Property | Value | Unit | Source |
---|---|---|---|
ΔcH°solid | -2642.22 ± 0.74 | kJ/mol | NIST |
ΔfG° | 35.44 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -25.40 | kJ/mol | NIST |
ΔfusH° | 20.96 | kJ/mol | Joback Calculated Property |
ΔsubH° | [60.84; 78.80] | kJ/mol |
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ΔsubH° | 78.80 ± 0.20 | kJ/mol | NIST |
ΔsubH° | 60.84 | kJ/mol | NIST |
ΔvapH° | 60.10 | kJ/mol | NIST |
IE | [8.90; 9.23] | eV |
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IE | 8.90 | eV | NIST |
IE | 9.23 ± 0.03 | eV | NIST |
IE | 9.11 | eV | NIST |
log10WS | [-4.63; -4.57] |
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|
log10WS | -4.63 | Aq. Sol... | |
log10WS | -4.57 | Estimat... | |
logPoct/wat | 4.300 | Crippen Calculated Property | |
McVol | 120.600 | ml/mol | McGowan Calculated Property |
Pc | 3646.53 | kPa | Joback Calculated Property |
Inp | [219.20; 1411.00] |
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|
Inp | 1388.00 | NIST | |
Inp | 1385.40 | NIST | |
Inp | 1385.30 | NIST | |
Inp | 1402.30 | NIST | |
Inp | 1370.00 | NIST | |
Inp | 1377.18 | NIST | |
Inp | 1343.88 | NIST | |
Inp | 1359.50 | NIST | |
Inp | 1366.00 | NIST | |
Inp | 1388.00 | NIST | |
Inp | 1366.00 | NIST | |
Inp | 1371.00 | NIST | |
Inp | 1388.00 | NIST | |
Inp | 1352.40 | NIST | |
Inp | 1362.21 | NIST | |
Inp | 1369.92 | NIST | |
Inp | 1362.00 | NIST | |
Inp | 1352.00 | NIST | |
Inp | 1353.00 | NIST | |
Inp | 1342.00 | NIST | |
Inp | 1345.00 | NIST | |
Inp | 1383.00 | NIST | |
Inp | 1336.00 | NIST | |
Inp | 1366.00 | NIST | |
Inp | 1375.00 | NIST | |
Inp | 1355.00 | NIST | |
Inp | 1411.00 | NIST | |
Inp | Outlier 237.00 | NIST | |
Inp | Outlier 219.20 | NIST | |
I | [1908.00; 1968.20] |
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|
I | 1914.10 | NIST | |
I | 1938.00 | NIST | |
I | 1968.20 | NIST | |
I | 1908.00 | NIST | |
I | 1941.00 | NIST | |
I | 1951.96 | NIST | |
I | 1931.77 | NIST | |
I | 1944.44 | NIST | |
I | 1920.95 | NIST | |
I | 1914.10 | NIST | |
Tboil | 527.20 | K | NIST |
Tc | 774.01 | K | Joback Calculated Property |
Tfus | [320.00; 320.40] | K |
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Tfus | 320.40 | K | Aq. Sol... |
Tfus | 320.00 ± 0.20 | K | NIST |
Ttriple | 319.68 ± 0.03 | K | NIST |
Vc | 0.460 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [186.59; 217.36] | J/mol×K | [528.02; 774.01] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 185 190 195 200 205 210 215 220 600 700 | ||||
Cp,gas | 186.59 | J/mol×K | 528.02 | Joback Calculated Property |
Cp,gas | 192.78 | J/mol×K | 569.02 | Joback Calculated Property |
Cp,gas | 198.52 | J/mol×K | 610.02 | Joback Calculated Property |
Cp,gas | 203.83 | J/mol×K | 651.01 | Joback Calculated Property |
Cp,gas | 208.73 | J/mol×K | 692.01 | Joback Calculated Property |
Cp,gas | 213.23 | J/mol×K | 733.01 | Joback Calculated Property |
