Property | Value | Unit | Source |
---|---|---|---|
ω | 0.4110 | KDB | |
PAff | 941.10 | kJ/mol | NIST |
BasG | 909.20 | kJ/mol | NIST |
ΔcH°liquid | [-4767.80; -4754.30] | kJ/mol |
![]() |
ΔcH°liquid | -4767.80 ± 3.20 | kJ/mol | NIST |
ΔcH°liquid | -4754.30 | kJ/mol | NIST |
μ | 1.60 | debye | KDB |
ΔfG° | 231.40 | kJ/mol | KDB |
ΔfH°gas | [84.10; 100.50] | kJ/mol |
![]() |
ΔfH°gas | 84.15 | kJ/mol | KDB |
ΔfH°gas | 100.50 ± 3.40 | kJ/mol | NIST |
ΔfH°gas | 84.10 | kJ/mol | NIST |
ΔfH°liquid | [34.00; 47.70] | kJ/mol |
![]() |
ΔfH°liquid | 47.70 ± 3.40 | kJ/mol | NIST |
ΔfH°liquid | 34.00 | kJ/mol | NIST |
ΔfusH° | 13.54 | kJ/mol | Joback Calculated Property |
ΔvapH° | 37.72 | kJ/mol | Joback Calculated Property |
IE | [7.10; 7.92] | eV |
![]() |
IE | 7.12 ± 0.02 | eV | NIST |
IE | 7.15 | eV | NIST |
IE | 7.78 | eV | NIST |
IE | 7.10 ± 0.02 | eV | NIST |
IE | 7.42 | eV | NIST |
IE | 7.11 | eV | NIST |
IE | 7.13 ± 0.04 | eV | NIST |
IE | 7.20 | eV | NIST |
IE | 7.10 ± 0.05 | eV | NIST |
IE | 7.31 | eV | NIST |
IE | 7.20 | eV | NIST |
IE | 7.14 ± 0.03 | eV | NIST |
IE | 7.35 | eV | NIST |
IE | Outlier 7.92 | eV | NIST |
IE | 7.60 | eV | NIST |
IE | 7.37 | eV | NIST |
IE | 7.51 | eV | NIST |
log10WS | [-1.92; -1.92] |
![]() |
|
log10WS | -1.92 | Aq. Sol... | |
log10WS | -1.92 | Estimat... | |
logPoct/wat | 1.753 | Crippen Calculated Property | |
McVol | 109.800 | ml/mol | McGowan Calculated Property |
NFPA Fire | 2 | KDB | |
NFPA Health | 3 | KDB | |
Pc | [3576.77; 3657.83] | kPa |
![]() |
Pc | 3630.00 | kPa | KDB |
Pc | 3610.00 ± 91.19 | kPa | NIST |
Pc | 3650.00 ± 91.19 | kPa | NIST |
Pc | 3597.04 ± 151.99 | kPa | NIST |
Pc | 3627.44 ± 151.99 | kPa | NIST |
Pc | 3657.83 ± 151.99 | kPa | NIST |
Pc | 3637.57 ± 151.99 | kPa | NIST |
Pc | 3576.77 ± 151.99 | kPa | NIST |
Inp | [1061.00; 1104.00] |
![]() |
|
Inp | 1083.90 | NIST | |
Inp | 1094.50 | NIST | |
Inp | 1074.00 | NIST | |
Inp | 1087.00 | NIST | |
Inp | 1087.00 | NIST | |
Inp | 1100.00 | NIST | |
Inp | 1103.00 | NIST | |
Inp | 1065.40 | NIST | |
Inp | 1062.37 | NIST | |
Inp | 1062.07 | NIST | |
Inp | 1063.00 | NIST | |
Inp | 1062.71 | NIST | |
Inp | 1100.00 | NIST | |
Inp | 1104.00 | NIST | |
Inp | 1086.00 | NIST | |
Inp | 1073.00 | NIST | |
Inp | 1062.00 | NIST | |
Inp | 1067.00 | NIST | |
Inp | 1086.10 | NIST | |
Inp | 1073.00 | NIST | |
Inp | 1061.00 | NIST | |
Inp | 1068.00 | NIST | |
Inp | 1080.00 | NIST | |
Inp | 1065.40 | NIST | |
Inp | 1100.00 | NIST | |
Inp | 1083.90 | NIST | |
Inp | 1068.00 | NIST | |
Inp | 1104.00 | NIST | |
I | [1569.90; 1605.00] |
![]() |
|
I | 1569.90 | NIST | |
I | 1602.00 | NIST | |
I | 1599.00 | NIST | |
I | 1603.00 | NIST | |
I | 1605.00 | NIST | |
I | 1604.80 | NIST | |
I | 1603.40 | NIST | |
I | 1574.00 | NIST | |
I | 1569.90 | NIST | |
I | 1604.80 | NIST | |
I | 1574.00 | NIST | |
Tboil | 467.30 | K | KDB |
Tc | 687.00 | K | KDB |
