Property | Value | Unit | Source |
---|---|---|---|
ΔcH°solid | -5712.70 ± 1.90 | kJ/mol | NIST |
ΔfG° | -452.06 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -509.80 ± 3.20 | kJ/mol | NIST |
ΔfH°solid | -610.20 ± 2.00 | kJ/mol | NIST |
ΔfusH° | 27.85 | kJ/mol | Joback Calculated Property |
ΔsubH° | 100.00 ± 2.00 | kJ/mol | NIST |
ΔvapH° | 52.04 | kJ/mol | Joback Calculated Property |
log10WS | -2.00 | Crippen Calculated Property | |
logPoct/wat | 2.001 | Crippen Calculated Property | |
McVol | 151.670 | ml/mol | McGowan Calculated Property |
Pc | 2982.79 | kPa | Joback Calculated Property |
Tboil | 430.22 | K | Joback Calculated Property |
Tc | 592.13 | K | Joback Calculated Property |
Tfus | 218.48 | K | Joback Calculated Property |
Vc | 0.610 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [309.58; 384.11] | J/mol×K | [430.22; 592.13] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 320 340 360 380 450 500 550 | ||||
Cp,gas | 309.58 | J/mol×K | 430.22 | Joback Calculated Property |
Cp,gas | 323.15 | J/mol×K | 457.20 | Joback Calculated Property |
Cp,gas | 336.26 | J/mol×K | 484.19 | Joback Calculated Property |
Cp,gas | 348.90 | J/mol×K | 511.17 | Joback Calculated Property |
Cp,gas | 361.09 | J/mol×K | 538.16 | Joback Calculated Property |
Cp,gas | 372.83 | J/mol×K | 565.14 | Joback Calculated Property |
Cp,gas | 384.11 | J/mol×K | 592.13 | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [426.20; 624.10] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.36446e+01 | |||
Coefficient B | -4.38453e+03 | |||
Coefficient C | -9.79420e+01 | |||
Temperature range, min. | 426.20 | |||
Temperature range, max. | 624.10 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 600 | ||||
Pvap | 1.33 | kPa | 426.20 | Calculated Property |
Pvap | 3.08 | kPa | 448.19 | Calculated Property |
Pvap | 6.46 | kPa | 470.18 | Calculated Property |
Pvap | 12.46 | kPa | 492.17 | Calculated Property |
Pvap | 22.43 | kPa | 514.16 | Calculated Property |
Pvap | 38.05 | kPa | 536.14 | Calculated Property |
Pvap | 61.37 | kPa | 558.13 | Calculated Property |
Pvap | 94.77 | kPa | 580.12 | Calculated Property |
Pvap | 140.90 | kPa | 602.11 | Calculated Property |
Pvap | 202.65 | kPa | 624.10 | Calculated Property |
Pvap | [8.74e-04; 2497.45] | kPa | [318.00; 767.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.17265e+02 | |||
Coefficient B | -1.37461e+04 | |||
Coefficient C | -1.41440e+01 | |||
Coefficient D | 4.13287e-06 | |||
Temperature range, min. | 318.00 | |||
Temperature range, max. | 767.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 400 500 600 700 | ||||
Pvap | 8.74e-04 | kPa | 318.00 | Calculated Property |
Pvap | 0.05 | kPa | 367.89 | Calculated Property |
Pvap | 0.76 | kPa | 417.78 | Calculated Property |
Pvap | 6.18 | kPa | 467.67 | Calculated Property |
Pvap | 30.72 | kPa | 517.56 | Calculated Property |
Pvap | 107.99 | kPa | 567.44 | Calculated Property |
Pvap | 296.52 | kPa | 617.33 | Calculated Property |
Pvap | 680.40 | kPa | 667.22 | Calculated Property |
Pvap | 1368.52 | kPa | 717.11 | Calculated Property |
Pvap | 2497.45 | kPa | 767.00 | Calculated Property |
Find more compounds similar to Butane, 1,1'-sulfonylbis-.
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