- InChI
- InChI=1S/C4H9NO/c1-4(6)5(2)3/h1-3H3
- InChI Key
- FXHOOIRPVKKKFG-UHFFFAOYSA-N
- Formula
- C4H9NO
- SMILES
- CC(=O)N(C)C
- Molecular Weight1
- 87.12
- CAS
- 127-19-5
- Other Names
-
- Acetamide, N,N-dimethyl-
- Acetdimethylamide
- Acetic acid dimethylamide
- Acetyl dimethylamine
- CBC 510337
- CH3CON(CH3)2
- DMA
- DMAc
- Dimethylacetamide
- Dimethylamid kyseliny octove
- Dimethylamide acetate
- Hallucinogen
- N,N-Dimethylethanamide
- N,N-dimethylacetamide [DMA]
- NSC 3138
- SK 7176
- U-5954
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| PAff | 908.00 | kJ/mol | NIST |
| BasG | 877.00 | kJ/mol | NIST |
| ΔcH°liquid | -2582.00 ± 1.50 | kJ/mol | NIST |
| Cp,liquid | 175.49 | J/mol×K | Volumes... |
| ΔfG° | -35.34 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -170.94 | kJ/mol | Joback Calculated Property |
| ΔfH°liquid | [-300.10; -278.30] | kJ/mol |
|
| ΔfH°liquid | -300.10 | kJ/mol | NIST |
| ΔfH°liquid | -298.20 | kJ/mol | NIST |
| ΔfH°liquid | -278.30 ± 1.50 | kJ/mol | NIST |
| ΔfusH° | [10.20; 50.66] | kJ/mol |
|
| ΔfusH° | 10.20 | kJ/mol | Thermod... |
| ΔfusH° | 50.66 | kJ/mol | Enthalp... |
| ΔvapH° | [43.70; 54.10] | kJ/mol |
|
| ΔvapH° | 50.70 ± 0.70 | kJ/mol | NIST |
| ΔvapH° | 53.70 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 45.80 | kJ/mol | NIST |
| ΔvapH° | 50.20 | kJ/mol | NIST |
| ΔvapH° | 54.10 | kJ/mol | NIST |
| ΔvapH° | 46.00 ± 2.00 | kJ/mol | NIST |
| ΔvapH° | 43.70 | kJ/mol | NIST |
| IE | [8.81; 9.43] | eV |
|
| IE | 9.20 ± 0.05 | eV | NIST |
| IE | 8.81 | eV | NIST |
| IE | 8.81 ± 0.03 | eV | NIST |
| IE | 9.43 | eV | NIST |
| log10WS | [1.11; 1.11] |
|
|
| log10WS | 1.11 | Aq. Sol... | |
| log10WS | 1.11 | Estimat... | |
| logPoct/wat | 0.094 | Crippen Calculated Property | |
| McVol | 78.770 | ml/mol | McGowan Calculated Property |
| Pc | 4211.09 | kPa | Joback Calculated Property |
| Inp | [820.00; 883.00] |
|
|
| Inp | 820.00 | NIST | |
| Inp | 833.30 | NIST | |
| Inp | 833.00 | NIST | |
| Inp | Outlier 883.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 840.00 | NIST | |
| Inp | 833.30 | NIST | |
| I | [1384.00; 1437.00] |
|
|
| I | 1414.00 | NIST | |
| I | 1437.00 | NIST | |
| I | 1437.00 | NIST | |
| I | 1384.00 | NIST | |
| I | 1409.00 | NIST | |
| I | 1414.00 | NIST | |
| Tboil | [438.20; 439.25] | K |
|
| Tboil | 439.05 | K | Isobari... |
| Tboil | 438.95 | K | Experim... |
| Tboil | 439.25 | K | Vapor L... |
| Tboil | 439.15 | K | Vapor-L... |
| Tboil | 438.77 | K | Vapor-L... |
| Tboil | Outlier 438.20 | K | NIST |
| Tc | 534.50 | K | Joback Calculated Property |
| Tfus | 217.24 | K | Joback Calculated Property |
| Vc | 0.283 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [133.54; 180.05] | J/mol×K | [357.23; 534.50] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 130 140 150 160 170 180 400 450 500 | ||||
| Cp,gas | 133.54 | J/mol×K | 357.23 | Joback Calculated Property |
| Cp,gas | 142.19 | J/mol×K | 386.77 | Joback Calculated Property |
| Cp,gas | 150.46 | J/mol×K | 416.32 | Joback Calculated Property |
| Cp,gas | 158.37 | J/mol×K | 445.86 | Joback Calculated Property |
| Cp,gas | 165.94 | J/mol×K | 475.41 | Joback Calculated Property |
| Cp,gas | 173.16 | J/mol×K | 504.95 | Joback Calculated Property |
| Cp,gas | 180.05 | J/mol×K | 534.50 | Joback Calculated Property |
| Cp,liquid | 178.20 | J/mol×K | 298.15 | NIST |
| η | [0.0007630; 0.0009370] | Pa×s | [298.15; 318.15] |
|
| η | 0.0009370 | Pa×s | 298.15 | Density... |
| η | 0.0008410 | Pa×s | 308.15 | Density... |
