Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -4416.00 ± 0.63 | kJ/mol | NIST |
ΔfG° | -468.90 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -468.30 ± 2.60 | kJ/mol | NIST |
ΔfH°liquid | -548.19 ± 0.84 | kJ/mol | NIST |
ΔfusH° | 22.67 | kJ/mol | Joback Calculated Property |
ΔvapH° | 80.00 ± 2.00 | kJ/mol | NIST |
log10WS | -1.17 | Crippen Calculated Property | |
logPoct/wat | 1.221 | Crippen Calculated Property | |
McVol | 123.490 | ml/mol | McGowan Calculated Property |
Pc | 3722.56 | kPa | Joback Calculated Property |
Tboil | 542.00 ± 3.00 | K | NIST |
Tc | 547.33 | K | Joback Calculated Property |
Tfus | 195.94 | K | Joback Calculated Property |
Vc | 0.497 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [229.01; 291.65] | J/mol×K | [384.46; 547.33] | |
Cp,gas | 229.01 | J/mol×K | 384.46 | Joback Calculated Property |
Cp,gas | 240.33 | J/mol×K | 411.61 | Joback Calculated Property |
Cp,gas | 251.31 | J/mol×K | 438.75 | Joback Calculated Property |
Cp,gas | 261.93 | J/mol×K | 465.90 | Joback Calculated Property |
Cp,gas | 272.19 | J/mol×K | 493.04 | Joback Calculated Property |
Cp,gas | 282.10 | J/mol×K | 520.19 | Joback Calculated Property |
Cp,gas | 291.65 | J/mol×K | 547.33 | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [409.40; 574.25] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.49813e+01 | |||
Coefficient B | -4.66224e+03 | |||
Coefficient C | -9.21040e+01 | |||
Temperature range, min. | 409.40 | |||
Temperature range, max. | 574.25 | |||
Pvap | 1.33 | kPa | 409.40 | Calculated Property |
Pvap | 2.97 | kPa | 427.72 | Calculated Property |
Pvap | 6.10 | kPa | 446.03 | Calculated Property |
Pvap | 11.67 | kPa | 464.35 | Calculated Property |
Pvap | 20.99 | kPa | 482.67 | Calculated Property |
Pvap | 35.83 | kPa | 500.98 | Calculated Property |
Pvap | 58.42 | kPa | 519.30 | Calculated Property |
Pvap | 91.50 | kPa | 537.62 | Calculated Property |
Pvap | 138.33 | kPa | 555.93 | Calculated Property |
Pvap | 202.65 | kPa | 574.25 | Calculated Property |
Pvap | [9.76e-04; 3095.64] | kPa | [303.00; 763.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.02832e+02 | |||
Coefficient B | -1.22739e+04 | |||
Coefficient C | -1.21800e+01 | |||
Coefficient D | 3.66502e-06 | |||
Temperature range, min. | 303.00 | |||
Temperature range, max. | 763.00 | |||
Pvap | 9.76e-04 | kPa | 303.00 | Calculated Property |
Pvap | 0.06 | kPa | 354.11 | Calculated Property |
Pvap | 1.01 | kPa | 405.22 | Calculated Property |
Pvap | 8.31 | kPa | 456.33 | Calculated Property |
Pvap | 41.03 | kPa | 507.44 | Calculated Property |
Pvap | 142.38 | kPa | 558.56 | Calculated Property |
Pvap | 384.94 | kPa | 609.67 | Calculated Property |
Pvap | 869.35 | kPa | 660.78 | Calculated Property |
Pvap | 1721.65 | kPa | 711.89 | Calculated Property |
Pvap | 3095.64 | kPa | 763.00 | Calculated Property |
Find more compounds similar to Propane, 1,1'-sulfonylbis-.
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