Property | Value | Unit | Source |
---|---|---|---|
PAff | 924.80 | kJ/mol | NIST |
BasG | 892.90 | kJ/mol | NIST |
ΔcH°gas | -4714.90 | kJ/mol | NIST |
ΔcH°liquid | -4724.20 ± 4.20 | kJ/mol | NIST |
μ | 1.70 | debye | KDB |
ΔfG° | 218.28 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [23.10; 56.10] | kJ/mol |
![]() |
ΔfH°gas | 56.10 | kJ/mol | NIST |
ΔfH°gas | 23.10 | kJ/mol | NIST |
ΔfH°liquid | [-29.00; 4.00] | kJ/mol |
![]() |
ΔfH°liquid | 4.00 | kJ/mol | NIST |
ΔfH°liquid | -29.00 | kJ/mol | NIST |
ΔfusH° | 15.62 | kJ/mol | Joback Calculated Property |
ΔvapH° | [52.10; 58.30] | kJ/mol |
![]() |
ΔvapH° | 58.30 ± 0.60 | kJ/mol | NIST |
ΔvapH° | 52.30 | kJ/mol | NIST |
ΔvapH° | 52.10 | kJ/mol | NIST |
IE | [7.50; 7.67] | eV |
![]() |
IE | 7.56 | eV | NIST |
IE | 7.50 | eV | NIST |
IE | 7.67 ± 0.06 | eV | NIST |
log10WS | [-1.70; -1.70] |
![]() |
|
log10WS | -1.70 | Aq. Sol... | |
log10WS | -1.70 | Estimat... | |
logPoct/wat | 2.118 | Crippen Calculated Property | |
McVol | 109.800 | ml/mol | McGowan Calculated Property |
NFPA Fire | 2 | KDB | |
NFPA Health | 3 | KDB | |
Pc | 3708.97 | kPa | Joback Calculated Property |
Inp | [1100.00; 1128.00] |
![]() |
|
Inp | 1100.00 | NIST | |
Inp | 1125.00 | NIST | |
Inp | 1128.00 | NIST | |
Inp | 1111.50 | NIST | |
Inp | 1100.00 | NIST | |
I | [1738.00; 1761.00] |
![]() |
|
I | 1740.90 | NIST | |
I | 1748.00 | NIST | |
I | 1738.00 | NIST | |
I | 1750.00 | NIST | |
I | 1751.00 | NIST | |
I | 1761.00 | NIST | |
I | 1761.00 | NIST | |
Tboil | [476.20; 479.70] | K |
![]() |
Tboil | Outlier 476.20 | K | KDB |
Tboil | 477.90 | K | NIST |
Tboil | 478.65 ± 0.50 | K | NIST |
Tboil | 478.15 ± 0.60 | K | NIST |
Tboil | 478.65 ± 0.35 | K | NIST |
Tboil | 478.65 ± 0.30 | K | NIST |
Tboil | 479.20 ± 0.20 | K | NIST |
Tboil | 479.70 ± 1.00 | K | NIST |
Tboil | 478.65 ± 1.00 | K | NIST |
Tboil | 477.15 ± 5.00 | K | NIST |
Tc | 698.00 | K | KDB |
Tfus | [209.53; 209.65] | K |
![]() |
Tfus | 209.60 | K | KDB |
Tfus | 209.53 | K | Aq. Sol... |
Tfus | 209.65 ± 0.40 | K | NIST |
Vc | 0.410 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [218.08; 286.49] | J/mol×K | [459.29; 671.67] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 220 230 240 250 260 270 280 290 500 550 600 650 | ||||
Cp,gas | 218.08 | J/mol×K | 459.29 | Joback Calculated Property |
Cp,gas | 231.34 | J/mol×K | 494.69 | Joback Calculated Property |
Cp,gas | 243.81 | J/mol×K | 530.08 | Joback Calculated Property |
Cp,gas | 255.53 | J/mol×K | 565.48 | Joback Calculated Property |
Cp,gas | 266.53 | J/mol×K | 600.88 | Joback Calculated Property |
Cp,gas | 276.83 | J/mol×K | 636.28 | Joback Calculated Property |
Cp,gas | 286.49 | J/mol×K | 671.67 | Joback Calculated Property |