| η | 0.0007630 | Pa×s | 318.15 | Density... |
| ΔfusH | [8.20; 10.42] | kJ/mol | [251.40; 254.20] |
|
| ΔfusH | 10.42 | kJ/mol | 251.40 | NIST |
| ΔfusH | 8.20 | kJ/mol | 253.20 | NIST |
| ΔfusH | 10.20 | kJ/mol | 254.20 | NIST |
| ΔvapH | [45.10; 67.90] | kJ/mol | [333.00; 397.00] |
|
| ΔvapH | 45.20 | kJ/mol | 333.00 | NIST |
| ΔvapH | 67.90 | kJ/mol | 367.50 | NIST |
| ΔvapH | 45.10 | kJ/mol | 397.00 | NIST |
| Pvap | [0.05; 101.33] | kPa | [276.50; 439.25] |
|
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 300 350 400 | ||||
| Pvap | 0.05 | kPa | 276.50 | Vapour ... |
| Pvap | 0.05 | kPa | 278.20 | Vapour ... |
| Pvap | 0.06 | kPa | 279.70 | Vapour ... |
| Pvap | 0.07 | kPa | 281.30 | Vapour ... |
| Pvap | 0.08 | kPa | 283.00 | Vapour ... |
| Pvap | 0.10 | kPa | 286.40 | Vapour ... |
| Pvap | 0.11 | kPa | 288.20 | Vapour ... |
| Pvap | 0.13 | kPa | 290.80 | Vapour ... |
| Pvap | 0.14 | kPa | 291.20 | Vapour ... |
| Pvap | 0.16 | kPa | 293.20 | Vapour ... |
| Pvap | 0.20 | kPa | 296.30 | Vapour ... |
| Pvap | 0.23 | kPa | 298.10 | Vapour ... |
| Pvap | 0.29 | kPa | 298.15 | Vapor P... |
| Pvap | 0.23 | kPa | 298.20 | Vapour ... |
| Pvap | 0.27 | kPa | 300.70 | Vapour ... |
| Pvap | 0.31 | kPa | 303.00 | Vapour ... |
| Pvap | 0.39 | kPa | 303.15 | Vapor P... |
| Pvap | 0.32 | kPa | 303.20 | Vapour ... |
| Pvap | 0.35 | kPa | 305.20 | Vapour ... |
| Pvap | 0.38 | kPa | 305.60 | Vapour ... |
| Pvap | 0.44 | kPa | 308.00 | Vapour ... |
| Pvap | 0.43 | kPa | 308.10 | Vapour ... |
| Pvap | 0.52 | kPa | 308.15 | Vapor P... |
| Pvap | 0.50 | kPa | 310.60 | Vapour ... |
| Pvap | 0.60 | kPa | 313.10 | Vapour ... |
| Pvap | 0.66 | kPa | 313.15 | (Vapour... |
| Pvap | 0.68 | kPa | 313.15 | Vapor P... |
| Pvap | 0.60 | kPa | 313.20 | Vapour ... |
| Pvap | 0.71 | kPa | 315.70 | Vapour ... |
| Pvap | 0.73 | kPa | 316.40 | Vapour ... |
| Pvap | 0.89 | kPa | 318.15 | Vapor P... |
| Pvap | 0.84 | kPa | 318.20 | Vapour ... |
| Pvap | 1.00 | kPa | 320.80 | Vapour ... |
| Pvap | 1.16 | kPa | 323.15 | Vapor P... |
| Pvap | 1.16 | kPa | 323.15 | Thermod... |
| Pvap | 1.11 | kPa | 323.20 | Vapour ... |
| Pvap | 1.13 | kPa | 323.30 | Vapour ... |
| Pvap | 1.28 | kPa | 325.80 | Vapour ... |
| Pvap | 1.64 | kPa | 328.15 | Vapor L... |
| Pvap | 1.61 | kPa | 328.15 | Vapor L... |
| Pvap | 1.53 | kPa | 328.15 | Vapor P... |
| Pvap | 1.48 | kPa | 328.30 | Vapour ... |
| Pvap | 1.98 | kPa | 333.15 | Vapor P... |
| Pvap | 1.98 | kPa | 333.15 | Thermod... |
| Pvap | 2.23 | kPa | 333.15 | Vapor L... |
| Pvap | 2.56 | kPa | 338.15 | Vapor P... |
| Pvap | 3.27 | kPa | 343.15 | Vapor P... |
| Pvap | 3.27 | kPa | 343.15 | Thermod... |
| Pvap | 3.39 | kPa | 343.15 | Vapor L... |
| Pvap | 4.13 | kPa | 348.15 | Vapor P... |
| Pvap | 5.29 | kPa | 353.15 | Vapor L... |
| Pvap | 5.19 | kPa | 353.15 | Vapor P... |
| Pvap | 5.32 | kPa | 353.15 | Vapor L... |
| Pvap | 5.35 | kPa | 353.15 | Vapor L... |
| Pvap | 5.37 | kPa | 353.15 | Vapor L... |
| Pvap | 5.19 | kPa | 353.15 | Thermod... |
| Pvap | 5.31 | kPa | 353.15 | Vapor L... |
| Pvap | 8.46 | kPa | 363.15 | Vapor L... |
| Pvap | 8.00 | kPa | 363.15 | Thermod... |
| Pvap | 8.00 | kPa | 363.15 | Vapor P... |
| Pvap | 9.81 | kPa | 368.15 | Vapor P... |
| Pvap | 12.00 | kPa | 373.15 | Thermod... |
| Pvap | 11.98 | kPa | 373.15 | Vapor P... |
| Pvap | 14.52 | kPa | 378.15 | Vapor P... |
| Pvap | 17.50 | kPa | 383.15 | Vapor P... |
| Pvap | 17.55 | kPa | 383.15 | Thermod... |
| Pvap | 21.01 | kPa | 388.15 | Vapor P... |
| Pvap | 25.03 | kPa | 393.15 | Thermod... |
