Property | Value | Unit | Source |
---|---|---|---|
PAff | 1012.80 | kJ/mol | NIST |
BasG | 970.60 | kJ/mol | NIST |
ΔfG° | 221.20 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -32.11 | kJ/mol | Joback Calculated Property |
ΔfusH° | 17.34 | kJ/mol | Joback Calculated Property |
ΔvapH° | 42.20 | kJ/mol | NIST |
IE | [7.57; 7.61] | eV |
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IE | 7.59 ± 0.04 | eV | NIST |
IE | 7.57 ± 0.03 | eV | NIST |
IE | 7.61 ± 0.05 | eV | NIST |
log10WS | 0.53 | Crippen Calculated Property | |
logPoct/wat | 0.110 | Crippen Calculated Property | |
McVol | 115.360 | ml/mol | McGowan Calculated Property |
Pc | 3093.29 | kPa | Joback Calculated Property |
Inp | [1052.00; 1095.00] |
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|
Inp | 1052.00 | NIST | |
Inp | 1065.00 | NIST | |
Inp | 1095.00 | NIST | |
I | [979.00; 1050.00] |
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|
I | 999.00 | NIST | |
I | 1050.00 | NIST | |
I | 1028.00 | NIST | |
I | 988.00 | NIST | |
I | 1015.00 | NIST | |
I | 979.00 | NIST | |
Tboil | 394.20 | K | NIST |
Tc | 523.14 | K | Joback Calculated Property |
Tfus | 214.50 ± 0.60 | K | NIST |
Vc | 0.407 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [210.52; 280.79] | J/mol×K | [361.56; 523.14] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 210 220 230 240 250 260 270 280 400 450 500 | ||||
Cp,gas | 210.52 | J/mol×K | 361.56 | Joback Calculated Property |
Cp,gas | 223.52 | J/mol×K | 388.49 | Joback Calculated Property |
Cp,gas | 235.99 | J/mol×K | 415.42 | Joback Calculated Property |
Cp,gas | 247.93 | J/mol×K | 442.35 | Joback Calculated Property |
Cp,gas | 259.37 | J/mol×K | 469.28 | Joback Calculated Property |
Cp,gas | 270.31 | J/mol×K | 496.21 | Joback Calculated Property |
Cp,gas | 280.79 | J/mol×K | 523.14 | Joback Calculated Property |
ΔvapH | 39.80 | kJ/mol | 330.00 | NIST |
Pvap | [1.77; 40.04] | kPa | [294.75; 364.97] | ![]() |
T(K) Vapor pressure (kPa) 0 5 10 15 20 25 30 35 40 300 320 340 360 | ||||
Pvap | 1.77 | kPa | 294.75 | Experim... |
Pvap | 3.06 | kPa | 304.74 | Experim... |
Pvap | 5.05 | kPa | 314.76 | Experim... |
Pvap | 8.12 | kPa | 324.95 | Experim... |
Pvap | 12.53 | kPa | 334.99 | Experim... |
Pvap | 19.34 | kPa | 344.96 | Experim... |
Pvap | 28.12 | kPa | 354.98 | Experim... |
Pvap | 40.04 | kPa | 364.97 | Experim... |
ρl | [750.30; 767.30] | kg/m3 | [303.15; 323.15] | ![]() |
T(K) Liquid Density (kg/m3) 750 755 760 765 305 310 315 320 | ||||
ρl | 767.30 | kg/m3 | 303.15 | Mutual ... |
ρl | 762.90 | kg/m3 | 308.15 | Mutual ... |
ρl | 759.10 | kg/m3 | 313.15 | Mutual ... |
ρl | 754.70 | kg/m3 | 318.15 | Mutual ... |
ρl | 750.30 | kg/m3 | 323.15 | Mutual ... |
λ | [0.14; 0.15] | W/m×K | [273.15; 333.15] | ![]() |
λ | 0.15 | W/m×K | 273.15 | Liquid ... |
λ | 0.15 | W/m×K | 293.15 | Liquid ... |
λ | 0.14 | W/m×K | 313.15 | Liquid ... |
λ | 0.14 | W/m×K | 333.15 | Liquid ... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.67] | kPa | [297.32; 417.25] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.56417e+01 | |||
Coefficient B | -3.78626e+03 | |||
Coefficient C | -5.07240e+01 | |||
Temperature range, min. | 297.32 | |||
Temperature range, max. | 417.25 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
Pvap | 1.33 | kPa | 297.32 | Calculated Property |
Pvap | 2.93 | kPa | 310.65 | Calculated Property |
Pvap | 5.96 | kPa | 323.97 | Calculated Property |
Pvap | 11.35 | kPa | 337.30 | Calculated Property |
Pvap | 20.42 | kPa | 350.62 | Calculated Property |
Pvap | 34.94 | kPa | 363.95 | Calculated Property |
Pvap | 57.22 | kPa | 377.27 | Calculated Property |
Pvap | 90.16 | kPa | 390.60 | Calculated Property |
Pvap | 137.25 | kPa | 403.92 | Calculated Property |
Pvap | 202.67 | kPa | 417.25 | Calculated Property |
Find more compounds similar to 1,2-Ethanediamine, N,N,N',N'-tetramethyl-.
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