ΔvapH | 52.20 | kJ/mol | 394.00 | NIST |
ρl | [938.23; 963.00] | kg/m3 | [293.00; 318.15] | ![]() |
T(K) Liquid Density (kg/m3) 940 945 950 955 960 965 300 310 | ||||
ρl | 963.00 | kg/m3 | 293.00 | KDB |
ρl | 952.41 | kg/m3 | 303.15 | Compara... |
ρl | 947.69 | kg/m3 | 308.15 | Compara... |
ρl | 942.95 | kg/m3 | 313.15 | Compara... |
ρl | 938.23 | kg/m3 | 318.15 | Compara... |
csound,fluid | [1431.00; 1497.00] | m/s | [303.15; 323.15] | ![]() |
T(K) Speed of sound in fluid (m/s) 1430 1440 1450 1460 1470 1480 1490 1500 305 310 315 320 | ||||
csound,fluid | 1497.00 | m/s | 303.15 | Thermod... |
csound,fluid | 1497.00 | m/s | 303.15 | Thermod... |
csound,fluid | 1462.00 | m/s | 313.15 | Thermod... |
csound,fluid | 1462.00 | m/s | 313.15 | Thermod... |
csound,fluid | 1431.00 | m/s | 323.15 | Thermod... |
csound,fluid | 1431.00 | m/s | 323.15 | Thermod... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.67] | kPa | [355.92; 509.41] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.45550e+01 | |||
Coefficient B | -4.02911e+03 | |||
Coefficient C | -7.35200e+01 | |||
Temperature range, min. | 355.92 | |||
Temperature range, max. | 509.41 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
Pvap | 1.33 | kPa | 355.92 | Calculated Property |
Pvap | 3.00 | kPa | 372.97 | Calculated Property |
Pvap | 6.20 | kPa | 390.03 | Calculated Property |
Pvap | 11.89 | kPa | 407.08 | Calculated Property |
Pvap | 21.40 | kPa | 424.14 | Calculated Property |
Pvap | 36.47 | kPa | 441.19 | Calculated Property |
Pvap | 59.28 | kPa | 458.25 | Calculated Property |
Pvap | 92.47 | kPa | 475.30 | Calculated Property |
Pvap | 139.10 | kPa | 492.36 | Calculated Property |
Pvap | 202.67 | kPa | 509.41 | Calculated Property |
Pvap | [0.11; 109.37] | kPa | [311.15; 481.00] |
KDB Vap...
![]() |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 3.29647e+01 | |||
Coefficient B | -7.19113e+03 | |||
Coefficient C | -2.06370e+00 | |||
Coefficient D | -2.48303e-06 | |||
Temperature range, min. | 311.15 | |||
Temperature range, max. | 481.00 | |||
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 120 350 400 450 | ||||
Pvap | 0.11 | kPa | 311.15 | Calculated Property |
Pvap | 0.35 | kPa | 330.02 | Calculated Property |
Pvap | 0.97 | kPa | 348.89 | Calculated Property |
Pvap | 2.42 | kPa | 367.77 | Calculated Property |
Pvap | 5.47 | kPa | 386.64 | Calculated Property |
Pvap | 11.36 | kPa | 405.51 | Calculated Property |
Pvap | 21.89 | kPa | 424.38 | Calculated Property |
Pvap | 39.52 | kPa | 443.26 | Calculated Property |
Pvap | 67.42 | kPa | 462.13 | Calculated Property |
Pvap | 109.37 | kPa | 481.00 | Calculated Property |
Find more compounds similar to Benzenamine, N-ethyl-.
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.