35 | kg/m3 | 308.62 | Calculated Property |
| ρl | 783.93 | kg/m3 | 354.68 | Calculated Property |
| ρl | 740.32 | kg/m3 | 400.73 | Calculated Property |
| ρl | 692.28 | kg/m3 | 446.79 | Calculated Property |
| ρl | 637.48 | kg/m3 | 492.85 | Calculated Property |
| ρl | 570.70 | kg/m3 | 538.91 | Calculated Property |
| ρl | 472.53 | kg/m3 | 584.97 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 8.54e-04] | N/m | [170.44; 584.97] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K | |||
| Coefficient A | -1.67470e-02 | |||
| Coefficient B | 1.68810e+01 | |||
| Coefficient C | -2.76670e+00 | |||
| Coefficient D | -7.67370e-04 | |||
| Coefficient E | -2.49300e-06 | |||
| Comment | ChemSep eq 16, SurfaceTension | |||
| Temperature range, min. | 170.44 | |||
| Temperature range, max. | 584.97 | |||
| γ | 0.04 | N/m | 170.44 | Calculated Property |
| γ | 0.03 | N/m | 216.50 | Calculated Property |
| γ | 0.03 | N/m | 262.56 | Calculated Property |
| γ | 0.02 | N/m | 308.62 | Calculated Property |
| γ | 0.02 | N/m | 354.68 | Calculated Property |
| γ | 0.02 | N/m | 400.73 | Calculated Property |
| γ | 0.01 | N/m | 446.79 | Calculated Property |
| γ | 0.01 | N/m | 492.85 | Calculated Property |
| γ | 0.00 | N/m | 538.91 | Calculated Property |
| γ | 8.54e-04 | N/m | 584.97 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.00; 0.08] | W/m×K | [170.44; 1000.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λ in W/m×K, T in K | |||
| Coefficient A | 8.61510e-03 | |||
| Coefficient B | 4.87060e-01 | |||
| Coefficient C | 1.64860e+03 | |||
| Coefficient D | 4.89220e+05 | |||
| Comment | ChemSep eq 102, VaporThermalConductivity | |||
| Temperature range, min. | 170.44 | |||
| Temperature range, max. | 1000.00 | |||
| λ | 0.00 | W/m×K | 170.44 | Calculated Property |
| λ | 0.01 | W/m×K | 262.61 | Calculated Property |
| λ | 0.02 | W/m×K | 354.79 | Calculated Property |
| λ | 0.02 | W/m×K | 446.96 | Calculated Property |
| λ | 0.03 | W/m×K | 539.13 | Calculated Property |
| λ | 0.04 | W/m×K | 631.31 | Calculated Property |
| λ | 0.05 | W/m×K | 723.48 | Calculated Property |
| λ | 0.06 | W/m×K | 815.65 | Calculated Property |
| λ | 0.07 | W/m×K | 907.83 | Calculated Property |
| λ | 0.08 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.16; 0.10] | W/m×K | [170.44; 415.98] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λ in W/m×K, T in K | |||
| Coefficient A | -7.81090e-02 | |||
| Coefficient B | 7.17330e+00 | |||
| Coefficient C | -1.42310e+00 | |||
| Coefficient D | -9.76390e-05 | |||
| Coefficient E | -1.54650e-06 | |||
| Comment | ChemSep eq 16, LiquidThermalConductivity | |||
| Temperature range, min. | 170.44 | |||
| Temperature range, max. | 415.98 | |||
| λ | 0.16 | W/m×K | 170.44 | Calculated Property |
| λ | 0.15 | W/m×K | 197.72 | Calculated Property |
| λ | 0.15 | W/m×K | 225.00 | Calculated Property |
| λ | 0.14 | W/m×K | 252.29 | Calculated Property |
| λ | 0.14 | W/m×K | 279.57 | Calculated Property |
| λ | 0.13 | W/m×K | 306.85 | Calculated Property |
| λ | 0.12 | W/m×K | 334.13 | Calculated Property |
| λ | 0.12 | W/m×K | 361.42 | Calculated Property |
| λ | 0.11 | W/m×K | 388.70 | Calculated Property |
| λ | 0.10 | W/m×K | 415.98 | 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
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- 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.
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