- InChI
- InChI=1S/C3H8S/c1-3-4-2/h3H2,1-2H3
- InChI Key
- WXEHBUMAEPOYKP-UHFFFAOYSA-N
- Formula
- C3H8S
- SMILES
- CCSC
- Molecular Weight1
- 76.16
- CAS
- 624-89-5
- Other Names
-
- (methylthio)ethane
- 1-(Methylsulfanyl)ethane
- 1-(methylthio)ethane
- 2-thiabutane
- C2H5SCH3
- Ethyl methyl sulphide
- Methyl ethyl sulphide
- Sulfide, ethyl methyl
- ethyl methyl sulfide
- methyl ethyl 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.
- Ip : Polar retention indices.
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : 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).
- VCOSTALD : COSTALD Characteristic Volume (m3/kmol).
- ωSRK : SRK acentric factor.
- 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 | [0.2080; 0.2160] |
|
|
| ω | 0.2080 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.2080 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.2160 | KDB | |
| PAff | 846.50 | kJ/mol | NIST |
| BasG | 815.30 | kJ/mol | NIST |
| ΔcH°liquid | -2833.60 ± 1.10 | kJ/mol | NIST |
| μ | 1.60 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | [11.40; 11.90] | kJ/mol |
|
| ΔfG° | 11.90 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | 11.40 | kJ/mol | KDB |
| ΔfH°gas | [-60.30; -59.30] | kJ/mol |
|
| ΔfH°gas | -59.30 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -59.66 | kJ/mol | KDB |
| ΔfH°gas | -60.30 ± 1.10 | kJ/mol | NIST |
| ΔfH°liquid | -92.30 ± 1.10 | kJ/mol | NIST |
| ΔfusH° | 7.66 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [31.50; 32.00] | kJ/mol |
|
| ΔvapH° | 31.99 | kJ/mol | NIST |
| ΔvapH° | 31.50 | kJ/mol | NIST |
| ΔvapH° | 31.80 | kJ/mol | NIST |
| ΔvapH° | 32.00 | kJ/mol | NIST |
| IE | [8.46; 10.96] | eV |
|
| IE | 8.55 ± 0.01 | eV | NIST |
| IE | 8.46 | eV | NIST |
| IE | 8.50 ± 0.10 | eV | NIST |
| IE | 8.55 ± 0.01 | eV | NIST |
| IE | Outlier 10.96 | eV | NIST |
| IE | 8.54 | eV | NIST |
| log10WS | -0.95 | Relay (1.0) Calculated Property | |
| logPoct/wat | 1.369 | Crippen Calculated Property | |
| McVol | 69.480 | ml/mol | McGowan Calculated Property |
| Pc | [4250.00; 4260.00] | kPa |
|
| Pc | 4250.00 | kPa | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 8 Compiled value |
| Pc | 4255.65 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 4260.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 4260.00 | kPa | KDB |
| Ptriple | 2.25e-04 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [605.00; 638.20] |
|
|
| Inp | 625.00 | NIST | |
| Inp | Outlier 638.20 | NIST | |
| Inp | 618.80 | NIST | |
| Inp | 621.90 | NIST | |
| Inp | 616.00 | NIST | |
| Inp | 608.00 | NIST | |
| Inp | 616.00 | NIST | |
| Inp | 623.00 | NIST | |
| Inp | 609.00 | NIST | |
| Inp | 609.00 | NIST | |
| Inp | 625.00 | NIST | |
| Inp | 619.00 | NIST | |
| Inp | 622.00 | NIST | |
| Inp | 620.00 | NIST | |
| Inp | 610.00 | NIST | |
| Inp | 614.00 | NIST | |
| Inp | 622.00 | NIST | |
| Inp | 611.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 617.00 | NIST | |
| Inp | 625.00 | NIST | |
| Inp | 608.00 | NIST | |
| Inp | 609.00 | NIST | |
| Inp | 614.00 | NIST | |
| Ip | [829.00; 859.00] |
|
|
| Ip | 859.00 | NIST | |
| Ip | 829.00 | NIST | |
| Ip | 859.00 | NIST | |
| Ip | 859.00 | NIST | |
| Ip | 829.00 | NIST | |
| Tboil | [335.20; 340.00] | K |
|
| Tboil | 339.80 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 339.80 | K | KDB |
| Tboil | 339.80 | K | NIST |
| Tboil | 339.80 | K | NIST |
| Tboil | 340.00 ± 5.00 | K | NIST |
| Tboil | 339.80 ± 0.30 | K | NIST |
| Tboil | Outlier 335.20 ± 1.50 | K | NIST |
| Tc | [533.00; 553.00] | K |
|
| Tc | 533.00 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 8 Compiled value |
