Property | Value | Unit | Source |
---|---|---|---|
PAff | 851.30 | kJ/mol | NIST |
BasG | 820.30 | kJ/mol | NIST |
EA | 0.02 | eV | NIST |
ΔfG° | -44.17 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -116.72 | kJ/mol | Joback Calculated Property |
ΔfusH° | 8.32 | kJ/mol | Joback Calculated Property |
ΔvapH° | [54.40; 56.20] | kJ/mol |
![]() |
ΔvapH° | 56.19 | kJ/mol | NIST |
ΔvapH° | 54.40 ± 1.30 | kJ/mol | NIST |
ΔvapH° | 56.20 | kJ/mol | NIST |
IE | [9.79; 10.00] | eV |
![]() |
IE | 9.83 ± 0.04 | eV | NIST |
IE | 9.86 | eV | NIST |
IE | 10.00 ± 0.05 | eV | NIST |
IE | 9.79 | eV | NIST |
log10WS | 0.38 | Crippen Calculated Property | |
logPoct/wat | -0.638 | Crippen Calculated Property | |
McVol | 50.590 | ml/mol | McGowan Calculated Property |
Pc | 5713.21 | kPa | Joback Calculated Property |
Inp | [722.00; 793.00] |
![]() |
|
Inp | 793.00 | NIST | |
Inp | 722.00 | NIST | |
Inp | 793.00 | NIST | |
I | [1615.00; 1615.00] |
![]() |
|
I | 1615.00 | NIST | |
I | 1615.00 | NIST | |
Tboil | [455.70; 472.25] | K |
![]() |
Tboil | 472.25 | K | Separat... |
Tboil | 471.20 | K | Separat... |
Tboil | 455.70 | K | NIST |
Tc | 524.37 | K | Joback Calculated Property |
Tfus | 206.96 | K | Joback Calculated Property |
Vc | 0.200 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [81.25; 107.70] | J/mol×K | [343.99; 524.37] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 80 85 90 95 100 105 110 350 400 450 500 | ||||
Cp,gas | 81.25 | J/mol×K | 343.99 | Joback Calculated Property |
Cp,gas | 86.11 | J/mol×K | 374.05 | Joback Calculated Property |
Cp,gas | 90.79 | J/mol×K | 404.12 | Joback Calculated Property |
Cp,gas | 95.28 | J/mol×K | 434.18 | Joback Calculated Property |
Cp,gas | 99.59 | J/mol×K | 464.24 | Joback Calculated Property |
Cp,gas | 103.73 | J/mol×K | 494.31 | Joback Calculated Property |
Cp,gas | 107.70 | J/mol×K | 524.37 | Joback Calculated Property |
Cp,liquid | [122.00; 126.63] | J/mol×K | [298.15; 308.00] | ![]() |
T(K) Liquid phase heat capacity (J/mol×K) 122 123 124 125 126 127 300 305 | ||||
Cp,liquid | 125.20 | J/mol×K | 298.15 | NIST |
Cp,liquid | 122.00 | J/mol×K | 298.15 | NIST |
Cp,liquid | 123.80 | J/mol×K | 298.15 | NIST |
Cp,liquid | 126.10 | J/mol×K | 298.15 | NIST |
Cp,liquid | 126.63 | J/mol×K | 308.00 | NIST |
ΔfusH | 10.44 | kJ/mol | 270.60 | NIST |
ΔvapH | [53.40; 54.50] | kJ/mol | [350.50; 420.50] | ![]() |
ΔvapH | 54.50 | kJ/mol | 350.50 | NIST |
ΔvapH | 53.80 | kJ/mol | 390.00 | NIST |
ΔvapH | 53.40 | kJ/mol | 420.50 | NIST |
Pvap | [0.37; 101.30] | kPa | [333.15; 471.20] | ![]() |
Pvap | 0.37 | kPa | 333.15 | Vapor l... |
Pvap | 0.67 | kPa | 343.15 | Vapor l... |
Pvap | 1.15 | kPa | 353.15 | Vapor l... |
Pvap | 101.30 | kPa | 471.20 | Separat... |
ρl | [785.32; 1007.94] | kg/m3 | [288.15; 323.15] | ![]() |
T(K) Liquid Density (kg/m3) 800 850 900 950 1000 290 300 310 320 | ||||
ρl | 1007.94 | kg/m3 | 288.15 | Solutio... |
ρl | 1003.35 | kg/m3 | 293.15 | Volumet... |
ρl | 1003.59 | kg/m3 | 293.15 | Volumet... |
ρl | 1003.35 | kg/m3 | 293.15 | Volumet... |
ρl | 998.91 | kg/m3 | 298.15 | Volumet... |
ρl | 999.25 | kg/m3 | 298.15 | Solutio... |
ρl | 998.91 | kg/m3 | 298.15 | Volumet... |
ρl | 999.00 | kg/m3 | 298.15 | Excess ... |
ρl | 999.00 | kg/m3 | 298.15 | Topolog... |
ρl | 999.36 | kg/m3 | 298.15 | PrhoT m... |
ρl | 999.12 | kg/m3 | 298.15 | Physico... |
