Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | [-6942.40; -6939.00] | kJ/mol | |
ΔcH°liquid | -6942.40 ± 2.80 | kJ/mol | NIST |
ΔcH°liquid | -6939.00 ± 2.00 | kJ/mol | NIST |
ΔfG° | 104.96 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-191.80; -188.30] | kJ/mol | |
ΔfH°gas | -188.30 ± 3.10 | kJ/mol | NIST |
ΔfH°gas | -191.80 | kJ/mol | NIST |
ΔfH°liquid | [-248.00; -244.50] | kJ/mol | |
ΔfH°liquid | -244.50 ± 3.00 | kJ/mol | NIST |
ΔfH°liquid | -248.00 ± 2.00 | kJ/mol | NIST |
ΔfusH° | 2.65 | kJ/mol | Joback Calculated Property |
ΔsubH° | 63.60 ± 0.80 | kJ/mol | NIST |
ΔvapH° | [56.10; 56.20] | kJ/mol | |
ΔvapH° | 56.10 ± 0.10 | kJ/mol | NIST |
ΔvapH° | 56.20 | kJ/mol | NIST |
ΔvapH° | 56.10 | kJ/mol | NIST |
log10WS | -3.97 | Crippen Calculated Property | |
logPoct/wat | 3.901 | Crippen Calculated Property | |
McVol | 144.130 | ml/mol | McGowan Calculated Property |
Pc | 3049.04 | kPa | Joback Calculated Property |
Tboil | 490.82 | K | Joback Calculated Property |
Tc | 728.55 | K | Joback Calculated Property |
Tfus | [248.65; 248.70] | K | |
Tfus | 248.65 ± 0.50 | K | NIST |
Tfus | 248.70 ± 0.50 | K | NIST |
Tfus | 248.70 ± 0.60 | K | NIST |
Vc | 0.524 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [334.74; 455.56] | J/mol×K | [490.82; 728.55] | |
T(K) Ideal gas heat capacity (J/mol×K) 340 360 380 400 420 440 460 500 600 700 | ||||
Cp,gas | 334.74 | J/mol×K | 490.82 | Joback Calculated Property |
Cp,gas | 358.84 | J/mol×K | 530.44 | Joback Calculated Property |
Cp,gas | 381.11 | J/mol×K | 570.06 | Joback Calculated Property |
Cp,gas | 401.73 | J/mol×K | 609.68 | Joback Calculated Property |
Cp,gas | 420.89 | J/mol×K | 649.31 | Joback Calculated Property |
Cp,gas | 438.77 | J/mol×K | 688.93 | Joback Calculated Property |
Cp,gas | 455.56 | J/mol×K | 728.55 | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [0.19; 202.63] | kPa | [369.00; 504.09] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.55909e+01 | |||
Coefficient B | -3.44213e+03 | |||
Coefficient C | -1.69238e+02 | |||
Temperature range, min. | 369.00 | |||
Temperature range, max. | 504.09 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
Pvap | 0.19 | kPa | 369.00 | Calculated Property |
Pvap | 0.65 | kPa | 384.01 | Calculated Property |
Pvap | 1.84 | kPa | 399.02 | Calculated Property |
Pvap | 4.62 | kPa | 414.03 | Calculated Property |
Pvap | 10.40 | kPa | 429.04 | Calculated Property |
Pvap | 21.45 | kPa | 444.05 | Calculated Property |
Pvap | 41.03 | kPa | 459.06 | Calculated Property |
Pvap | 73.63 | kPa | 474.07 | Calculated Property |
Pvap | 125.08 | kPa | 489.08 | Calculated Property |
Pvap | 202.63 | kPa | 504.09 | Calculated Property |
Find more compounds similar to Spiro[5.5]undecane.
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