Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | 148.46 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -65.93 | kJ/mol | Joback Calculated Property |
ΔfusH° | 21.06 | kJ/mol | Joback Calculated Property |
ΔvapH° | 65.25 | kJ/mol | Joback Calculated Property |
log10WS | -3.63 | Crippen Calculated Property | |
logPoct/wat | 3.718 | Crippen Calculated Property | |
McVol | 180.560 | ml/mol | McGowan Calculated Property |
Pc | 2992.59 | kPa | Joback Calculated Property |
Inp | 1860.00 | NIST | |
Tboil | 608.20 | K | NIST |
Tc | 931.82 | K | Joback Calculated Property |
Tfus | 346.40 ± 0.05 | K | NIST |
Vc | 0.615 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [480.34; 562.39] | J/mol×K | [673.35; 931.82] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 480 500 520 540 560 700 800 900 | ||||
Cp,gas | 480.34 | J/mol×K | 673.35 | Joback Calculated Property |
Cp,gas | 496.80 | J/mol×K | 716.43 | Joback Calculated Property |
Cp,gas | 511.88 | J/mol×K | 759.51 | Joback Calculated Property |
Cp,gas | 525.77 | J/mol×K | 802.58 | Joback Calculated Property |
Cp,gas | 538.68 | J/mol×K | 845.66 | Joback Calculated Property |
Cp,gas | 550.83 | J/mol×K | 888.74 | Joback Calculated Property |
Cp,gas | 562.39 | J/mol×K | 931.82 | Joback Calculated Property |
η | [0.0000148; 0.0007455] | Pa×s | [425.79; 673.35] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 1.00e-4 2.00e-4 3.00e-4 4.00e-4 5.00e-4 6.00e-4 7.00e-4 8.00e-4 500 600 | ||||
η | 0.0007455 | Pa×s | 425.79 | Joback Calculated Property |
η | 0.0002905 | Pa×s | 467.05 | Joback Calculated Property |
η | 0.0001319 | Pa×s | 508.31 | Joback Calculated Property |
η | 0.0000674 | Pa×s | 549.57 | Joback Calculated Property |
η | 0.0000379 | Pa×s | 590.83 | Joback Calculated Property |
η | 0.0000229 | Pa×s | 632.09 | Joback Calculated Property |
η | 0.0000148 | Pa×s | 673.35 | Joback Calculated Property |
ΔfusH | [21.68; 22.80] | kJ/mol | [346.20; 346.40] | ![]() |
ΔfusH | 22.80 | kJ/mol | 346.20 | NIST |
ΔfusH | 21.68 | kJ/mol | 346.40 | NIST |
ΔfusH | 21.68 | kJ/mol | 346.40 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.66] | kPa | [460.77; 643.60] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.53045e+01 | |||
Coefficient B | -5.46100e+03 | |||
Coefficient C | -9.71150e+01 | |||
Temperature range, min. | 460.77 | |||
Temperature range, max. | 643.60 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 500 550 600 | ||||
Pvap | 1.33 | kPa | 460.77 | Calculated Property |
Pvap | 2.95 | kPa | 481.08 | Calculated Property |
Pvap | 6.03 | kPa | 501.40 | Calculated Property |
Pvap | 11.51 | kPa | 521.71 | Calculated Property |
Pvap | 20.70 | kPa | 542.03 | Calculated Property |
Pvap | 35.38 | kPa | 562.34 | Calculated Property |
Pvap | 57.82 | kPa | 582.66 | Calculated Property |
Pvap | 90.83 | kPa | 602.97 | Calculated Property |
Pvap | 137.79 | kPa | 623.29 | Calculated Property |
Pvap | 202.66 | kPa | 643.60 | Calculated Property |
Pvap | [1.29e-03; 2612.27] | kPa | [346.00; 834.00] |
KDB Vap...
![]() |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.07084e+02 | |||
Coefficient B | -1.41369e+04 | |||
Coefficient C | -1.25239e+01 | |||
Coefficient D | 2.83679e-06 | |||
Temperature range, min. | 346.00 | |||
Temperature range, max. | 834.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 400 600 800 | ||||
Pvap | 1.29e-03 | kPa | 346.00 | Calculated Property |
Pvap | 0.06 | kPa | 400.22 | Calculated Property |
Pvap | 0.93 | kPa | 454.44 | Calculated Property |
Pvap | 7.24 | kPa | 508.67 | Calculated Property |
Pvap | 34.93 | kPa | 562.89 | Calculated Property |
Pvap | 120.26 | kPa | 617.11 | Calculated Property |
Pvap | 324.86 | kPa | 671.33 | Calculated Property |
Pvap | 734.51 | kPa | 725.56 | Calculated Property |
Pvap | 1455.32 | kPa | 779.78 | Calculated Property |
Pvap | 2612.27 | kPa | 834.00 | Calculated Property |
Find more compounds similar to Phenol, 4-(1-methyl-1-phenylethyl)-.
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