Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | -6.16 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -243.24 | kJ/mol | Joback Calculated Property |
ΔfusH° | 30.70 | kJ/mol | Solubil... |
ΔvapH° | 78.27 | kJ/mol | Joback Calculated Property |
log10WS | -2.82 | Aq. Sol... | |
logPoct/wat | 3.424 | Crippen Calculated Property | |
McVol | 186.430 | ml/mol | McGowan Calculated Property |
Pc | 3547.31 | kPa | Joback Calculated Property |
Inp | 2108.00 | NIST | |
Tboil | 753.97 | K | Joback Calculated Property |
Tc | 1018.62 | K | Joback Calculated Property |
Tfus | 427.65 | K | Aq. Sol... |
Vc | 0.581 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [528.97; 608.03] | J/mol×K | [753.97; 1018.62] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 540 560 580 600 800 900 1000 | ||||
Cp,gas | 528.97 | J/mol×K | 753.97 | Joback Calculated Property |
Cp,gas | 543.20 | J/mol×K | 798.08 | Joback Calculated Property |
Cp,gas | 556.63 | J/mol×K | 842.19 | Joback Calculated Property |
Cp,gas | 569.54 | J/mol×K | 886.29 | Joback Calculated Property |
Cp,gas | 582.22 | J/mol×K | 930.40 | Joback Calculated Property |
Cp,gas | 594.96 | J/mol×K | 974.51 | Joback Calculated Property |
Cp,gas | 608.03 | J/mol×K | 1018.62 | Joback Calculated Property |
η | [0.0000007; 0.0000313] | Pa×s | [537.51; 753.97] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-6 1.00e-5 1.50e-5 2.00e-5 2.50e-5 3.00e-5 600 700 | ||||
η | 0.0000313 | Pa×s | 537.51 | Joback Calculated Property |
η | 0.0000137 | Pa×s | 573.59 | Joback Calculated Property |
η | 0.0000066 | Pa×s | 609.66 | Joback Calculated Property |
η | 0.0000035 | Pa×s | 645.74 | Joback Calculated Property |
η | 0.0000019 | Pa×s | 681.82 | Joback Calculated Property |
η | 0.0000012 | Pa×s | 717.89 | Joback Calculated Property |
η | 0.0000007 | Pa×s | 753.97 | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [507.33; 665.02] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.44248e+01 | |||
Coefficient B | -4.04412e+03 | |||
Coefficient C | -2.21266e+02 | |||
Temperature range, min. | 507.33 | |||
Temperature range, max. | 665.02 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 550 600 650 | ||||
Pvap | 1.33 | kPa | 507.33 | Calculated Property |
Pvap | 3.01 | kPa | 524.85 | Calculated Property |
Pvap | 6.24 | kPa | 542.37 | Calculated Property |
Pvap | 11.97 | kPa | 559.89 | Calculated Property |
Pvap | 21.53 | kPa | 577.41 | Calculated Property |
Pvap | 36.67 | kPa | 594.94 | Calculated Property |
Pvap | 59.55 | kPa | 612.46 | Calculated Property |
Pvap | 92.76 | kPa | 629.98 | Calculated Property |
Pvap | 139.32 | kPa | 647.50 | Calculated Property |
Pvap | 202.63 | kPa | 665.02 | Calculated Property |
Pvap | [4.93e-03; 3034.89] | kPa | [426.15; 849.00] |
KDB Vap...
![]() |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 2.95077e+02 | |||
Coefficient B | -3.04193e+04 | |||
Coefficient C | -3.80451e+01 | |||
Coefficient D | 7.42083e-06 | |||
Temperature range, min. | 426.15 | |||
Temperature range, max. | 849.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 500 600 700 800 | ||||
Pvap | 4.93e-03 | kPa | 426.15 | Calculated Property |
Pvap | 0.15 | kPa | 473.13 | Calculated Property |
Pvap | 1.94 | kPa | 520.12 | Calculated Property |
Pvap | 13.42 | kPa | 567.10 | Calculated Property |
Pvap | 59.43 | kPa | 614.08 | Calculated Property |
Pvap | 189.64 | kPa | 661.07 | Calculated Property |
Pvap | 475.17 | kPa | 708.05 | Calculated Property |
Pvap | 995.15 | kPa | 755.03 | Calculated Property |
Pvap | 1824.84 | kPa | 802.02 | Calculated Property |
Pvap | 3034.89 | kPa | 849.00 | Calculated Property |
Find more compounds similar to Phenol, 4,4'-(1-methylethylidene)bis-.
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