Property | Value | Unit | Source |
---|---|---|---|
PAff | 871.80 | kJ/mol | NIST |
BasG | 842.10 | kJ/mol | NIST |
ΔcH°liquid | [-6102.03; -6102.00] | kJ/mol |
![]() |
ΔcH°liquid | -6102.03 | kJ/mol | NIST |
ΔcH°liquid | -6102.00 ± 1.30 | kJ/mol | NIST |
ΔfG° | 49.60 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-167.40; -167.20] | kJ/mol |
![]() |
ΔfH°gas | -167.40 | kJ/mol | NIST |
ΔfH°gas | -167.20 | kJ/mol | NIST |
ΔfH°liquid | [-220.70; -220.50] | kJ/mol |
![]() |
ΔfH°liquid | -220.70 ± 1.90 | kJ/mol | NIST |
ΔfH°liquid | -220.50 ± 1.50 | kJ/mol | NIST |
ΔfusH° | 20.61 | kJ/mol | Joback Calculated Property |
ΔvapH° | [40.30; 54.20] | kJ/mol |
![]() |
ΔvapH° | 52.96 | kJ/mol | NIST |
ΔvapH° | 40.30 | kJ/mol | NIST |
ΔvapH° | 53.00 | kJ/mol | NIST |
ΔvapH° | 54.20 ± 0.80 | kJ/mol | NIST |
ΔvapH° | 53.35 | kJ/mol | NIST |
IE | [8.20; 8.40] | eV |
![]() |
IE | 8.20 | eV | NIST |
IE | 8.40 ± 0.05 | eV | NIST |
IE | 8.22 | eV | NIST |
log10WS | -3.05 | Crippen Calculated Property | |
logPoct/wat | 3.320 | Crippen Calculated Property | |
McVol | 139.930 | ml/mol | McGowan Calculated Property |
Pc | 2579.34 | kPa | Joback Calculated Property |
Inp | [1050.00; 1092.00] |
![]() |
|
Inp | 1084.40 | NIST | |
Inp | 1088.50 | NIST | |
Inp | 1078.10 | NIST | |
Inp | 1081.30 | NIST | |
Inp | 1081.00 | NIST | |
Inp | 1059.00 | NIST | |
Inp | 1077.00 | NIST | |
Inp | 1081.00 | NIST | |
Inp | 1082.00 | NIST | |
Inp | 1084.00 | NIST | |
Inp | 1070.00 | NIST | |
Inp | 1064.00 | NIST | |
Inp | 1070.00 | NIST | |
Inp | 1064.00 | NIST | |
Inp | 1084.00 | NIST | |
Inp | 1077.00 | NIST | |
Inp | 1081.00 | NIST | |
Inp | 1081.00 | NIST | |
Inp | 1082.00 | NIST | |
Inp | 1086.00 | NIST | |
Inp | 1092.00 | NIST | |
Inp | 1060.00 | NIST | |
Inp | 1062.00 | NIST | |
Inp | 1056.00 | NIST | |
Inp | 1057.00 | NIST | |
Inp | 1058.00 | NIST | |
Inp | 1053.00 | NIST | |
Inp | 1056.00 | NIST | |
Inp | 1060.00 | NIST | |
Inp | 1055.00 | NIST | |
Inp | 1057.00 | NIST | |
Inp | 1079.00 | NIST | |
Inp | 1072.00 | NIST | |
Inp | 1075.00 | NIST | |
Inp | 1060.00 | NIST | |
Inp | 1055.00 | NIST | |
Inp | 1057.00 | NIST | |
Inp | 1066.00 | NIST | |
Inp | 1060.00 | NIST | |
Inp | 1062.00 | NIST | |
Inp | 1056.00 | NIST | |
Inp | 1050.00 | NIST | |
Inp | 1053.00 | NIST | |
Inp | 1061.00 | NIST | |
Inp | 1056.00 | NIST | |
Inp | 1058.00 | NIST | |
Inp | 1057.00 | NIST | |
Inp | 1084.00 | NIST | |
Inp | 1088.00 | NIST | |
Inp | 1078.00 | NIST | |
Inp | 1081.00 | NIST | |
Inp | 1073.00 | NIST | |
Inp | 1082.00 | NIST | |
Inp | 1073.00 | NIST | |
Inp | 1057.00 | NIST | |
Inp | 1073.00 | NIST | |
Inp | 1084.40 | NIST | |
Inp | 1059.00 | NIST | |
Inp | 1070.00 | NIST | |
Inp | 1077.00 | NIST | |
Inp | 1092.00 | NIST | |
Inp | 1058.00 | NIST | |
Inp | 1057.00 | NIST | |
Inp | 1055.00 | NIST | |
Inp | 1056.00 | NIST | |
I | [1254.00; 1289.00] |
![]() |
|
I | 1270.60 | NIST | |
I | 1256.60 | NIST | |
I | 1286.00 | NIST | |
I | 1289.00 | NIST | |
I | 1262.00 | NIST | |
I | 1270.00 | NIST | |
I | 1254.00 | NIST | |
I | 1270.00 | NIST | |
I | 1256.00 | NIST | |
I | 1270.00 | NIST | |
S°liquid | 405.09 | J/mol×K | NIST |
Tboil | [458.20; 461.95] | K |
![]() |
Tboil | 461.70 | K | NIST |
Tboil | 461.95 ± 0.30 | K | NIST |
