Property | Value | Unit | Source |
---|---|---|---|
ΔvapH° | [48.50; 53.90] | kJ/mol | |
ΔvapH° | 53.90 | kJ/mol | NIST |
ΔvapH° | 52.30 | kJ/mol | NIST |
ΔvapH° | 48.50 ± 0.30 | kJ/mol | NIST |
IE | 9.77 | eV | NIST |
log10WS | 0.68 | Crippen Calculated Property | |
logPoct/wat | 1.568 | Crippen Calculated Property | |
Pc | 2040.00 | kPa | Vapor-L... |
Inp | [847.00; 869.00] | ||
Inp | Outlier 869.00 | NIST | |
Inp | 850.00 | NIST | |
Inp | 851.20 | NIST | |
Inp | 847.00 | NIST | |
Inp | 850.00 | NIST | |
Inp | 850.00 | NIST | |
Inp | 847.00 | NIST | |
S°liquid | 533.10 | J/mol×K | NIST |
Tboil | [439.70; 442.00] | K | |
Tboil | 439.70 ± 1.00 | K | NIST |
Tboil | 442.00 | K | NIST |
Tboil | 441.95 ± 0.50 | K | NIST |
Tfus | 191.00 ± 0.10 | K | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,liquid | [352.10; 364.40] | J/mol×K | [298.15; 298.15] | |
Cp,liquid | 364.40 | J/mol×K | 298.15 | NIST |
Cp,liquid | 352.10 | J/mol×K | 298.15 | NIST |
ΔfusH | [11.14; 13.20] | kJ/mol | [187.70; 191.00] | |
ΔfusH | 13.20 | kJ/mol | 187.70 | NIST |
ΔfusH | 11.14 | kJ/mol | 191.00 | NIST |
ΔfusH | 11.14 | kJ/mol | 191.00 | NIST |
ΔvapH | [40.90; 50.00] | kJ/mol | [365.00; 420.50] | |
ΔvapH | 49.50 | kJ/mol | 365.00 | NIST |
ΔvapH | 50.00 | kJ/mol | 376.50 | NIST |
ΔvapH | 40.90 | kJ/mol | 420.50 | NIST |
Pvap | [24.00; 53.32] | kPa | [393.40; 419.20] | |
Pvap | 24.00 | kPa | 393.40 | Vapor-L... |
Pvap | 53.32 | kPa | 419.20 | Vapor-L... |
n0 | [1.38250; 1.38350] | [293.15; 298.15] | ||
n0 | 1.38350 | 293.15 | Isobari... | |
n0 | 1.38250 | 298.15 | (Vapor ... | |
ρl | 1032.00 | kg/m3 | 293.15 | Bubble ... |
ΔfusS | [58.33; 70.32] | J/mol×K | [187.70; 191.00] | |
ΔfusS | 70.32 | J/mol×K | 187.70 | NIST |
ΔfusS | 58.33 | J/mol×K | 191.00 | NIST |
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