ρl | 998.80 | kg/m3 | 298.15 | Excess ... |
ρl | 999.19 | kg/m3 | 298.15 | Volumet... |
ρl | 785.32 | kg/m3 | 298.15 | Binary ... |
ρl | 994.65 | kg/m3 | 303.15 | Excess ... |
ρl | 994.75 | kg/m3 | 303.15 | Volumet... |
ρl | 994.49 | kg/m3 | 303.15 | Volumet... |
ρl | 994.49 | kg/m3 | 303.15 | Volumet... |
ρl | 994.65 | kg/m3 | 303.15 | Topolog... |
ρl | 990.01 | kg/m3 | 308.15 | Volumet... |
ρl | 990.30 | kg/m3 | 308.15 | Excess ... |
ρl | 990.63 | kg/m3 | 308.15 | Solutio... |
ρl | 990.01 | kg/m3 | 308.15 | Volumet... |
ρl | 990.33 | kg/m3 | 308.15 | Volumet... |
ρl | 990.30 | kg/m3 | 308.15 | Topolog... |
ρl | 985.47 | kg/m3 | 313.15 | Volumet... |
ρl | 985.47 | kg/m3 | 313.15 | Volumet... |
ρl | 985.78 | kg/m3 | 313.15 | Volumet... |
ρl | 980.88 | kg/m3 | 318.15 | Volumet... |
ρl | 980.88 | kg/m3 | 318.15 | Volumet... |
ρl | 981.23 | kg/m3 | 318.15 | Volumet... |
ρl | 976.24 | kg/m3 | 323.15 | Volumet... |
ρl | 976.57 | kg/m3 | 323.15 | Volumet... |
ρl | 976.24 | kg/m3 | 323.15 | Volumet... |
csound,fluid | [1402.55; 1432.86] | m/s | [298.15; 308.15] | ![]() |
csound,fluid | 1431.91 | m/s | 298.15 | Isentro... |
csound,fluid | 1432.86 | m/s | 298.15 | Topolog... |
csound,fluid | 1417.66 | m/s | 303.15 | Topolog... |
csound,fluid | 1402.55 | m/s | 308.15 | Topolog... |
Fixed | Measured | |
---|---|---|
Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
100.00 | 298.15 | 997.61 |
Reference |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [354.33; 501.18] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.52412e+01 | |||
Coefficient B | -4.34038e+03 | |||
Coefficient C | -6.40690e+01 | |||
Temperature range, min. | 354.33 | |||
Temperature range, max. | 501.18 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
Pvap | 1.33 | kPa | 354.33 | Calculated Property |
Pvap | 2.96 | kPa | 370.65 | Calculated Property |
Pvap | 6.04 | kPa | 386.96 | Calculated Property |
Pvap | 11.54 | kPa | 403.28 | Calculated Property |
Pvap | 20.76 | kPa | 419.60 | Calculated Property |
Pvap | 35.47 | kPa | 435.91 | Calculated Property |
Pvap | 57.93 | kPa | 452.23 | Calculated Property |
Pvap | 90.95 | kPa | 468.55 | Calculated Property |
Pvap | 137.89 | kPa | 484.86 | Calculated Property |
Pvap | 202.65 | kPa | 501.18 | Calculated Property |
Pvap | [2.70e-03; 5478.19] | kPa | [269.35; 721.00] |
KDB Vap...
![]() |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 7.41690e+01 | |||
Coefficient B | -9.24638e+03 | |||
Coefficient C | -8.20817e+00 | |||
Coefficient D | 2.46022e-06 | |||
Temperature range, min. | 269.35 | |||
Temperature range, max. | 721.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 400 600 | ||||
Pvap | 2.70e-03 | kPa | 269.35 | Calculated Property |
Pvap | 0.16 | kPa | 319.53 | Calculated Property |
Pvap | 2.62 | kPa | 369.72 | Calculated Property |
Pvap | 20.18 | kPa | 419.90 | Calculated Property |
Pvap | 93.58 | kPa | 470.08 | Calculated Property |
Pvap | 306.69 | kPa | 520.27 | Calculated Property |
Pvap | 786.92 | kPa | 570.45 | Calculated Property |
Pvap | 1692.11 | kPa | 620.63 | Calculated Property |
Pvap | 3195.42 | kPa | 670.82 | Calculated Property |
Pvap | 5478.19 | kPa | 721.00 | Calculated Property |
Find more compounds similar to Formamide, N-methyl-.
Find more mixtures with Formamide, N-methyl-.
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.