Tfus | [272.00; 275.75] | K |
![]() |
Tfus | 275.60 | K | KDB |
Tfus | 275.53 | K | Aq. Sol... |
Tfus | 275.65 ± 0.30 | K | NIST |
Tfus | Outlier 272.00 ± 1.00 | K | NIST |
Tfus | 275.60 ± 0.30 | K | NIST |
Tfus | 275.36 ± 0.25 | K | NIST |
Tfus | 275.75 ± 0.20 | K | NIST |
Tfus | 275.35 ± 0.40 | K | NIST |
Tfus | 274.60 ± 0.14 | K | NIST |
Tfus | 274.15 ± 0.30 | K | NIST |
Vc | 0.394 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [204.33; 276.52] | J/mol×K | [421.56; 628.44] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 200 220 240 260 280 450 500 550 600 | ||||
Cp,gas | 204.33 | J/mol×K | 421.56 | Joback Calculated Property |
Cp,gas | 218.35 | J/mol×K | 456.04 | Joback Calculated Property |
Cp,gas | 231.52 | J/mol×K | 490.52 | Joback Calculated Property |
Cp,gas | 243.89 | J/mol×K | 525.00 | Joback Calculated Property |
Cp,gas | 255.49 | J/mol×K | 559.48 | Joback Calculated Property |
Cp,gas | 266.35 | J/mol×K | 593.96 | Joback Calculated Property |
Cp,gas | 276.52 | J/mol×K | 628.44 | Joback Calculated Property |
Cp,liquid | [209.60; 214.60] | J/mol×K | [283.00; 302.40] | ![]() |
T(K) Liquid phase heat capacity (J/mol×K) 210 211 212 213 214 215 285 290 295 300 | ||||
Cp,liquid | 212.10 | J/mol×K | 283.00 | NIST |
Cp,liquid | 209.60 | J/mol×K | 289.00 | NIST |
Cp,liquid | 212.10 | J/mol×K | 298.00 | NIST |
Cp,liquid | 214.60 | J/mol×K | 302.30 | NIST |
Cp,liquid | 214.60 | J/mol×K | 302.40 | NIST |
η | [0.0008259; 0.0016960] | Pa×s | [283.15; 343.15] | ![]() |
T(K) Dynamic viscosity (Pa×s) 8.00e-4 1.00e-3 1.20e-3 1.40e-3 1.60e-3 300 320 340 | ||||
η | 0.0016960 | Pa×s | 283.15 | Densiti... |
η | 0.0014390 | Pa×s | 293.15 | Densiti... |
η | 0.0011743 | Pa×s | 303.15 | Densiti... |
η | 0.0011700 | Pa×s | 303.15 | Densiti... |
η | 0.0009823 | Pa×s | 313.15 | Densiti... |
η | 0.0009810 | Pa×s | 313.15 | Densiti... |
η | 0.0008259 | Pa×s | 323.15 | Densiti... |
η | 0.0009280 | Pa×s | 323.15 | Densiti... |
η | 0.0009110 | Pa×s | 333.15 | Densiti... |
η | 0.0008410 | Pa×s | 343.15 | Densiti... |
ΔfusH | [11.56; 11.56] | kJ/mol | [275.60; 275.60] | ![]() |
ΔfusH | 11.56 | kJ/mol | 275.60 | NIST |
ΔfusH | 11.56 | kJ/mol | 275.60 | NIST |
ΔvapH | [44.35; 53.70] | kJ/mol | [303.50; 465.70] | ![]() |
ΔvapH | 53.70 ± 0.50 | kJ/mol | 303.50 | NIST |
ΔvapH | 47.60 | kJ/mol | 384.50 | NIST |
ΔvapH | 49.20 | kJ/mol | 390.50 | NIST |
ΔvapH | 44.35 | kJ/mol | 465.70 | NIST |
Pvap | [5.16; 8.04] | kPa | [373.70; 384.96] | ![]() |
Pvap | 5.16 | kPa | 373.70 | Vapor-L... |
Pvap | 8.04 | kPa | 384.96 | Vapor-L... |
ρl | [923.50; 960.60] | kg/m3 | [288.15; 333.15] | ![]() |
T(K) Liquid Density (kg/m3) 920 930 940 950 960 300 320 | ||||
ρl | 960.60 | kg/m3 | 288.15 | Excess ... |
ρl | 956.00 | kg/m3 | 293.00 | KDB |
ρl | 956.50 | kg/m3 | 293.15 | Excess ... |
ρl | 952.30 | kg/m3 | 298.15 | Excess ... |