| Tc | 533.00 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 533.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 533.00 | K | KDB |
| Tc | 553.00 | K | NIST |
| Tfus | [167.15; 167.24] | K |
|
| Tfus | 167.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 167.24 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 167.20 | K | KDB |
| Tfus | 167.24 ± 0.10 | K | NIST |
| Ttriple | [167.23; 167.23] | K |
|
| Ttriple | 167.23 | K | ChemSep v8.3 pure component data Compiled value |
| Ttriple | 167.23 ± 0.02 | K | NIST |
| UQi | 2.76 | ChemSep v8.3 pure component data Compiled value | |
| URi | 3.19 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.259; 0.260] | m3/kmol |
|
| Vc | 0.259 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.260 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| VCOSTALD | 0.26 | m3/kmol | Hankinson and Thomson (1979), COSTALD parameters Compiled value |
| ωSRK | 0.24 | Hankinson and Thomson (1979), COSTALD parameters Compiled value | |
| Zc | 0.2500000 | ChemSep v8.3 pure component data Compiled value | |
| Zra | [0.25; 0.27] |
|
|
| Zra | 0.27 | Hankinson and Thomson (1979), COSTALD parameters Compiled value | |
| Zra | 0.25 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [89.91; 231.60] | J/mol×K | [273.16; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 6.50180e+01 | |||
| Coefficient B | -6.02450e+02 | |||
| Coefficient C | 5.36124e+00 | |||
| Coefficient D | 2.39380e-04 | |||
| Coefficient E | -9.02990e-08 | |||
| Temperature range, min. | 273.16 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 89.91 | J/mol×K | 273.16 | Calculated Property |
| Cp,gas | 118.15 | J/mol×K | 409.48 | Calculated Property |
| Cp,gas | 143.37 | J/mol×K | 545.79 | Calculated Property |
| Cp,gas | 164.43 | J/mol×K | 682.11 | Calculated Property |
| Cp,gas | 181.83 | J/mol×K | 818.42 | Calculated Property |
| Cp,gas | 196.18 | J/mol×K | 954.74 | Calculated Property |
| Cp,gas | 208.01 | J/mol×K | 1091.05 | Calculated Property |
| Cp,gas | 217.67 | J/mol×K | 1227.37 | Calculated Property |
| Cp,gas | 225.47 | J/mol×K | 1363.68 | Calculated Property |
| Cp,gas | 231.60 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [136.47; 153.43] | J/mol×K | [147.21; 339.80] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 1.28430e+02 | |||
| Coefficient B | 1.34020e+03 | |||
| Coefficient C | -1.48425e+01 | |||
| Coefficient D | 6.20090e-02 | |||
| Coefficient E | -6.02200e-05 | |||
| Temperature range, min. | 147.21 | |||
| Temperature range, max. | 339.80 | |||
| Cp,liquid | 136.47 | J/mol×K | 147.21 | Calculated Property |
| Cp,liquid | 134.79 | J/mol×K | 168.61 | Calculated Property |
| Cp,liquid | 134.60 | J/mol×K | 190.01 | Calculated Property |
| Cp,liquid | 135.21 | J/mol×K | 211.41 | Calculated Property |
| Cp,liquid | 136.49 | J/mol×K | 232.81 | Calculated Property |
| Cp,liquid | 138.42 | J/mol×K | 254.20 | Calculated Property |
| Cp,liquid | 141.06 | J/mol×K | 275.60 | Calculated Property |
| Cp,liquid | 144.46 | J/mol×K | 297.00 | Calculated Property |
| Cp,liquid | 148.62 | J/mol×K | 318.40 | Calculated Property |
| Cp,liquid | 153.43 | J/mol×K | 339.80 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0034100; 0.0001752] | Pa×s | [167.23; 393.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.11370e+01 | |||
| Coefficient B | 8.71680e+02 | |||
| Coefficient C | 4.82270e-02 | |||
| Coefficient D | -1.21980e-07 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 167.23 | |||
| Temperature range, max. | 393.00 | |||
| η | 0.0034100 | Pa×s | 167.23 | Calculated Property |
| η | 0.0017375 | Pa×s | 192.32 | Calculated Property |
