Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -830.00 ± 10.00 | kJ/mol | NIST |
μ | 0.00 | debye | KDB |
η | [0.0008474; 0.0008900] | Pa×s |
![]() |
η | 0.0008474 | Pa×s | Densiti... |
η | 0.0008900 | Pa×s | Studies... |
EA | [0.50; 0.64] | eV |
![]() |
EA | 0.64 ± 0.03 | eV | NIST |
EA | 0.50 | eV | NIST |
ΔfG° | 22.61 | kJ/mol | KDB |
ΔfH°gas | [-24.00; -12.14] | kJ/mol |
![]() |
ΔfH°gas | -12.14 | kJ/mol | KDB |
ΔfH°gas | -24.00 ± 4.00 | kJ/mol | NIST |
ΔfH°gas | -15.00 | kJ/mol | NIST |
ΔfH°liquid | [-64.00; -54.40] | kJ/mol |
![]() |
ΔfH°liquid | -64.00 ± 4.00 | kJ/mol | NIST |
ΔfH°liquid | -54.40 | kJ/mol | NIST |
ΔfusH° | 15.31 | kJ/mol | Joback Calculated Property |
ΔvapH° | [39.70; 39.72] | kJ/mol |
![]() |
ΔvapH° | 39.72 | kJ/mol | NIST |
ΔvapH° | 39.72 ± 0.05 | kJ/mol | NIST |
ΔvapH° | 39.70 ± 0.10 | kJ/mol | NIST |
ΔvapH° | 39.70 ± 0.84 | kJ/mol | NIST |
IE | [9.32; 9.51] | eV |
![]() |
IE | 9.33 ± 0.00 | eV | NIST |
IE | 9.33 ± 0.00 | eV | NIST |
IE | 9.51 | eV | NIST |
IE | 9.34 | eV | NIST |
IE | 9.32 ± 0.01 | eV | NIST |
IE | 9.32 | eV | NIST |
IE | 9.50 | eV | NIST |
log10WS | [-2.60; -2.54] |
![]() |
|
log10WS | -2.60 | Aq. Sol... | |
log10WS | -2.54 | Estimat... | |
logPoct/wat | 3.068 | Crippen Calculated Property | |
McVol | 83.700 | ml/mol | McGowan Calculated Property |
Pc | 4760.00 | kPa | KDB |
Inp | [785.00; 832.30] |
![]() |
|
Inp | 825.59 | NIST | |
Inp | Outlier 832.30 | NIST | |
Inp | 803.00 | NIST | |
Inp | 799.00 | NIST | |
Inp | 801.00 | NIST | |
Inp | 809.00 | NIST | |
Inp | 814.00 | NIST | |
Inp | 804.00 | NIST | |
Inp | 806.00 | NIST | |
Inp | 825.00 | NIST | |
Inp | 814.00 | NIST | |
Inp | 801.00 | NIST | |
Inp | 815.45 | NIST | |
Inp | 817.10 | NIST | |
Inp | 815.90 | NIST | |
Inp | 794.80 | NIST | |
Inp | 809.30 | NIST | |
Inp | 804.00 | NIST | |
Inp | 804.00 | NIST | |
Inp | 815.00 | NIST | |
Inp | 796.00 | NIST | |
Inp | 801.00 | NIST | |
Inp | 806.00 | NIST | |
Inp | 814.00 | NIST | |
Inp | 807.00 | NIST | |
Inp | 796.52 | NIST | |
Inp | 819.00 | NIST | |
Inp | 823.00 | NIST | |
Inp | 794.00 | NIST | |
Inp | 808.00 | NIST | |
Inp | 814.00 | NIST | |
Inp | 808.00 | NIST | |
Inp | 815.00 | NIST | |
Inp | 806.00 | NIST | |
Inp | 794.51 | NIST | |
Inp | 794.00 | NIST | |
Inp | 803.00 | NIST | |
Inp | 806.00 | NIST | |
Inp | 811.00 | NIST | |
Inp | 802.00 | NIST | |
Inp | 793.00 | NIST | |
Inp | 793.00 | NIST | |
Inp | 811.00 | NIST | |
Inp | 797.00 | NIST | |
Inp | 816.00 | NIST | |
Inp | 785.00 | NIST | |
Inp | 800.00 | NIST | |
Inp | 789.00 | NIST | |
Inp | 797.00 | NIST | |