| Pvap | 25.03 | kPa | 393.15 | Vapor P... |
| Pvap | 29.69 | kPa | 398.15 | Vapor P... |
| Pvap | 35.02 | kPa | 403.15 | Vapor P... |
| Pvap | 35.04 | kPa | 403.15 | Thermod... |
| Pvap | 41.11 | kPa | 408.15 | Vapor P... |
| Pvap | 48.09 | kPa | 413.15 | Thermod... |
| Pvap | 48.06 | kPa | 413.15 | Vapor P... |
| Pvap | 55.91 | kPa | 418.15 | Vapor P... |
| Pvap | 64.73 | kPa | 423.15 | Thermod... |
| Pvap | 64.78 | kPa | 423.15 | Vapor P... |
| Pvap | 101.30 | kPa | 439.05 | Isobari... |
| Pvap | 101.30 | kPa | 439.15 | Vapor-L... |
| Pvap | 101.33 | kPa | 439.25 | Vapor L... |
| n0 | [1.42600; 1.43820] | [288.15; 318.18] |
|
|
|
T(K) Refractive Index 1.43 1.43 1.43 1.43 1.43 1.44 1.44 290 300 310 | ||||
| n0 | 1.43820 | 288.15 | Partial... | |
| n0 | 1.43520 | 298.15 | Vapor L... | |
| n0 | 1.43556 | 298.15 | Excess ... | |
| n0 | 1.43560 | 298.15 | Bubble ... | |
| n0 | 1.43630 | 298.15 | Density... | |
| n0 | 1.43460 | 298.15 | Partial... | |
| n0 | 1.43570 | 298.15 | Activit... | |
| n0 | 1.43570 | 298.15 | Densiti... | |
| n0 | 1.43560 | 298.15 | Bubble ... | |
| n0 | 1.43420 | 303.15 | Density... | |
| n0 | 1.43120 | 308.15 | Partial... | |
| n0 | 1.43200 | 308.15 | Density... | |
| n0 | 1.42600 | 318.18 | Partial... | |
| ρl | [875.43; 962.30] | kg/m3 | [273.15; 363.15] |
|
|
T(K) Liquid Density (kg/m3) 880 900 920 940 960 300 350 | ||||
| ρl | 959.16 | kg/m3 | 273.15 | Density... |
| ρl | 954.56 | kg/m3 | 278.15 | Density... |
| ρl | 954.78 | kg/m3 | 278.15 | Apparen... |
| ρl | 950.13 | kg/m3 | 283.15 | Density... |
| ρl | 950.04 | kg/m3 | 283.15 | Apparen... |
| ρl | 949.95 | kg/m3 | 283.15 | Density... |
| ρl | 950.19 | kg/m3 | 283.15 | Conduct... |
| ρl | 945.50 | kg/m3 | 288.15 | Densiti... |
| ρl | 945.35 | kg/m3 | 288.15 | Density... |
| ρl | 945.59 | kg/m3 | 288.15 | Conduct... |
| ρl | 945.59 | kg/m3 | 288.15 | Apparen... |
| ρl | 940.92 | kg/m3 | 293.15 | Volumet... |
| ρl | 940.98 | kg/m3 | 293.15 | Conduct... |
| ρl | 941.00 | kg/m3 | 293.15 | Densiti... |
| ρl | 940.92 | kg/m3 | 293.15 | Volumet... |
| ρl | 941.00 | kg/m3 | 293.15 | Densiti... |
| ρl | 941.34 | kg/m3 | 293.15 | Density... |
| ρl | 940.83 | kg/m3 | 293.15 | Apparen... |
| ρl | 962.30 | kg/m3 | 293.15 | Interpr... |
| ρl | 940.74 | kg/m3 | 293.15 | Density... |
| ρl | 936.54 | kg/m3 | 293.15 | Volumet... |
| ρl | 936.88 | kg/m3 | 298.15 | Thermod... |
| ρl | 950.20 | kg/m3 | 298.15 | Interpr... |
| ρl | 936.34 | kg/m3 | 298.15 | (Vapour... |
| ρl | 936.38 | kg/m3 | 298.15 | Apparen... |
| ρl | 936.14 | kg/m3 | 298.15 | Thermod... |
| ρl | 936.13 | kg/m3 | 298.15 | Density... |
| ρl | 936.80 | kg/m3 | 298.15 | Physics... |
| ρl | 936.50 | kg/m3 | 298.15 | Densiti... |
| ρl | 937.00 | kg/m3 | 298.15 | Densiti... |
| ρl | 936.27 | kg/m3 | 298.15 | Volumet... |
| ρl | 936.21 | kg/m3 | 298.15 | Thermod... |
| ρl | 936.29 | kg/m3 | 298.15 | Density... |
| ρl | 936.28 | kg/m3 | 298.15 | Solvati... |
| ρl | 936.34 | kg/m3 | 298.15 | Excess ... |
| ρl | 936.30 | kg/m3 | 298.15 | Volumet... |
| ρl | 936.73 | kg/m3 | 298.15 | PrhoT m... |
| ρl | 936.50 | kg/m3 | 298.15 | Thermod... |
| ρl | 936.50 | kg/m3 | 298.15 | Densiti... |
| ρl | 936.36 | kg/m3 | 298.15 | Limitin... |
| ρl | 936.30 | kg/m3 | 298.15 | Volumet... |
| ρl | 936.38 | kg/m3 | 298.15 | Conduct... |
| ρl | 936.50 | kg/m3 | 298.15 | Densiti... |
| ρl | 936.28 | kg/m3 | 298.15 | Solvati... |
| ρl | 936.54 | kg/m3 | 298.15 | Excess ... |
| ρl | 936.73 | kg/m3 | 298.15 | Density... |
| ρl | 936.31 | kg/m3 | 298.15 | Thermod... |