Tboil | 458.20 ± 0.60 | K | NIST |
Tc | 636.81 | K | Joback Calculated Property |
Tfus | [198.12; 221.85] | K |
![]() |
Tfus | 221.85 | K | KDB |
Tfus | 198.12 ± 0.02 | K | NIST |
Ttriple | [198.13; 198.13] | K |
![]() |
Ttriple | 198.13 ± 0.04 | K | NIST |
Ttriple | 198.13 ± 0.03 | K | NIST |
Vc | 0.537 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [286.95; 362.10] | J/mol×K | [451.22; 636.81] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 280 300 320 340 360 450 500 550 600 | ||||
Cp,gas | 286.95 | J/mol×K | 451.22 | Joback Calculated Property |
Cp,gas | 300.83 | J/mol×K | 482.15 | Joback Calculated Property |
Cp,gas | 314.15 | J/mol×K | 513.08 | Joback Calculated Property |
Cp,gas | 326.93 | J/mol×K | 544.01 | Joback Calculated Property |
Cp,gas | 339.17 | J/mol×K | 574.95 | Joback Calculated Property |
Cp,gas | 350.89 | J/mol×K | 605.88 | Joback Calculated Property |
Cp,gas | 362.10 | J/mol×K | 636.81 | Joback Calculated Property |
Cp,liquid | 284.34 | J/mol×K | 298.15 | NIST |
ΔfusH | [19.41; 19.43] | kJ/mol | [198.10; 198.13] | ![]() |
ΔfusH | 19.41 | kJ/mol | 198.10 | NIST |
ΔfusH | 19.41 | kJ/mol | 198.10 | NIST |
ΔfusH | 19.43 | kJ/mol | 198.13 | NIST |
ΔvapH | [44.80; 46.50] | kJ/mol | [338.50; 430.00] | ![]() |
ΔvapH | 44.80 | kJ/mol | 338.50 | NIST |
ΔvapH | 46.50 | kJ/mol | 430.00 | NIST |
ΔfusS | 98.05 | J/mol×K | 198.13 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.66] | kPa | [340.12; 492.01] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.43227e+01 | |||
Coefficient B | -3.82370e+03 | |||
Coefficient C | -6.76820e+01 | |||
Temperature range, min. | 340.12 | |||
Temperature range, max. | 492.01 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
Pvap | 1.33 | kPa | 340.12 | Calculated Property |
Pvap | 3.02 | kPa | 357.00 | Calculated Property |
Pvap | 6.26 | kPa | 373.87 | Calculated Property |
Pvap | 12.03 | kPa | 390.75 | Calculated Property |
Pvap | 21.64 | kPa | 407.63 | Calculated Property |
Pvap | 36.84 | kPa | 424.50 | Calculated Property |
Pvap | 59.78 | kPa | 441.38 | Calculated Property |
Pvap | 93.02 | kPa | 458.26 | Calculated Property |
Pvap | 139.53 | kPa | 475.13 | Calculated Property |
Pvap | 202.66 | kPa | 492.01 | Calculated Property |
Pvap | [0.12; 2648.39] | kPa | [303.15; 650.00] |
KDB Vap...
![]() |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 2.52296e+02 | |||
Coefficient B | -1.67842e+04 | |||
Coefficient C | -3.51983e+01 | |||
Coefficient D | 2.22154e-05 | |||
Temperature range, min. | 303.15 | |||
Temperature range, max. | 650.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 300 400 500 600 | ||||
Pvap | 0.12 | kPa | 303.15 | Calculated Property |
Pvap | 1.53 | kPa | 341.69 | Calculated Property |
Pvap | 9.59 | kPa | 380.23 | Calculated Property |
Pvap | 36.91 | kPa | 418.77 | Calculated Property |
Pvap | 103.29 | kPa | 457.31 | Calculated Property |
Pvap | 234.69 | kPa | 495.84 | Calculated Property |
Pvap | 467.25 | kPa | 534.38 | Calculated Property |
Pvap | 859.69 | kPa | 572.92 | Calculated Property |
Pvap | 1518.64 | kPa | 611.46 | Calculated Property |
Pvap | 2648.39 | kPa | 650.00 | Calculated Property |
Find more compounds similar to Butyl sulfide.
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.