Inp | 789.00 | NIST | |
Inp | 796.00 | NIST | |
Inp | 814.00 | NIST | |
Inp | 794.00 | NIST | |
Inp | 793.00 | NIST | |
Inp | 785.00 | NIST | |
Inp | 796.00 | NIST | |
Inp | 806.00 | NIST | |
Inp | 823.00 | NIST | |
I | [1012.00; 1059.96] |
![]() |
|
I | 1044.00 | NIST | |
I | 1038.00 | NIST | |
I | 1050.23 | NIST | |
I | Outlier 1059.96 | NIST | |
I | 1036.20 | NIST | |
I | 1030.00 | NIST | |
I | 1024.00 | NIST | |
I | 1022.00 | NIST | |
I | 1022.00 | NIST | |
I | 1021.00 | NIST | |
I | 1026.00 | NIST | |
I | 1045.00 | NIST | |
I | 1012.00 | NIST | |
I | 1012.00 | NIST | |
I | 1018.00 | NIST | |
I | 1021.00 | NIST | |
I | 1024.00 | NIST | |
I | 1044.00 | NIST | |
I | 1030.00 | NIST | |
S°liquid | 240.60 | J/mol×K | NIST |
Tboil | [394.15; 394.45] | K |
![]() |
Tboil | 394.40 | K | KDB |
Tboil | 394.45 | K | Excess ... |
Tboil | 394.15 | K | Excess ... |
Tboil | 394.15 | K | Vapor-L... |
Tboil | 394.15 | K | Isobari... |
Tc | [620.00; 620.20] | K |
![]() |
Tc | 620.20 | K | KDB |
Tc | 620.00 | K | NIST |
Tfus | [250.60; 251.00] | K |
![]() |
Tfus | 250.80 | K | KDB |
Tfus | 251.00 | K | Aq. Sol... |
Tfus | 250.97 ± 0.05 | K | NIST |
Tfus | 250.60 ± 0.60 | K | NIST |
Ttriple | 250.81 ± 0.02 | K | NIST |
Vc | 0.326 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [100.86; 114.10] | J/mol×K | [398.80; 620.38] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 100 102 104 106 108 110 112 114 400 500 600 | ||||
Cp,gas | 100.86 | J/mol×K | 398.80 | Joback Calculated Property |
Cp,gas | 103.82 | J/mol×K | 435.73 | Joback Calculated Property |
Cp,gas | 106.43 | J/mol×K | 472.66 | Joback Calculated Property |
Cp,gas | 108.74 | J/mol×K | 509.59 | Joback Calculated Property |
Cp,gas | 110.77 | J/mol×K | 546.52 | Joback Calculated Property |
Cp,gas | 112.54 | J/mol×K | 583.45 | Joback Calculated Property |
Cp,gas | 114.10 | J/mol×K | 620.38 | Joback Calculated Property |
Cp,liquid | [139.70; 157.90] | J/mol×K | [298.00; 298.15] | ![]() |
T(K) Liquid phase heat capacity (J/mol×K) 140 145 150 155 298 298.05 298.09999999999997 298.15 | ||||
Cp,liquid | 139.70 | J/mol×K | 298.00 | NIST |
Cp,liquid | 146.90 | J/mol×K | 298.00 | NIST |
Cp,liquid | 147.16 | J/mol×K | 298.15 | NIST |
Cp,liquid | 157.90 | J/mol×K | 298.15 | NIST |
Cp,liquid | 146.50 | J/mol×K | 298.15 | NIST |
ΔfusH | [0.82; 10.88] | kJ/mol | [210.00; 250.81] | ![]() |
ΔfusH | 0.82 | kJ/mol | 210.00 | NIST |
ΔfusH | 10.88 | kJ/mol | 250.80 | NIST |
ΔfusH | 10.88 | kJ/mol | 250.80 | NIST |
ΔfusH | 10.88 | kJ/mol | 250.81 | NIST |
