Property | Value | Unit | Source |
---|---|---|---|
ΔcH°solid | [-3227.96; -3189.30] | kJ/mol |
![]() |
ΔcH°solid | -3189.30 ± 1.50 | kJ/mol | NIST |
ΔcH°solid | -3189.50 ± 0.42 | kJ/mol | NIST |
ΔcH°solid | -3227.96 | kJ/mol | NIST |
ΔfG° | -412.22 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -513.01 | kJ/mol | Joback Calculated Property |
ΔfH°solid | [-816.30; -816.17] | kJ/mol |
![]() |
ΔfH°solid | -816.30 ± 1.50 | kJ/mol | NIST |
ΔfH°solid | -816.17 | kJ/mol | NIST |
ΔfusH° | 21.50 | kJ/mol | Joback Calculated Property |
ΔsubH° | [98.11; 146.60] | kJ/mol |
![]() |
ΔsubH° | 146.60 ± 0.50 | kJ/mol | NIST |
ΔsubH° | 98.11 | kJ/mol | NIST |
ΔvapH° | 83.19 | kJ/mol | Joback Calculated Property |
IE | 9.90 ± 0.20 | eV | NIST |
log10WS | -1.59 | Crippen Calculated Property | |
logPoct/wat | 1.083 | Crippen Calculated Property | |
McVol | 114.700 | ml/mol | McGowan Calculated Property |
Pc | 5406.57 | kPa | Joback Calculated Property |
Tboil | 706.20 | K | Joback Calculated Property |
Tc | 907.67 | K | Joback Calculated Property |
Tfus | 703.10 | K | Solid-L... |
Vc | 0.425 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [282.80; 315.57] | J/mol×K | [706.20; 907.67] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 280 285 290 295 300 305 310 315 750 800 850 900 | ||||
Cp,gas | 282.80 | J/mol×K | 706.20 | Joback Calculated Property |
Cp,gas | 289.37 | J/mol×K | 739.78 | Joback Calculated Property |
Cp,gas | 295.47 | J/mol×K | 773.36 | Joback Calculated Property |
Cp,gas | 301.12 | J/mol×K | 806.93 | Joback Calculated Property |
Cp,gas | 306.34 | J/mol×K | 840.51 | Joback Calculated Property |
Cp,gas | 311.15 | J/mol×K | 874.09 | Joback Calculated Property |
Cp,gas | 315.57 | J/mol×K | 907.67 | Joback Calculated Property |
Cp,solid | 199.60 | J/mol×K | 323.00 | NIST |
η | [0.0000196; 0.0013822] | Pa×s | [440.36; 706.20] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 2.00e-4 4.00e-4 6.00e-4 8.00e-4 1.00e-3 1.20e-3 1.40e-3 500 600 700 | ||||
η | 0.0013822 | Pa×s | 440.36 | Joback Calculated Property |
η | 0.0004918 | Pa×s | 484.67 | Joback Calculated Property |
η | 0.0002081 | Pa×s | 528.97 | Joback Calculated Property |
η | 0.0001006 | Pa×s | 573.28 | Joback Calculated Property |
η | 0.0000539 | Pa×s | 617.59 | Joback Calculated Property |
η | 0.0000314 | Pa×s | 661.89 | Joback Calculated Property |
η | 0.0000196 | Pa×s | 706.20 | Joback Calculated Property |
ΔsubH | [131.00; 142.20] | kJ/mol | [471.00; 621.50] | ![]() |
ΔsubH | 142.20 ± 1.50 | kJ/mol | 471.00 | NIST |
ΔsubH | 139.20 | kJ/mol | 578.00 | NIST |
ΔsubH | 131.00 | kJ/mol | 578.00 | NIST |
ΔsubH | 139.30 ± 3.80 | kJ/mol | 621.50 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [2.36; 6322.50] | kPa | [567.15; 1113.00] |
KDB Vap...
![]() |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 4.38606e+02 | |||
Coefficient B | -3.45524e+04 | |||
Coefficient C | -6.04690e+01 | |||
Coefficient D | 2.04789e-05 | |||
Temperature range, min. | 567.15 | |||
Temperature range, max. | 1113.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 600 800 1000 | ||||
Pvap | 2.36 | kPa | 567.15 | Calculated Property |
Pvap | 8.05 | kPa | 627.80 | Calculated Property |
Pvap | 19.94 | kPa | 688.45 | Calculated Property |
Pvap | 41.95 | kPa | 749.10 | Calculated Property |
Pvap | 83.06 | kPa | 809.75 | Calculated Property |
Pvap | 166.04 | kPa | 870.40 | Calculated Property |
Pvap | 351.58 | kPa | 931.05 | Calculated Property |
Pvap | 815.78 | kPa | 991.70 | Calculated Property |
Pvap | 2124.96 | kPa | 1052.35 | Calculated Property |
Pvap | 6322.50 | kPa | 1113.00 | Calculated Property |
Find more compounds similar to Terephthalic acid.
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.