Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -3366.70 ± 0.50 | kJ/mol | NIST |
η | 0.0056272 | Pa×s | Thermod... |
ΔfG° | 205.09 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -4.84 | kJ/mol | Joback Calculated Property |
ΔfH°liquid | [-287.00; -65.20] | kJ/mol |
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ΔfH°liquid | -65.20 ± 0.50 | kJ/mol | NIST |
ΔfH°liquid | -287.00 | kJ/mol | NIST |
ΔfusH° | 21.61 | kJ/mol | Joback Calculated Property |
ΔvapH° | 63.40 ± 0.70 | kJ/mol | NIST |
log10WS | 0.45 | Crippen Calculated Property | |
logPoct/wat | -1.507 | Crippen Calculated Property | |
McVol | 97.160 | ml/mol | McGowan Calculated Property |
Pc | 3050.00 ± 250.00 | kPa | NIST |
ρc | 286.80 ± 15.47 | kg/m3 | NIST |
Inp | [1025.00; 1030.00] |
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|
Inp | 1030.00 | NIST | |
Inp | 1028.00 | NIST | |
Inp | 1025.00 | NIST | |
Inp | 1030.00 | NIST | |
I | [1727.00; 1763.00] |
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|
I | 1729.00 | NIST | |
I | Outlier 1763.00 | NIST | |
I | 1748.00 | NIST | |
I | 1731.00 | NIST | |
I | 1727.00 | NIST | |
I | 1734.00 | NIST | |
I | 1729.00 | NIST | |
I | 1734.00 | NIST | |
Tboil | [477.20; 480.15] | K |
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Tboil | 477.20 | K | NIST |
Tboil | 480.15 ± 2.00 | K | NIST |
Tboil | 480.05 | K | NIST |
Tc | 677.00 ± 6.00 | K | NIST |
Tfus | 234.15 | K | NIST |
Vc | 0.352 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [224.95; 278.83] | J/mol×K | [486.15; 685.98] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 220 230 240 250 260 270 280 500 550 600 650 | ||||
Cp,gas | 224.95 | J/mol×K | 486.15 | Joback Calculated Property |
Cp,gas | 235.11 | J/mol×K | 519.45 | Joback Calculated Property |
Cp,gas | 244.78 | J/mol×K | 552.76 | Joback Calculated Property |
Cp,gas | 253.97 | J/mol×K | 586.06 | Joback Calculated Property |
Cp,gas | 262.70 | J/mol×K | 619.37 | Joback Calculated Property |
Cp,gas | 270.98 | J/mol×K | 652.67 | Joback Calculated Property |
Cp,gas | 278.83 | J/mol×K | 685.98 | Joback Calculated Property |
Cp,liquid | [254.00; 274.00] | J/mol×K | [303.15; 353.15] | ![]() |
T(K) Liquid phase heat capacity (J/mol×K) 255 260 265 270 275 320 340 | ||||
Cp,liquid | 269.50 | J/mol×K | 303.15 | Molar h... |
Cp,liquid | 269.90 | J/mol×K | 308.15 | Molar h... |
Cp,liquid | 254.00 | J/mol×K | 313.00 | NIST |
Cp,liquid | 270.20 | J/mol×K | 313.15 | Molar h... |
Cp,liquid | 270.80 | J/mol×K | 318.15 | Molar h... |
Cp,liquid | 271.20 | J/mol×K | 323.15 | Molar h... |
Cp,liquid | 272.00 | J/mol×K | 328.15 | Molar h... |
Cp,liquid | 272.70 | J/mol×K | 333.15 | Molar h... |
Cp,liquid | 273.20 | J/mol×K | 338.15 | Molar h... |
Cp,liquid | 273.60 | J/mol×K | 343.15 | Molar h... |
Cp,liquid | 273.80 | J/mol×K | 348.15 | Molar h... |
Cp,liquid | 274.00 | J/mol×K | 353.15 | Molar h... |
ΔvapH | 54.80 | kJ/mol | 406.00 | NIST |
ρl | [891.90; 951.16] | kg/m3 | [293.15; 363.15] | ![]() |
T(K) Liquid Density (kg/m3) 890 900 910 920 930 940 950 300 320 340 360 | ||||
ρl | 951.16 | kg/m3 | 293.15 | Volumet... |
ρl | 951.00 | kg/m3 | 293.15 | Density... |
ρl | 945.80 | kg/m3 | 298.15 | Thermod... |
ρl | 942.30 | kg/m3 | 303.15 | Density... |
ρl | 942.19 | kg/m3 | 303.15 | Volumet... |
ρl | 942.10 | kg/m3 | 303.15 | Thermod... |
ρl | 942.10 | kg/m3 | 303.15 | Mutual ... |
ρl | 937.90 | kg/m3 | 308.15 | Mutual ... |
ρl | 937.80 | kg/m3 | 308.15 | Thermod... |
ρl | 933.80 | kg/m3 | 313.15 | Mutual ... |
ρl | 933.93 | kg/m3 | 313.15 | Volumet... |
ρl | 933.80 | kg/m3 | 313.15 | Density... |
ρl | 929.60 | kg/m3 | 318.15 | Mutual ... |
ρl | 925.42 | kg/m3 | 323.15 | Volumet... |
ρl | 925.50 | kg/m3 | 323.15 | Density... |
ρl | 925.50 | kg/m3 | 323.15 | Mutual ... |
ρl | 917.00 | kg/m3 | 333.15 | Density... |
ρl | 908.90 | kg/m3 | 343.15 | Density... |
ρl | 900.40 | kg/m3 | 353.15 | Density... |
ρl | 891.90 | kg/m3 | 363.15 | Density... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [5.21e-05; 3989.70] | kPa | [234.15; 676.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 8.10727e+01 | |||
Coefficient B | -9.24563e+03 | |||
Coefficient C | -9.48992e+00 | |||
Coefficient D | 5.98254e-06 | |||
Temperature range, min. | 234.15 | |||
Temperature range, max. | 676.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 300 400 500 600 | ||||
Pvap | 5.21e-05 | kPa | 234.15 | Calculated Property |
Pvap | 9.35e-03 | kPa | 283.24 | Calculated Property |
Pvap | 0.31 | kPa | 332.34 | Calculated Property |
Pvap | 3.66 | kPa | 381.43 | Calculated Property |
Pvap | 23.34 | kPa | 430.53 | Calculated Property |
Pvap | 98.57 | kPa | 479.62 | Calculated Property |
Pvap | 314.84 | kPa | 528.72 | Calculated Property |
Pvap | 828.98 | kPa | 577.81 | Calculated Property |
Pvap | 1906.90 | kPa | 626.91 | Calculated Property |
Pvap | 3989.70 | kPa | 676.00 | Calculated Property |
Find more compounds similar to 1,2-Ethanediamine, N-(2-aminoethyl)-.
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