ΔvapH | [34.68; 38.90] | kJ/mol | [340.00; 394.20] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 35 36 37 38 39 340 360 380 | ||||
ΔvapH | 38.90 | kJ/mol | 340.00 | NIST |
ΔvapH | 38.40 | kJ/mol | 350.00 | NIST |
ΔvapH | 38.70 | kJ/mol | 351.50 | NIST |
ΔvapH | 37.60 | kJ/mol | 353.00 | NIST |
ΔvapH | 34.68 | kJ/mol | 394.10 | NIST |
ΔvapH | 34.73 | kJ/mol | 394.20 | KDB |
Pvap | [1.02; 8.29] | kPa | [283.15; 323.15] | ![]() |
T(K) Vapor pressure (kPa) 2 4 6 8 290 300 310 320 | ||||
Pvap | 1.02 | kPa | 283.15 | Isother... |
Pvap | 1.02 | kPa | 283.15 | Total v... |
Pvap | 1.02 | kPa | 283.15 | Total v... |
Pvap | 1.40 | kPa | 288.15 | Total v... |
Pvap | 1.40 | kPa | 288.15 | Total v... |
Pvap | 1.40 | kPa | 288.15 | Isother... |
Pvap | 1.86 | kPa | 293.15 | Total v... |
Pvap | 1.86 | kPa | 293.15 | Total v... |
Pvap | 1.86 | kPa | 293.15 | Isother... |
Pvap | 2.46 | kPa | 298.15 | Isother... |
Pvap | 2.46 | kPa | 298.15 | Total v... |
Pvap | 2.46 | kPa | 298.15 | Total v... |
Pvap | 3.21 | kPa | 303.15 | Total v... |
Pvap | 3.21 | kPa | 303.15 | Isother... |
Pvap | 3.21 | kPa | 303.15 | Total v... |
Pvap | 4.12 | kPa | 308.15 | Total v... |
Pvap | 4.12 | kPa | 308.15 | Isother... |
Pvap | 4.12 | kPa | 308.15 | Total v... |
Pvap | 5.25 | kPa | 313.15 | Total v... |
Pvap | 5.25 | kPa | 313.15 | Total v... |
Pvap | 5.25 | kPa | 313.15 | Isother... |
Pvap | 6.62 | kPa | 318.15 | Isother... |
Pvap | 6.62 | kPa | 318.15 | Total v... |
Pvap | 6.62 | kPa | 318.15 | Total v... |
Pvap | 8.29 | kPa | 323.15 | Total v... |
Pvap | 8.29 | kPa | 323.15 | Total v... |
Pvap | 8.29 | kPa | 323.15 | Isother... |
n0 | [1.49780; 1.50580] | [293.15; 308.15] | ![]() |
|
T(K) Refractive Index 1.5 1.5 1.5 1.5 1.51 295 300 305 | ||||
n0 | 1.50500 | 293.15 | Activit... | |
n0 | 1.50580 | 293.15 | Excess ... | |
n0 | 1.50500 | 293.15 | Bubble ... | |
n0 | 1.50580 | 293.15 | Vapor-L... | |
n0 | 1.50500 | 298.15 | Bubble ... | |
n0 | 1.50320 | 298.15 | Bubble-... | |
n0 | 1.50500 | 298.15 | Bubble ... | |
n0 | 1.50360 | 298.15 | Density... | |
n0 | 1.50360 | 298.15 | Density... | |
n0 | 1.50050 | 303.15 | Density... | |
n0 | 1.50100 | 303.15 | Density... | |
n0 | 1.49780 | 308.15 | Density... | |
n0 | 1.49800 | 308.15 | Density... | |
ρl | [1590.60; 1622.39] | kg/m3 | [293.00; 313.15] | ![]() |
T(K) Liquid Density (kg/m3) 1590 1595 1600 1605 1610 1615 1620 1625 295 300 305 310 | ||||
ρl | 1620.00 | kg/m3 | 293.00 | KDB |
ρl | 1622.39 | kg/m3 | 293.15 | Thermop... |
ρl | 1614.49 | kg/m3 | 298.15 | Excess ... |
ρl | 1614.80 | kg/m3 | 298.15 | Excess ... |
ρl | 1607.20 | kg/m3 | 303.15 | Excess ... |