| ρl | 936.27 | kg/m3 | 298.15 | Volumet... |
| ρl | 936.22 | kg/m3 | 298.15 | Apparen... |
| ρl | 935.90 | kg/m3 | 298.15 | Conduct... |
| ρl | 931.62 | kg/m3 | 303.15 | Volumet... |
| ρl | 932.11 | kg/m3 | 303.15 | Density... |
| ρl | 932.00 | kg/m3 | 303.15 | Densiti... |
| ρl | 932.00 | kg/m3 | 303.15 | Thermod... |
| ρl | 932.00 | kg/m3 | 303.15 | Densiti... |
| ρl | 941.35 | kg/m3 | 303.15 | Effect ... |
| ρl | 931.85 | kg/m3 | 303.15 | Influen... |
| ρl | 931.67 | kg/m3 | 303.15 | Solvati... |
| ρl | 931.62 | kg/m3 | 303.15 | Volumet... |
| ρl | 931.51 | kg/m3 | 303.15 | Density... |
| ρl | 931.67 | kg/m3 | 303.15 | Solvati... |
| ρl | 931.61 | kg/m3 | 303.15 | Apparen... |
| ρl | 931.69 | kg/m3 | 303.15 | Density... |
| ρl | 936.00 | kg/m3 | 303.15 | Interpr... |
| ρl | 931.85 | kg/m3 | 303.15 | Effect ... |
| ρl | 931.76 | kg/m3 | 303.15 | Conduct... |
| ρl | 927.26 | kg/m3 | 308.15 | Effect ... |
| ρl | 927.14 | kg/m3 | 308.15 | Apparen... |
| ρl | 926.80 | kg/m3 | 308.15 | Interpr... |
| ρl | 926.90 | kg/m3 | 308.15 | Densiti... |
| ρl | 927.05 | kg/m3 | 308.15 | Solvati... |
| ρl | 926.89 | kg/m3 | 308.15 | Volumet... |
| ρl | 927.49 | kg/m3 | 308.15 | Density... |
| ρl | 926.89 | kg/m3 | 308.15 | Volumet... |
| ρl | 927.60 | kg/m3 | 308.15 | Densiti... |
| ρl | 927.80 | kg/m3 | 308.15 | Thermod... |
| ρl | 927.26 | kg/m3 | 308.15 | Influen... |
| ρl | 927.14 | kg/m3 | 308.15 | Conduct... |
| ρl | 927.50 | kg/m3 | 308.15 | Densiti... |
| ρl | 927.05 | kg/m3 | 308.15 | Solvati... |
| ρl | 922.42 | kg/m3 | 313.15 | Solvati... |
| ρl | 922.66 | kg/m3 | 313.15 | Effect ... |
| ρl | 923.00 | kg/m3 | 313.15 | Densiti... |
| ρl | 922.10 | kg/m3 | 313.15 | Interpr... |
| ρl | 922.86 | kg/m3 | 313.15 | Density... |
| ρl | 922.52 | kg/m3 | 313.15 | Conduct... |
| ρl | 922.66 | kg/m3 | 313.15 | Influen... |
| ρl | 922.09 | kg/m3 | 313.15 | Volumet... |
| ρl | 922.26 | kg/m3 | 313.15 | Density... |
| ρl | 922.35 | kg/m3 | 313.15 | Apparen... |
| ρl | 922.43 | kg/m3 | 313.15 | Density... |
| ρl | 922.41 | kg/m3 | 313.15 | Solvati... |
| ρl | 923.50 | kg/m3 | 313.15 | Thermod... |
| ρl | 922.09 | kg/m3 | 313.15 | Volumet... |
| ρl | 922.44 | kg/m3 | 313.15 | Density... |
| ρl | 923.10 | kg/m3 | 313.15 | Densiti... |
| ρl | 917.23 | kg/m3 | 318.15 | Volumet... |
| ρl | 917.89 | kg/m3 | 318.15 | Conduct... |
| ρl | 917.23 | kg/m3 | 318.15 | Volumet... |
| ρl | 917.86 | kg/m3 | 318.15 | Apparen... |
| ρl | 917.79 | kg/m3 | 318.15 | Solvati... |
| ρl | 918.23 | kg/m3 | 318.15 | Density... |
| ρl | 918.60 | kg/m3 | 318.15 | Densiti... |
| ρl | 918.50 | kg/m3 | 318.15 | Densiti... |
| ρl | 918.06 | kg/m3 | 318.15 | Influen... |
| ρl | 917.78 | kg/m3 | 318.15 | Solvati... |
| ρl | 918.06 | kg/m3 | 318.15 | Effect ... |
| ρl | 913.59 | kg/m3 | 323.15 | Density... |
| ρl | 913.13 | kg/m3 | 323.15 | Density... |
| ρl | 913.44 | kg/m3 | 323.15 | Influen... |
| ρl | 912.23 | kg/m3 | 323.15 | Volumet... |
| ρl | 912.23 | kg/m3 | 323.15 | Volumet... |
| ρl | 913.17 | kg/m3 | 323.15 | Density... |
| ρl | 912.99 | kg/m3 | 323.15 | Density... |
| ρl | 913.08 | kg/m3 | 323.15 | Apparen... |
| ρl | 913.44 | kg/m3 | 323.15 | Effect ... |
| ρl | 908.93 | kg/m3 | 328.15 | Density... |
| ρl | 908.81 | kg/m3 | 328.15 | Influen... |
| ρl | 908.81 | kg/m3 | 328.15 | Effect ... |
| ρl | 903.86 | kg/m3 | 333.15 | Density... |
| ρl | 903.76 | kg/m3 | 333.15 | Apparen... |
| ρl | 904.16 | kg/m3 | 333.15 | Influen... |
| ρl | 903.68 | kg/m3 | 333.15 | Density... |
| ρl | 904.27 | kg/m3 | 333.15 | Density... |