Cp,gas | 217.36 | J/mol×K | 774.01 | Joback Calculated Property |
Cp,liquid | [225.17; 229.50] | J/mol×K | [327.15; 353.15] | ![]() |
T(K) Liquid phase heat capacity (J/mol×K) 225 226 227 228 229 330 340 350 | ||||
Cp,liquid | 225.17 | J/mol×K | 327.15 | Heat Ca... |
Cp,liquid | 225.49 | J/mol×K | 329.15 | Heat Ca... |
Cp,liquid | 225.82 | J/mol×K | 331.15 | Heat Ca... |
Cp,liquid | 226.14 | J/mol×K | 333.15 | Heat Ca... |
Cp,liquid | 226.47 | J/mol×K | 335.15 | Heat Ca... |
Cp,liquid | 226.80 | J/mol×K | 337.15 | Heat Ca... |
Cp,liquid | 227.13 | J/mol×K | 339.15 | Heat Ca... |
Cp,liquid | 227.46 | J/mol×K | 341.15 | Heat Ca... |
Cp,liquid | 227.80 | J/mol×K | 343.15 | Heat Ca... |
Cp,liquid | 228.13 | J/mol×K | 345.15 | Heat Ca... |
Cp,liquid | 228.47 | J/mol×K | 347.15 | Heat Ca... |
Cp,liquid | 228.81 | J/mol×K | 349.15 | Heat Ca... |
Cp,liquid | 229.16 | J/mol×K | 351.15 | Heat Ca... |
Cp,liquid | 229.50 | J/mol×K | 353.15 | Heat Ca... |
η | [0.0003001; 0.0013389] | Pa×s | [341.04; 528.02] | ![]() |
T(K) Dynamic viscosity (Pa×s) 2.00e-4 4.00e-4 6.00e-4 8.00e-4 1.00e-3 1.20e-3 1.40e-3 350 400 450 500 | ||||
η | 0.0013389 | Pa×s | 341.04 | Joback Calculated Property |
η | 0.0009401 | Pa×s | 372.20 | Joback Calculated Property |
η | 0.0006972 | Pa×s | 403.37 | Joback Calculated Property |
η | 0.0005397 | Pa×s | 434.53 | Joback Calculated Property |
η | 0.0004323 | Pa×s | 465.69 | Joback Calculated Property |
η | 0.0003561 | Pa×s | 496.86 | Joback Calculated Property |
η | 0.0003001 | Pa×s | 528.02 | Joback Calculated Property |
ΔfusH | [16.96; 17.00] | kJ/mol | [319.68; 320.00] | ![]() |
ΔfusH | 16.96 | kJ/mol | 319.68 | NIST |
ΔfusH | 17.00 | kJ/mol | 319.70 | NIST |
ΔfusH | 17.00 | kJ/mol | 320.00 | NIST |
ΔfusH | 17.00 | kJ/mol | 320.00 | NIST |
ΔvapH | 56.70 | kJ/mol | 434.00 | NIST |
ΔfusS | 53.10 | J/mol×K | 319.68 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 527.20 | K | 101.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [387.40; 562.66] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.39017e+01 | |||
Coefficient B | -4.07979e+03 | |||
Coefficient C | -8.77250e+01 | |||
Temperature range, min. | 387.40 | |||
Temperature range, max. | 562.66 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 550 | ||||
Pvap | 1.33 | kPa | 387.40 | Calculated Property |
Pvap | 3.06 | kPa | 406.87 | Calculated Property |
Pvap | 6.38 | kPa | 426.35 | Calculated Property |
Pvap | 12.29 | kPa | 445.82 | Calculated Property |
Pvap | 22.11 | kPa | 465.29 | Calculated Property |
Pvap | 37.57 | kPa | 484.77 | Calculated Property |
Pvap | 60.74 | kPa | 504.24 | Calculated Property |
Pvap | 94.08 | kPa | 523.71 | Calculated Property |
Pvap | 140.36 | kPa | 543.19 | Calculated Property |
Pvap | 202.65 | kPa | 562.66 | Calculated Property |
Find more compounds similar to Benzene, 1,2,3,4-tetrachloro-.
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