ρl | 1597.90 | kg/m3 | 308.15 | Excess ... |
ρl | 1590.60 | kg/m3 | 313.15 | Excess ... |
ΔfusS | [3.90; 43.38] | J/mol×K | [210.00; 250.81] | ![]() |
ΔfusS | 3.90 | J/mol×K | 210.00 | NIST |
ΔfusS | 43.38 | J/mol×K | 250.80 | NIST |
ΔfusS | 43.38 | J/mol×K | 250.81 | NIST |
csound,fluid | [1038.97; 1054.03] | m/s | [293.15; 298.15] | ![]() |
csound,fluid | 1054.03 | m/s | 293.15 | Densiti... |
csound,fluid | 1038.97 | m/s | 298.15 | Densiti... |
γ | 0.03 | N/m | 293.20 | KDB |
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
308.15 | 101.00 | 0.0007 |
Reference |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 203.96] | kPa | [286.48; 421.37] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.42797e+01 | |||
Coefficient B | -3.36251e+03 | |||
Coefficient C | -4.61640e+01 | |||
Temperature range, min. | 286.48 | |||
Temperature range, max. | 421.37 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
Pvap | 1.33 | kPa | 286.48 | Calculated Property |
Pvap | 3.03 | kPa | 301.47 | Calculated Property |
Pvap | 6.29 | kPa | 316.46 | Calculated Property |
Pvap | 12.10 | kPa | 331.44 | Calculated Property |
Pvap | 21.79 | kPa | 346.43 | Calculated Property |
Pvap | 37.10 | kPa | 361.42 | Calculated Property |
Pvap | 60.21 | kPa | 376.41 | Calculated Property |
Pvap | 93.67 | kPa | 391.39 | Calculated Property |
Pvap | 140.48 | kPa | 406.38 | Calculated Property |
Pvap | 203.96 | kPa | 421.37 | Calculated Property |
Pvap | [0.11; 4603.17] | kPa | [250.80; 620.00] |
KDB Vap...
![]() |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 6.04740e+01 | |||
Coefficient B | -6.53097e+03 | |||
Coefficient C | -6.66587e+00 | |||
Coefficient D | 3.52238e-06 | |||
Temperature range, min. | 250.80 | |||
Temperature range, max. | 620.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 300 400 500 600 | ||||
Pvap | 0.11 | kPa | 250.80 | Calculated Property |
Pvap | 1.75 | kPa | 291.82 | Calculated Property |
Pvap | 12.55 | kPa | 332.84 | Calculated Property |
Pvap | 55.13 | kPa | 373.87 | Calculated Property |
Pvap | 173.62 | kPa | 414.89 | Calculated Property |
Pvap | 432.94 | kPa | 455.91 | Calculated Property |
Pvap | 912.80 | kPa | 496.93 | Calculated Property |
Pvap | 1701.91 | kPa | 537.96 | Calculated Property |
Pvap | 2896.38 | kPa | 578.98 | Calculated Property |
Pvap | 4603.17 | kPa | 620.00 | Calculated Property |
Find more compounds similar to Tetrachloroethylene.
Find more mixtures with Tetrachloroethylene.
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.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.