| η | 0.0010347 | Pa×s | 217.40 | Calculated Property |
| η | 0.0006860 | Pa×s | 242.49 | Calculated Property |
| η | 0.0004913 | Pa×s | 267.57 | Calculated Property |
| η | 0.0003726 | Pa×s | 292.66 | Calculated Property |
| η | 0.0002951 | Pa×s | 317.74 | Calculated Property |
| η | 0.0002418 | Pa×s | 342.83 | Calculated Property |
| η | 0.0002036 | Pa×s | 367.91 | Calculated Property |
| η | 0.0001752 | Pa×s | 393.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [38.97; 0.00] | kJ/mol | [167.23; 533.00] |
ChemSep v8.3 pure component data Compiled value
|
| 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 | 5.10140e+01 | |||
| Coefficient B | 1.04500e+00 | |||
| Coefficient C | -1.38340e+00 | |||
| Coefficient D | 1.19140e+00 | |||
| Coefficient E | -4.10550e-01 | |||
| Critical temperature, Tc (K) | 5.33000e+02 | |||
| Temperature range, min. | 167.23 | |||
| Temperature range, max. | 533.00 | |||
| ΔvapH | 38.97 | kJ/mol | 167.23 | Calculated Property |
| ΔvapH | 36.77 | kJ/mol | 207.87 | Calculated Property |
| ΔvapH | 34.62 | kJ/mol | 248.51 | Calculated Property |
| ΔvapH | 32.42 | kJ/mol | 289.15 | Calculated Property |
| ΔvapH | 30.08 | kJ/mol | 329.79 | Calculated Property |
| ΔvapH | 27.47 | kJ/mol | 370.44 | Calculated Property |
| ΔvapH | 24.46 | kJ/mol | 411.08 | Calculated Property |
| ΔvapH | 20.75 | kJ/mol | 451.72 | Calculated Property |
| ΔvapH | 15.61 | kJ/mol | 492.36 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 533.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 4259.64] | kPa | [247.75; 533.00] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.39945e+01 | |||
| Coefficient B | -2.73161e+03 | |||
| Coefficient C | -4.84660e+01 | |||
| Temperature range, min. | 247.75 | |||
| Temperature range, max. | 533.00 | |||
| Pvap | 1.33 | kPa | 247.75 | Calculated Property |
| Pvap | 8.74 | kPa | 279.44 | Calculated Property |
| Pvap | 36.43 | kPa | 311.14 | Calculated Property |
| Pvap | 111.60 | kPa | 342.83 | Calculated Property |
| Pvap | 275.05 | kPa | 374.53 | Calculated Property |
| Pvap | 577.75 | kPa | 406.22 | Calculated Property |
| Pvap | 1075.49 | kPa | 437.92 | Calculated Property |
| Pvap | 1823.28 | kPa | 469.61 | Calculated Property |
| Pvap | 2870.84 | kPa | 501.31 | Calculated Property |
| Pvap | 4259.64 | kPa | 533.00 | Calculated Property |
| Pvap | [2.14e-04; 4260.00] | kPa | [167.23; 528.50] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 7.75402e+01 | |||
| Coefficient B | -6.28717e+03 | |||
| Coefficient C | -9.49751e+00 | |||
| Coefficient D | 8.10195e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | Range stopped where the equation exceeds Pc; ChemSep gives it to 533 K. | |||
| Temperature range, min. | 167.23 | |||
| Temperature range, max. | 528.50 | |||
| Pvap | 2.14e-04 | kPa | 167.23 | Calculated Property |
| Pvap | 0.05 | kPa | 207.37 | Calculated Property |
| Pvap | 1.34 | kPa | 247.51 | Calculated Property |
| Pvap | 13.21 | kPa | 287.65 | Calculated Property |
| Pvap | 67.84 | kPa | 327.79 | Calculated Property |
| Pvap | 230.17 | kPa | 367.93 | Calculated Property |
| Pvap | 595.02 | kPa | 408.07 | Calculated Property |
| Pvap | 1281.49 | kPa | 448.22 | Calculated Property |
| Pvap | 2437.49 | kPa | 488.36 | Calculated Property |
| Pvap | 4260.00 | kPa | 528.50 | Calculated Property |
| Pvap | [1.30; 4251.33] | kPa | [247.15; 532.80] |
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 | 7.85436e+01 | |||
| Coefficient B | -6.34327e+03 | |||
| Coefficient C | -9.63519e+00 | |||
| Coefficient D | 7.77843e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 247.15 | |||
| Temperature range, max. | 532.80 | |||
