Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | 83.28 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -249.14 | kJ/mol | Joback Calculated Property |
ΔfusH° | 30.97 | kJ/mol | Joback Calculated Property |
ΔvapH° | 49.12 | kJ/mol | Joback Calculated Property |
log10WS | -4.73 | Crippen Calculated Property | |
logPoct/wat | 4.880 | Crippen Calculated Property | |
McVol | 196.290 | ml/mol | McGowan Calculated Property |
Pc | 1806.16 | kPa | Joback Calculated Property |
Inp | [1457.00; 1499.00] | ||
Inp | 1473.00 | NIST | |
Inp | 1468.00 | NIST | |
Inp | 1473.00 | NIST | |
Inp | 1473.00 | NIST | |
Inp | Outlier 1499.00 | NIST | |
Inp | 1457.00 | NIST | |
Inp | 1473.00 | NIST | |
Inp | 1472.00 | NIST | |
Inp | 1473.00 | NIST | |
Inp | 1473.00 | NIST | |
Inp | 1473.00 | NIST | |
I | [1667.00; 1678.00] | ||
I | 1667.00 | NIST | |
I | 1678.00 | NIST | |
I | 1667.00 | NIST | |
Tboil | 503.20 | K | NIST |
Tc | 721.16 | K | Joback Calculated Property |
Tfus | 259.40 | K | Joback Calculated Property |
Vc | 0.761 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [472.53; 565.21] | J/mol×K | [542.74; 721.16] | |
T(K) Ideal gas heat capacity (J/mol×K) 480 500 520 540 560 550 600 650 700 | ||||
Cp,gas | 472.53 | J/mol×K | 542.74 | Joback Calculated Property |
Cp,gas | 489.74 | J/mol×K | 572.48 | Joback Calculated Property |
Cp,gas | 506.22 | J/mol×K | 602.21 | Joback Calculated Property |
Cp,gas | 521.99 | J/mol×K | 631.95 | Joback Calculated Property |
Cp,gas | 537.07 | J/mol×K | 661.69 | Joback Calculated Property |
Cp,gas | 551.47 | J/mol×K | 691.42 | Joback Calculated Property |
Cp,gas | 565.21 | J/mol×K | 721.16 | Joback Calculated Property |
ΔvapH | 72.40 | kJ/mol | 373.50 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [378.52; 533.55] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.49517e+01 | |||
Coefficient B | -4.36250e+03 | |||
Coefficient C | -8.10260e+01 | |||
Temperature range, min. | 378.52 | |||
Temperature range, max. | 533.55 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
Pvap | 1.33 | kPa | 378.52 | Calculated Property |
Pvap | 2.97 | kPa | 395.75 | Calculated Property |
Pvap | 6.11 | kPa | 412.97 | Calculated Property |
Pvap | 11.68 | kPa | 430.20 | Calculated Property |
Pvap | 21.01 | kPa | 447.42 | Calculated Property |
Pvap | 35.87 | kPa | 464.65 | Calculated Property |
Pvap | 58.47 | kPa | 481.87 | Calculated Property |
Pvap | 91.56 | kPa | 499.10 | Calculated Property |
Pvap | 138.36 | kPa | 516.32 | Calculated Property |
Pvap | 202.63 | kPa | 533.55 | Calculated Property |
Find more compounds similar to Hexane, 1,1'-thiobis-.
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