Property | Value | Unit | Source |
---|---|---|---|
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 |
ΔfG° | 11.40 | kJ/mol | KDB |
ΔfH°gas | [-60.30; -59.66] | kJ/mol |
![]() |
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 | -0.96 | Crippen Calculated Property | |
logPoct/wat | 1.369 | Crippen Calculated Property | |
McVol | 69.480 | ml/mol | McGowan Calculated Property |
Pc | 4260.00 | kPa | KDB |
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 | |
I | [829.00; 859.00] |
![]() |
|
I | 859.00 | NIST | |
I | 829.00 | NIST | |
I | 859.00 | NIST | |
I | 859.00 | NIST | |
Tboil | [335.20; 340.00] | K |
![]() |
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 | KDB |
Tc | 553.00 | K | NIST |
Tfus | [167.20; 167.24] | K |
![]() |
Tfus | 167.20 | K | KDB |
Tfus | 167.24 ± 0.10 | K | NIST |
Ttriple | 167.23 ± 0.02 | K | NIST |
Vc | 0.258 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [103.79; 141.26] | J/mol×K | [336.82; 528.38] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 110 120 130 140 350 400 450 500 | ||||
Cp,gas | 103.79 | J/mol×K | 336.82 | Joback Calculated Property |
Cp,gas | 110.56 | J/mol×K | 368.75 | Joback Calculated Property |
Cp,gas | 117.12 | J/mol×K | 400.67 | Joback Calculated Property |
Cp,gas | 123.47 | J/mol×K | 432.60 | Joback Calculated Property |
Cp,gas | 129.61 | J/mol×K | 464.53 | Joback Calculated Property |
Cp,gas | 135.54 | J/mol×K | 496.46 | Joback Calculated Property |
Cp,gas | 141.26 | J/mol×K | 528.38 | Joback Calculated Property |
ΔfusH | [9.76; 9.76] | kJ/mol | [167.20; 167.20] | ![]() |
ΔfusH | 9.76 | kJ/mol | 167.20 | NIST |
ΔfusH | 9.76 | kJ/mol | 167.20 | NIST |
ΔvapH | [29.50; 33.70] | kJ/mol | [287.00; 340.20] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 30 31 32 33 34 300 320 340 | ||||
ΔvapH | 32.30 | kJ/mol | 287.00 | NIST |
ΔvapH | 32.00 ± 0.08 | kJ/mol | 301.00 | NIST |
ΔvapH | 31.64 | kJ/mol | 301.66 | NIST |
ΔvapH | 33.70 | kJ/mol | 308.00 | NIST |
ΔvapH | 31.80 | kJ/mol | 334.50 | NIST |
ΔvapH | 30.30 | kJ/mol | 338.00 | NIST |
ΔvapH | 29.53 | kJ/mol | 339.80 | NIST |
ΔvapH | 29.50 | kJ/mol | 340.20 | KDB |
Pvap | [1.00; 40.00] | kPa | [247.76; 313.35] | ![]() |
T(K) Vapor pressure (kPa) 0 5 10 15 20 25 30 35 40 260 280 300 | ||||
Pvap | 1.00 | kPa | 247.76 | Measure... |
Pvap | 6.00 | kPa | 272.96 | Measure... |
Pvap | 17.00 | kPa | 293.23 | Measure... |
Pvap | 17.00 | kPa | 293.41 | Measure... |
Pvap | 40.00 | kPa | 313.33 | Measure... |
Pvap | 40.00 | kPa | 313.35 | Measure... |
ρl | 837.00 | kg/m3 | 293.00 | KDB |
γ | 0.03 | N/m | 293.20 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 4259.64] | kPa | [247.75; 533.00] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
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 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 300 400 500 | ||||
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 | [1.30; 4251.33] | kPa | [247.15; 532.80] |
KDB Vap...
![]() |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 7.85436e+01 | |||
Coefficient B | -6.34327e+03 | |||
Coefficient C | -9.63519e+00 | |||
Coefficient D | 7.77843e-06 | |||
Temperature range, min. | 247.15 | |||
Temperature range, max. | 532.80 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 300 400 500 | ||||
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 |
Find more compounds similar to Ethane, (methylthio)-.
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.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.