| ρl | 904.16 | kg/m3 | 333.15 | Effect ... |
| ρl | 899.60 | kg/m3 | 338.15 | Density... |
| ρl | 899.53 | kg/m3 | 338.15 | Influen... |
| ρl | 899.53 | kg/m3 | 338.15 | Effect ... |
| ρl | 894.87 | kg/m3 | 343.15 | Influen... |
| ρl | 894.87 | kg/m3 | 343.15 | Effect ... |
| ρl | 894.31 | kg/m3 | 343.15 | Density... |
| ρl | 894.91 | kg/m3 | 343.15 | Density... |
| ρl | 890.19 | kg/m3 | 348.15 | Effect ... |
| ρl | 890.19 | kg/m3 | 348.15 | Influen... |
| ρl | 885.51 | kg/m3 | 353.15 | Influen... |
| ρl | 884.90 | kg/m3 | 353.15 | Density... |
| ρl | 885.51 | kg/m3 | 353.15 | Effect ... |
| ρl | 875.43 | kg/m3 | 363.15 | Density... |
| csound,fluid | [1455.37; 1455.91] | m/s | [298.15; 298.15] |
|
| csound,fluid | 1455.91 | m/s | 298.15 | Isentro... |
| csound,fluid | 1455.37 | m/s | 298.15 | Apparen... |
| csound,fluid | 1455.37 | m/s | 298.15 | Adiabat... |
Datasets
Refractive index (Na D-line)
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Refractive index (Na D-line) - Liquid |
| 85.90 | 298.15 | 1.436 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 85.90 | 298.15 | 936.57 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 936.31 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 100.00 | 945.7 |
| 288.15 | 2000.00 | 946.7 |
| 288.15 | 4000.00 | 947.8 |
| 288.15 | 6000.00 | 949.0 |
| 288.15 | 8100.00 | 950.1 |
| 288.15 | 9900.00 | 951.1 |
| 288.15 | 12000.00 | 952.2 |
| 288.15 | 13900.00 | 953.2 |
| 288.15 | 16000.00 | 954.3 |
| 288.15 | 18100.00 | 955.4 |
| 288.15 | 20000.00 | 956.5 |
| 298.15 | 100.00 | 937.0 |
| 298.15 | 2000.00 | 938.1 |
| 298.15 | 4100.00 | 939.4 |
| 298.15 | 6100.00 | 940.6 |
| 298.15 | 8100.00 | 941.8 |
| 298.15 | 10000.00 | 943.0 |
| 298.15 | 12100.00 | 944.1 |
| 298.15 | 14200.00 | 945.3 |
| 298.15 | 16300.00 | 946.4 |
| 298.15 | 18400.00 | 947.5 |
| 298.15 | 20100.00 | 948.6 |
| 308.15 | 100.00 | 927.9 |
| 308.15 | 2000.00 | 929.1 |
| 308.15 | 4100.00 | 930.4 |
| 308.15 | 6100.00 | 931.6 |
| 308.15 | 8100.00 | 932.8 |
| 308.15 | 10100.00 | 934.0 |
| 308.15 | 12100.00 | 935.3 |
| 308.15 | 14200.00 | 936.5 |
| 308.15 | 16300.00 | 937.6 |
| 308.15 | 18200.00 | 938.7 |
| 308.15 | 20200.00 | 939.9 |
| 318.15 | 100.00 | 918.7 |
| 318.15 | 2000.00 | 919.8 |
| 318.15 | 4000.00 | 921.2 |
| 318.15 | 6000.00 | 922.5 |
| 318.15 | 8000.00 | 923.8 |
| 318.15 | 9900.00 | 925.0 |
| 318.15 | 12000.00 | 926.3 |
| 318.15 | 14000.00 | 927.5 |
| 318.15 | 16000.00 | 928.7 |
| 318.15 | 18100.00 | 930.0 |
| 318.15 | 20000.00 | 931.3 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [5.63e-03; 3302.88] | kPa | [253.15; 658.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | -4.27944e+01 | |||
| Coefficient B | -3.73912e+03 | |||
| Coefficient C | 9.62289e+00 | |||
| Coefficient D | -1.35470e-05 | |||
| Temperature range, min. | 253.15 | |||
| Temperature range, max. | 658.00 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 300 400 500 600 | ||||
| Pvap | 5.63e-03 | kPa | 253.15 | Calculated Property |
| Pvap | 0.18 | kPa | 298.13 | Calculated Property |
| Pvap | 2.44 | kPa | 343.12 | Calculated Property |
| Pvap | 18.09 | kPa | 388.10 | Calculated Property |
| Pvap | 85.70 | kPa | 433.08 | Calculated Property |
| Pvap | 286.84 | kPa | 478.07 | Calculated Property |
| Pvap | 725.50 | kPa | 523.05 | Calculated Property |
| Pvap | 1453.89 | kPa | 568.03 | Calculated Property |
| Pvap | 2389.13 | kPa | 613.02 | Calculated Property |
| Pvap | 3302.88 | kPa | 658.00 | Calculated Property |
Similar Compounds
Find more compounds similar to N,N-Dimethylacetamide.