ρl | 952.05 | kg/m3 | 298.15 | Cloud P... |
ρl | 947.70 | kg/m3 | 303.15 | Volumet... |
ρl | 948.18 | kg/m3 | 303.15 | Study o... |
ρl | 948.20 | kg/m3 | 303.15 | Excess ... |
ρl | 944.10 | kg/m3 | 308.15 | Excess ... |
ρl | 943.50 | kg/m3 | 308.15 | Volumet... |
ρl | 943.55 | kg/m3 | 308.15 | Study o... |
ρl | 939.40 | kg/m3 | 313.15 | Volumet... |
ρl | 940.00 | kg/m3 | 313.15 | Excess ... |
ρl | 939.78 | kg/m3 | 313.15 | Study o... |
ρl | 935.30 | kg/m3 | 318.15 | Study o... |
ρl | 935.90 | kg/m3 | 318.15 | Excess ... |
ρl | 931.80 | kg/m3 | 323.15 | Excess ... |
ρl | 931.45 | kg/m3 | 323.15 | Study o... |
ρl | 927.70 | kg/m3 | 328.15 | Excess ... |
ρl | 923.50 | kg/m3 | 333.15 | Excess ... |
csound,fluid | [1393.00; 1468.00] | m/s | [303.15; 323.15] | ![]() |
csound,fluid | 1468.00 | m/s | 303.15 | Thermod... |
csound,fluid | 1431.00 | m/s | 313.15 | Thermod... |
csound,fluid | 1393.00 | m/s | 323.15 | Thermod... |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 350.20 | K | 1.70 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [342.92; 495.81] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.50960e+01 | |||
Coefficient B | -4.40969e+03 | |||
Coefficient C | -4.51330e+01 | |||
Temperature range, min. | 342.92 | |||
Temperature range, max. | 495.81 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
Pvap | 1.33 | kPa | 342.92 | Calculated Property |
Pvap | 2.97 | kPa | 359.91 | Calculated Property |
Pvap | 6.08 | kPa | 376.90 | Calculated Property |
Pvap | 11.61 | kPa | 393.88 | Calculated Property |
Pvap | 20.88 | kPa | 410.87 | Calculated Property |
Pvap | 35.67 | kPa | 427.86 | Calculated Property |
Pvap | 58.20 | kPa | 444.85 | Calculated Property |
Pvap | 91.25 | kPa | 461.83 | Calculated Property |
Pvap | 138.12 | kPa | 478.82 | Calculated Property |
Pvap | 202.63 | kPa | 495.81 | Calculated Property |
Pvap | [0.02; 3612.43] | kPa | [275.60; 687.15] |
KDB Vap...
![]() |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 4.20032e+01 | |||
Coefficient B | -7.05985e+03 | |||
Coefficient C | -3.63909e+00 | |||
Coefficient D | 4.98882e-07 | |||
Temperature range, min. | 275.60 | |||
Temperature range, max. | 687.15 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 300 400 500 600 | ||||
Pvap | 0.02 | kPa | 275.60 | Calculated Property |
Pvap | 0.40 | kPa | 321.33 | Calculated Property |
Pvap | 3.84 | kPa | 367.06 | Calculated Property |
Pvap | 21.48 | kPa | 412.78 | Calculated Property |
Pvap | 82.31 | kPa | 458.51 | Calculated Property |
Pvap | 240.53 | kPa | 504.24 | Calculated Property |
Pvap | 575.43 | kPa | 549.97 | Calculated Property |
Pvap | 1183.22 | kPa | 595.69 | Calculated Property |
Pvap | 2164.57 | kPa | 641.42 | Calculated Property |
Pvap | 3612.43 | kPa | 687.15 | Calculated Property |
Find more compounds similar to Benzenamine, N,N-dimethyl-.
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.