Property | Value | Unit | Source |
---|---|---|---|
ΔcH°solid | [-2720.00; -2696.90] | kJ/mol | |
ΔcH°solid | -2697.20 ± 3.20 | kJ/mol | NIST |
ΔcH°solid | -2696.90 ± 2.70 | kJ/mol | NIST |
ΔcH°solid | -2703.10 ± 2.70 | kJ/mol | NIST |
ΔcH°solid | -2709.68 | kJ/mol | NIST |
ΔcH°solid | -2720.00 | kJ/mol | NIST |
ΔfG° | 18.90 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -140.94 | kJ/mol | Joback Calculated Property |
ΔfH°solid | [-235.50; -223.00] | kJ/mol | |
ΔfH°solid | -235.50 | kJ/mol | NIST |
ΔfH°solid | -223.00 | kJ/mol | NIST |
ΔfusH° | 33.45 | kJ/mol | Joback Calculated Property |
ΔvapH° | 78.08 | kJ/mol | Joback Calculated Property |
IE | 9.57 | eV | NIST |
log10WS | -2.32 | Crippen Calculated Property | |
logPoct/wat | 1.209 | Crippen Calculated Property | |
McVol | 112.350 | ml/mol | McGowan Calculated Property |
Pc | 5871.90 | kPa | Joback Calculated Property |
Inp | [257.00; 1512.00] | ||
Inp | 1512.00 | NIST | |
Inp | 1500.00 | NIST | |
Inp | 1471.00 | NIST | |
Inp | 257.00 | NIST | |
Inp | 258.24 | NIST | |
Inp | 1471.00 | NIST | |
Inp | 257.00 | NIST | |
Tboil | 752.64 | K | Joback Calculated Property |
Tc | 1038.65 | K | Joback Calculated Property |
Tfus | [385.95; 388.00] | K | |
Tfus | 385.95 | K | KDB |
Tfus | 388.00 ± 0.20 | K | NIST |
Vc | 0.394 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [287.91; 327.23] | J/mol×K | [752.64; 1038.65] | |
Cp,gas | 287.91 | J/mol×K | 752.64 | Joback Calculated Property |
Cp,gas | 295.32 | J/mol×K | 800.31 | Joback Calculated Property |
Cp,gas | 302.18 | J/mol×K | 847.98 | Joback Calculated Property |
Cp,gas | 308.65 | J/mol×K | 895.64 | Joback Calculated Property |
Cp,gas | 314.88 | J/mol×K | 943.31 | Joback Calculated Property |
Cp,gas | 321.02 | J/mol×K | 990.98 | Joback Calculated Property |
Cp,gas | 327.23 | J/mol×K | 1038.65 | Joback Calculated Property |
ΔfusH | [24.17; 26.19] | kJ/mol | [383.20; 388.00] | |
ΔfusH | 26.19 | kJ/mol | 383.20 | NIST |
ΔfusH | 24.17 | kJ/mol | 388.00 | NIST |
ΔfusH | 24.17 | kJ/mol | 388.00 | NIST |
ΔfusH | 24.17 | kJ/mol | 388.00 | NIST |
ΔsubH | [104.60; 104.60] | kJ/mol | [293.00; 313.00] | |
ΔsubH | 104.60 ± 4.20 | kJ/mol | 293.00 | NIST |
ΔsubH | 104.60 ± 4.20 | kJ/mol | 313.00 | NIST |
ΔfusS | 62.30 | J/mol×K | 388.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [2.69e-06; 4.65e-04] | kPa | [293.15; 333.15] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 3.00816e+01 | |||
Coefficient B | -1.25851e+04 | |||
Coefficient C | 3.92271e-03 | |||
Coefficient D | -6.67004e-09 | |||
Temperature range, min. | 293.15 | |||
Temperature range, max. | 333.15 | |||
Pvap | 2.69e-06 | kPa | 293.15 | Calculated Property |
Pvap | 5.10e-06 | kPa | 297.59 | Calculated Property |
Pvap | 9.50e-06 | kPa | 302.04 | Calculated Property |
Pvap | 1.74e-05 | kPa | 306.48 | Calculated Property |
Pvap | 3.13e-05 | kPa | 310.93 | Calculated Property |
Pvap | 5.53e-05 | kPa | 315.37 | Calculated Property |
Pvap | 9.64e-05 | kPa | 319.82 | Calculated Property |
Pvap | 1.65e-04 | kPa | 324.26 | Calculated Property |
Pvap | 2.79e-04 | kPa | 328.71 | Calculated Property |
Pvap | 4.65e-04 | kPa | 333.15 | Calculated Property |
Find more compounds similar to Phenol, 2,4-dinitro-.
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