Mixtures
- Formamide, N,N-dimethyl- + N,N-Dimethylacetamide
- Benzenamine, 4,4'-oxybis- + N,N-Dimethylacetamide
- Benzene, 1,2-dichloro- + N,N-Dimethylacetamide
- N,N-Dimethylacetamide + Benzene, 1,3-dichloro-
- Benzene, 1,2,4-trichloro- + N,N-Dimethylacetamide
- Benzene, 1-chloro-2-methyl- + N,N-Dimethylacetamide
- Benzene, 1-chloro-3-methyl- + N,N-Dimethylacetamide
- N,N-Dimethylacetamide + Benzene, 1-chloro-4-methyl-
- Benzene, 1-methyl-2-nitro- + N,N-Dimethylacetamide
- Benzene, 1-methyl-3-nitro- + N,N-Dimethylacetamide
- N,N-Dimethylacetamide + 1-Propanamine, N-propyl-
- 1-Butanamine, N-butyl- + N,N-Dimethylacetamide
- 1-Butanamine + N,N-Dimethylacetamide
- 1-Hexanamine + N,N-Dimethylacetamide
- N,N-Dimethylacetamide + lithium chloride
- lithium bromide + N,N-Dimethylacetamide
- N,N-Dimethylacetamide + Ethylbenzene
- N,N-Dimethylacetamide + Water
- N,N-Dimethylacetamide + Tetrabutylammonium hexafluorophosphate
- Ethanol + N,N-Dimethylacetamide
Find more mixtures with N,N-Dimethylacetamide.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Volumetric Properties of the Ionic Liquid, 1-Butyl-3-methylimidazolium Tetrafluoroborate, in Organic Solvents at T = 298.15 K
- Interpretation of Association Behavior and Molecular Interactions in Binary Mixtures from Thermoacoustics and Molecular Compression Data
- Activity coefficients and excess Gibbs energy of binary mixtures of N,N-dimethyl formamide with selected compounds at 95.5 kPa
- Thermodynamic properties of vanadyl (N,N'-salicylideneethylendiamine) Schiff base complex in ionic liquid + N,N-dimethylacetamide solutions
- Vapor-liquid equilibria of difluoromethane + N,N-dimethylacetamide, difluoromethane + dimethylether diethylene glycol and 1,1-difluoroethane + dimethylether diethylene glycol systems
- Effect of solvent on the volumetric behavior ofN,N' -salicylidenephenyl diamine (Salophen) Schiff base at differenttemperatures (288.15 - 318.15) K
- Measurement and correlation of the solubility of 4,4'-oxydianiline in different organic solvents
- Determination and correlation of liquid-liquid equilibrium data for the dichloromethane + water + N, N-dimethylacetamide + NaCl system
- Isobaric vapor-liquid equilibrium for ternary system of sec-butyl alcohol + sec-butyl acetate + N,N- dimethyl acetamide at 101.3 kPa
- Effect of various substituents on benzene ring and their impact on volumetric, acoustic and transport properties of binary liquid mixtures with dimethylacetamide
- Isobaric vapor-liquid equilibrium of acetic acid + N,N-dimethylacetamide + 1-butyl-3-methylimidazolium Bis [(trifluoromethyl)sulfonyl]-imide
- Isobaric vapor-liquid equilibrium for binary system of N, N-dimethyl formamide + N, N-dimethyl acetamide and quaternary system of sec-butyl alcohol + sec-butyl acetate + N, N-dimethyl formamide + N, N-dimethyl acetamide at 101.3 kPa
- A model to calculate concentration-dependent surface tension of binary systems
- PrhoT measurement and PC-SAFT modeling of N,N-dimethyl formamide, N -methyl formamide, N,N-dimethyl acetamide, and ethylenediamine from T = (293.15-423.15) K and pressures up to 35 MPa
- Vapour pressures and enthalpies of vaporisation of N,N-di-alkylacetamides
- Thermodynamics of amide + amine mixtures. 5. Excess molar enthalpies of N,N-dimethylformamide or N,N-dimethylacetamide + N-propylpropan-1-amine, + N-butylbutan-1-amine, + butan-1-amine, or + hexan-1-amine systems at 298.15 K. Application of the ERAS model
- Thermodynamic properties of (LiCl + N,N-dimethylacetamide) and (LiBr + N,N-dimethylacetamide) at temperatures from (323.15 to 423.15) K
- Bubble temperature measurements on seven binary mixtures formed by ethylbenzene at 94.7 kPa
- Coexistence curves of critical nonaqueous microemulsions of (AOT + DMA + nonane) and (AOT + DMA + octane)
- Limiting partial molar volumes and expansibilities of ammonium perchlorate, tetraalkylammonium perchlorates, and tetrabutylammonium tetraphenylborate in N,N-dimethylformamide
- Volumetric properties of binary mixtures of (water + organic solvents) at temperatures between T = 288.15 K and T = 303.15 K at p = 0.1 MPa
- Volumetric and compressibility behaviour of ionic liquid, 1-n-butyl-3-methylimidazolium hexafluorophosphate and tetrabutylammonium hexafluorophosphate in organic solvents at T = 298.15 K
- (Vapour + liquid) equilibrium in (N,N-dimethylacetamide + ethanol + water) at the temperature 313.15 K
- Densities and volumetric properties of (acetonitrile + an amide) binary mixtures at temperatures between 293.15 K and 318.15 K
- (Vapour + liquid) equilibria and excess molar enthalpies for binary mixtures containing N,N-dialkylamides and 1-chloroalkanes
- Thermodynamic properties of N,N-dimethylformamide and N,N-dimethylacetamide
- Density and speed of sound of lithium bromide with organic solvents: Measurement and correlation
- Isentropic compressibilities of (amide + water) mixtures: A comparative study
- Excess molar enthalpies and (vapour + liquid) equilibria for mixtures containing N,N-dialkylamides and a,x-dichloroalkanes
- Excess volumes of mixing in (N,N-dimethylacetamide + methanol + water) and (N,N-dimethylacetamide + ethanol + water) at the temperature 313.15 K