| Pvap | 1.30 | kPa | 247.15 | Calculated Property |
| Pvap | 8.58 | kPa | 278.89 | Calculated Property |
| Pvap | 35.90 | kPa | 310.63 | Calculated Property |
| Pvap | 109.70 | kPa | 342.37 | Calculated Property |
| Pvap | 268.35 | kPa | 374.11 | Calculated Property |
| Pvap | 559.06 | kPa | 405.84 | Calculated Property |
| Pvap | 1035.51 | kPa | 437.58 | Calculated Property |
| Pvap | 1758.46 | kPa | 469.32 | Calculated Property |
| Pvap | 2800.03 | kPa | 501.06 | Calculated Property |
| Pvap | 4251.33 | kPa | 532.80 | Calculated Property |
| Pvap | [19.91; 270.08] | kPa | [296.58; 373.97] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.39615e+01 | |||
| Coefficient B | -2.72295e+03 | |||
| Coefficient C | -4.83660e+01 | |||
| Reference | Osborn and Douslin, 1966 | |||
| Temperature range, min. | 296.58 | |||
| Temperature range, max. | 373.97 | |||
| Pvap | 19.91 | kPa | 296.58 | Calculated Property |
| Pvap | 28.75 | kPa | 305.18 | Calculated Property |
| Pvap | 40.53 | kPa | 313.78 | Calculated Property |
| Pvap | 55.93 | kPa | 322.38 | Calculated Property |
| Pvap | 75.68 | kPa | 330.98 | Calculated Property |
| Pvap | 100.58 | kPa | 339.57 | Calculated Property |
| Pvap | 131.52 | kPa | 348.17 | Calculated Property |
| Pvap | 169.42 | kPa | 356.77 | Calculated Property |
| Pvap | 215.26 | kPa | 365.37 | Calculated Property |
| Pvap | 270.08 | kPa | 373.97 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [965.04; 299.84] | kg/m3 | [167.23; 533.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 8.12634e+01 | |||
| Coefficient B | 2.71020e-01 | |||
| Coefficient C | 5.33000e+02 | |||
| Coefficient D | 2.93640e-01 | |||
| Temperature range, min. | 167.23 | |||
| Temperature range, max. | 533.00 | |||
| ρl | 965.04 | kg/m3 | 167.23 | Calculated Property |
| ρl | 927.45 | kg/m3 | 207.87 | Calculated Property |
| ρl | 888.04 | kg/m3 | 248.51 | Calculated Property |
| ρl | 846.38 | kg/m3 | 289.15 | Calculated Property |
| ρl | 801.81 | kg/m3 | 329.79 | Calculated Property |
| ρl | 753.32 | kg/m3 | 370.44 | Calculated Property |
| ρl | 699.15 | kg/m3 | 411.08 | Calculated Property |
| ρl | 635.77 | kg/m3 | 451.72 | Calculated Property |
| ρl | 553.59 | kg/m3 | 492.36 | Calculated Property |
| ρl | 299.84 | kg/m3 | 533.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 0.02] | N/m | [167.15; 340.15] |
Jasper (1972), surface tension of pure liquid compounds Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K | |||
| Coefficient A | 6.27571e-02 | |||
| Coefficient B | -1.28600e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 167.15 | |||
| Temperature range, max. | 340.15 | |||
| γ | 0.04 | N/m | 167.15 | Calculated Property |
| γ | 0.04 | N/m | 186.37 | Calculated Property |
| γ | 0.04 | N/m | 205.59 | Calculated Property |
| γ | 0.03 | N/m | 224.82 | Calculated Property |
| γ | 0.03 | N/m | 244.04 | Calculated Property |
| γ | 0.03 | N/m | 263.26 | Calculated Property |
| γ | 0.03 | N/m | 282.48 | Calculated Property |
| γ | 0.02 | N/m | 301.71 | Calculated Property |
| γ | 0.02 | N/m | 320.93 | Calculated Property |
| γ | 0.02 | N/m | 340.15 | Calculated Property |
| γ | [0.04; 1.48e-05] | N/m | [167.23; 528.61] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K | |||
| Coefficient A | -1.02550e-02 | |||
| Coefficient B | 5.23770e+01 | |||
| Coefficient C | -3.25110e+00 | |||
| Coefficient D | 1.24940e-03 | |||
| Coefficient E | -7.46870e-06 | |||
| Comment | Range stopped where the equation turns negative; ChemSep gives it to 533 K. | |||
| Temperature range, min. | 167.23 | |||
| Temperature range, max. | 528.61 | |||
| γ | 0.04 | N/m | 167.23 | Calculated Property |
| γ | 0.04 | N/m | 207.38 | Calculated Property |
| γ | 0.03 | N/m | 247.54 | Calculated Property |
| γ | 0.03 | N/m | 287.69 | Calculated Property |
| γ | 0.02 | N/m | 327.84 | Calculated Property |
| γ | 0.02 | N/m | 368.00 | Calculated Property |
| γ | 0.01 | N/m | 408.15 | Calculated Property |
| γ | 0.01 | N/m | 448.30 | Calculated Property |
| γ | 0.00 | N/m | 488.46 | Calculated Property |
| γ | 1.48e-05 | N/m | 528.61 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.00; 0.08] | W/m×K | [167.23; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | 3.41680e-03 | |||
| Coefficient B | 6.21580e-01 | |||
| Coefficient C | 1.81160e+03 | |||
| Coefficient D | 1.62180e+05 | |||
| Temperature range, min. | 167.23 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.00 | W/m×K | 167.23 | Calculated Property |
| λgas | 0.01 | W/m×K | 259.76 | Calculated Property |
| λgas | 0.02 | W/m×K | 352.29 | Calculated Property |
| λgas | 0.03 | W/m×K | 444.82 | Calculated Property |
| λgas | 0.03 | W/m×K | 537.35 | Calculated Property |
| λgas | 0.04 | W/m×K | 629.88 | Calculated Property |
| λgas | 0.05 | W/m×K | 722.41 | Calculated Property |
| λgas | 0.06 | W/m×K | 814.94 | Calculated Property |
| λgas | 0.07 | W/m×K | 907.47 | Calculated Property |
| λgas | 0.08 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.17; 0.12] | W/m×K | [167.23; 339.80] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K | |||
| Coefficient A | -5.01720e-02 | |||
| Coefficient B | -1.12070e+00 | |||
| Coefficient C | -1.32080e+00 | |||
| Coefficient D | -8.22470e-04 | |||
| Coefficient E | -1.30760e-06 | |||
| Temperature range, min. | 167.23 | |||
| Temperature range, max. | 339.80 | |||
| λliquid | 0.17 | W/m×K | 167.23 | Calculated Property |
| λliquid | 0.17 | W/m×K | 186.40 | Calculated Property |
| λliquid | 0.16 | W/m×K | 205.58 | Calculated Property |
| λliquid | 0.16 | W/m×K | 224.75 | Calculated Property |
| λliquid | 0.15 | W/m×K | 243.93 | Calculated Property |
| λliquid | 0.15 | W/m×K | 263.10 | Calculated Property |
| λliquid | 0.14 | W/m×K | 282.28 | Calculated Property |
| λliquid | 0.13 | W/m×K | 301.45 | Calculated Property |
| λliquid | 0.13 | W/m×K | 320.63 | Calculated Property |
| λliquid | 0.12 | W/m×K | 339.80 | Calculated Property |
Similar Compounds
![Ethane, 1,1'-[methylenebis(thio)]bis-.](data:image/png;base64,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)
![2-[Ethylthio]ethanal.](data:image/png;base64,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)
Find more compounds similar to Ethane, (methylthio)-.
Mixtures
Sources
- KDB Vapor Pressure Data
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- Hankinson and Thomson (1979), COSTALD parameters ChEDL chemicals 1.5.2, from Hankinson, R. W.; Thomson, G. H. A New Correlation for Saturated Densities of Liquids and Their Mixtures. AIChE J. 1979, 25, 653-663.
- IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 8 ChEDL chemicals 1.5.2, from Tsonopoulos, C.; Ambrose, D. Vapor-Liquid Critical Properties of Elements and Compounds. 8. Organic Sulfur, Silicon, and Tin Compounds (C + H + S, Si, and Sn). J. Chem. Eng. Data 2001, 46, 480-485.
- Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- Cheméo Relay (1.0)
- 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
- Crippen Method
- Measurement of VLE (TPx or TPxy data) for hydrogen sulfide + (dimethylsulfide or ethylmethylsulfide or carbon disulfide) and methane solubilities in (dimethylsulfide or ethylmethylsulfide or methylmercaptan or ethylmercaptan)
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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