- Apparent molar volumes and expansibilities of H2O and D2O in N,N-dimethylformamide and N,N-dimethylacetamide in the range of T = (278.15 to 318.15) K at p = 0.1 MPa: A comparative analysis
- Physics and chemistry of an ionic liquid in some industrially important solvent media probed by physicochemical techniques
- Densities and volumetric properties of binary mixtures of N,N-dimethylformamide/N,N-dimethylacetamide with some alkyl acrylates at temperatures from 288.15 K to 318.15 K
- Apparent molar volumes and compressibilities of lanthanum, gadolinium, lutetium and sodium trifluoromethanesulfonates in N,N-dimethylformamide and N,N-dimethylacetamide
- Densities, ultrasonic speeds, viscosities and excess properties of binary mixtures of methyl methacrylate with N,N-dimethylformamide and N,N-dimethylacetamide at different temperatures
- Effect of ionic liquid on the solvation behavior of nonaqueous N,N'-salicylidenephenylediamine Schiff base (Salophen) solutions at 298.15 K
- Effect of N,N'-bis(2-pyridylmethylidene)-1,2-diiminoethane Schiff base (BPIE) on the thermodynamic properties of the ionic liquid 1-hexyl-3-methylimidazolium chloride in N,N-dimethylacetamide solvent at T = 298.15 K
- Solvation of alkaline earth metal ions in N,N-dimethylformamide and N,N-dimethylacetamide - A volumetric and acoustic study
- Measurement and correlation of the solubility of rivaroxaban (form I) in binary mixtures of ethyl acetate with tetrahydrofuran, N,N-dimethylformamide, and N,N-dimethylacetamide from T = (278.15 to 318.15) K
- Measurement and prediction of dabigatran etexilate mesylate Form II solubility in mono-solvents and mixed solvents
- Effect of organic solvents on lowering the viscosity of 1-hexyl-3- methylimidazolium chloride
- Solvation of ionic liquids based on N-methyl-N-alkylmorpholinium cations in N,N-dimethylformamide and N,N-dimethylacetamide - Volumetric and compressibility studies
- Isobaric vapour-liquid equilibrium measurements and extractive distillation process for the azeotrope of (N,N-dimethylisopropylamine + acetone)
- Solubility modelling, solvent effect and preferential solvation of 6-chloropurine in several aqueous co-solvent mixtures between 283.15 K and 328.15 K
- Determination and correlation of solubility and solution thermodynamics of musk xylene in different pure solvents
- Experimental isobaric vapour-liquid equilibrium data for the binary system (N, N-dimethyl acetamide + dimethyl sulfoxide) and the quaternary system (sec-butyl acetate + sec-butyl alcohol + N, N-dimethyl acetamide + dimethyl sulfoxide) at 101.3 kPa
- Adducts of antimony triiodide and 2-aminomethylpyridines: Synthesis, characterization and thermochemistry
- Thermochemistry of 1-bromoadamantane in binary mixtures of water aprotic solvent
- Enthalpies of vaporization of N,N-dialkyl monamides at 298.15K
- Probing molecular interactions of ionic liquid in industrially important solvents by means of conductometric and spectroscopic approach
- Conductometric, refractometric and FT-IR spectroscopic study of [EMIm]NO3, [EMIm]CH3SO3, and [EMIm]OTs in N,N-dimethyl formamide, N,N-dimethyl acetamide and dimethyl sulphoxide
- Thermophysical study of the binary mixtures of N,N-dimethylacetamide with 2-propanol and 2-butanol
- Vapor Liquid Equilibrium Data for Binary Systems of N,N-Dimethylacetamide with Cyclohexene, Cyclohexane, and Benzene Separately at Atmospheric Pressure
- Determination and Correlation of Solubility of N-tertbutylacrylamide in Seven Different Solvents at Temperatures between (279.15 and 353.15) K
- Solubility of Etoricoxib in Aqueous Solutions of 1,4-Butanediol, 1,4-Dioxane, N,N-Dimethylacetamide, N,N-Dimethylformamide, Dimethyl Sulfoxide, and Ethanol at 298.2 K
- P-T-x Measurements for 1,1,1,2-Tetrafluoroethane (R134a) + N,N dimethylacetamide (DMA), and N-methyl-2-pyrrolidone (NMP)
- Density and Viscosity Measurements for Binary Mixtures of 1-Ethyl-3-methylimidazolium Tetrafluoroborate ([Emim][BF4]) with Dimethylacetamide, Dimethylformamide, and Dimethyl Sulfoxide
- Density, Speed of Sound, Refractive Index, and Viscosity of the Binary Mixtures of N,N-dimethylacetamide with Methanol and Ethanol
- Conductance and Ionic Association of Imidazolium-Based Ionic Liquids in N,N-Dimethylacetamide
- Density and Speed of Sound of Binary Mixtures of Ionic Liquid 1-Ethyl-3-methylimidazolium Tetrafluoroborate, N,N-Dimethylformamide, and N,N-Dimethylacetamide at Temperature Range of 293.15 343.15 K: Measurement and PC-SAFT Modeling
- Density, Viscosity, and Electrical Conductivity of Protic Amidium Bis(trifluoromethanesulfonyl)amide Ionic Liquids
- Influence of Aprotic Cosolvents on the Thermophysical Properties of Imidazolium-Based Ionic Liquid
- Vapor Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide
- Measurement and Thermodynamic Modeling of Ternary (Liquid + Liquid) Equilibrium for Extraction of N,N-Dimethylacetamide from Aqueous Solution with Different Solvents
- Measurement and Correlation of Vapor-Liquid Equilibrium for R124 (1-Chloro-1,2,2,2-Tetrafluoroethane)-NMP (N-Methyl-2-Pyrrolidone) and R124-DMF (N,N-Dimethylformamide) Mixtures
- Solution Thermodynamics of Benzotriazole in Different Pure Solvents
- Vapor-Liquid Equilibrium for Binary of 1-Butanol + N,N-Dimethylacetamide and Methyl Isobutyl Ketone + N,N-Dimethylacetamide at 101.3 kPa
- Bubble Temperature Measurements on Binary Mixtures Formed by Cyclohexane at 94.7 kPa
- Solubility of Tripolycyanamide and Cyanuric Acid in Ethanediol, N,N-Dimethylformamide, and N,N-Dimethylacetamide from (301.07 to 363.35) K
- Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of 1,4-Dioxane with Different Organic Liquids at (298.15, 303.15, and 308.15) K
- Excess Molar Volumes and Kinematic Viscosities for Binary Mixtures of Dipropylene Glycol Monobutyl Ether and Dipropylene Glycol tert-Butyl Ether with 2-Pyrrolidinone, N-Methyl-2-pyrrolidinone, N,N-Dimethylformamide, and N,N-Dimethylacetamide at 298.15 K
- Vapor Pressures of Propylene Carbonate and N,N-Dimethylacetamide
- Thermodynamics of Mixtures Containing a Strongly Polar Compound. 8. Liquid-Liquid Equilibria for N,N-Dialkylamide + Selected N-Alkanes
- Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of N,N-Dimethylacetamide (1) + 2-Methylbutan-2-ol (2) + Ethyl Acetate (3) at 298.15 K for the Liquid Region and at Ambient Pressure
- Apparent Molar Compressibilities and Volumes of Some 1,1-Electrolytes in N,N-Dimethylacetamide and N,N-Dimethylformamide
- Solubility of Anthracene in N,N-Dimethyformamide, N,N-Dimethylacetamide, and N-Methyl-2-pyrrolidone
- Measurement and Correlation of Griseofulvin Solubility in Different Solvents at Temperatures from (281.95 to 357.60) K
- Density, Viscosity, and Speed of Sound of (1-Octanol + 2-Methoxyethanol), (1-Octanol + N,N-Dimethylacetamide), and (1-Octanol + Acetophenone) at Temperatures of (298.15, 308.15, and 318.15) K
- Partial Molar Volumes of N,N'-1,2-Ethyl-bis(salicyladimine) Schiff Base (Salen) in Organic Solvents at T = (283.15 to 318.15) K
- Volumes, Heat Capacities, and Compressibilities of the Mixtures of Acetonitrile with N,N-Dimethylacetamide and Propylene Carbonate
- Critical Assessment of CO2 Solubility in Volatile Solvents at 298.15 K
- Solubilities of Pioglitazone Hydrochloride in Different Solvents
- Thermodynamic Properties and Crystal Structures of the Adductive 2,6-Naphthalenedicarboxylic Acid Crystallization with N,N-Dimethyl Acetamide and N-Methyl Pyrrolidone
- Vapor Liquid Equilibrium for Ternary and Binary Mixtures of 2-Isopropoxypropane, 2-Propanol, and N,N-Dimethylacetamide at 101.3 kPa
- Isothermal Vapor Liquid Equilibrium Measurements of 1,1-Difluoroethane + N,N-Dimethylformamide and N,N-Dimethylacetamide
- Thermodynamics of Mixtures Containing a Very Strongly Polar Compound. 10. Liquid Liquid Equilibria for N,N-Dimethylacetamide + Selected Alkanes
- Solubility and Dissolution Thermodynamic Data of Mefenamic Acid Crystals in Different Classes of Organic Solvents
- Measurement and Correlation of Isothermal Vapor Liquid Equilibrium of Fluoroethane + N,N-Dimethylacetamide, Fluoroethane + N-Methyl-2-pyrrolidone, and 1,1,1,2-Tetrafluoroethane + N,N-Dimethylacetamide Systems
- Volumetric Properties of Binary Mixtures of 1-Butyl-1-Methylpyrrolidinium Tris(pentafluoroethyl)trifluorophosphate with N-Methylformamide, N-Ethylformamide, N,N-Dimethylformamide, N,N-Dibutylformamide, and N,N-Dimethylacetamide from (293.15 to 323.15) K
- Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
- Solid Liquid Equilibrium (SLE) of the N,N-Dimethylacetamide (DMA) + MCl (M = Na, K, Rb, and Cs) + Water Ternary Systems at Multiple Temperatures
- Determination and Correlation of Liquid Liquid Equilibrium Data for the Ternary Dichloromethane + Water + N,N-Dimethylacetamide System
- Volumetric Properties of Binary Mixtures of 1-Butyl-3-Methylimidazolium Tris(pentafluoroethyl)trifluorophosphate with N-Methylformamide, N-Ethylformamide, N,N-Dimethylformamide, N,N-Dibutylformamide, and N,N-Dimethylacetamide from (293.15 to 323.15) K
- Solubility of Hydrogen Sulfide in N-Methylacetamide and N,N-Dimethylacetamide: Experimental Measurement and Modeling
- Measurement and Correlation of Isothermal Vapor Liquid Equilibrium of 1,1,1,3,3-Pentafluoropropane + N,N-Dimethylacetamide and 1,1,1,3,3,3-Hexafluoropropane + N,N-Dimethylacetamide/Diethylene Glycol Dimethyl Ether Systems
- Densities and Isothermal Compressibilities at Pressures up to 20 MPa of the Systems N,N-Dimethylformamide or N,N-Dimethylacetamide + 1-Chloroalkane
- Densities and Isothermal Compressibilities at Pressures up to 20 MPa of the Systems N,N-Dimethylformamide or N,N-Dimethylacetamide + r,o-Dichloroalkane
- Solubility of Terephthalic Acid in Aqueous N-Methyl Pyrrolidone and N,N-Dimethyl Acetamide Solvents at (303.2 to 363.2) K
- Adiabatic Compressibilities of Divalent Transition-Metal Perchlorates and Chlorides in N,N-Dimethylacetamide and Dimethylsulfoxide
- Vapor-Liquid Equilibrium Data for N-Methylacetamide and N,N-Dimethylacetamide with Cumene at 97.3 kPa
- Liquid-Liquid Equilibria for Water + Benzonitrile + N-Methylacetamide, or + N,N-Dimethylacetamide
- Joback Method
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
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