- InChI
- InChI=1S/C5H9NO/c1-6-4-2-3-5(6)7/h2-4H2,1H3
- InChI Key
- SECXISVLQFMRJM-UHFFFAOYSA-N
- Formula
- C5H9NO
- SMILES
- CN1CCCC1=O
- Molecular Weight1
- 99.13
- CAS
- 872-50-4
- Other Names
-
- 1-Methyl-2-Pyrrolidinone
- 1-Methyl-2-pyrrolidone
- 1-Methyl-5-pyrrolidinone
- 1-Methylazacyclopentan-2-one
- 1-Methylazacyclopentane-2-one
- 1-Methylpyrrolidinone
- 1-Methylpyrrolidone
- 1-methylpyrrolidin-2-one
- 2-Pyrrolidone, 1-methyl-
- Agsolex 1
- M-Pyrol
- Methylpyrrolidone
- Micropure ultra
- N 0131
- N-Methyl-2-pyrrolidinone
- N-Methyl-2-pyrrolidone
- N-Methyl-gamma-butyrolactam
- N-Methyl-«alpha»-pyrrolidinone
- N-Methyl-«alpha»-pyrrolidone
- N-Methyl-«gamma»-butyrolactam
- N-Methyl-«alpha»-pyrrolidinone
- N-Methyl-«alpha»-pyrrolidone
- N-Methyl-«gamma»-butyrolactam
- N-Methylpyrrolid-2-one
- N-Methylpyrrolidinone
- N-Methylpyrrolidone
- N-Methylpyrrolidone-(2)
- N-methyl-.alpha.-pyrrolidinone
- N-methyl-.alpha.-pyrrolidone
- N-methyl-.gamma.-butyrolactam
- N-methylpyrrolidin-2-one
- NMP
- NSC 4594
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- 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.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| PAff | 923.50 | kJ/mol | NIST |
| BasG | 891.60 | kJ/mol | NIST |
| ΔcH°liquid | [-2994.00; -2988.05] | kJ/mol |
|
| ΔcH°liquid | -2988.05 ± 0.46 | kJ/mol | NIST |
| ΔcH°liquid | -2992.00 ± 0.40 | kJ/mol | NIST |
| ΔcH°liquid | -2994.00 | kJ/mol | NIST |
| ΔfH°gas | -210.85 ± 0.56 | kJ/mol | NIST |
| ΔfH°liquid | -265.73 ± 0.54 | kJ/mol | NIST |
| ΔfusH° | [11.04; 11.04] | kJ/mol |
|
| ΔfusH° | 11.04 | kJ/mol | (Solid ... |
| ΔfusH° | 11.04 | kJ/mol | Thermod... |
| ΔvapH° | [54.88; 61.90] | kJ/mol |
|
| ΔvapH° | 61.90 | kJ/mol | NIST |
| ΔvapH° | 54.88 ± 0.13 | kJ/mol | NIST |
| IE | 9.17 | eV | NIST |
| log10WS | 1.00 | Aq. Sol... | |
| logPoct/wat | 0.239 | Crippen Calculated Property | |
| McVol | 82.000 | ml/mol | McGowan Calculated Property |
| Pc | 4520.00 ± 25.00 | kPa | NIST |
| ρc | 319.20 ± 5.95 | kg/m3 | NIST |
| Inp | [1002.00; 1083.00] |
|
|
| Inp | 1045.50 | NIST | |
| Inp | 1045.00 | NIST | |
| Inp | 1043.00 | NIST | |
| Inp | 1012.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1083.00 | NIST | |
| Inp | 1009.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1045.50 | NIST | |
| Inp | 1083.00 | NIST | |
| Inp | 1002.00 | NIST | |
| I | [1646.00; 1679.00] |
|
|
| I | 1646.00 | NIST | |
| I | 1678.00 | NIST | |
| I | 1660.00 | NIST | |
| I | 1660.00 | NIST | |
| I | 1665.00 | NIST | |
| I | 1662.00 | NIST | |
| I | 1679.00 | NIST | |
| I | 1652.00 | NIST | |
| I | 1678.00 | NIST | |
| I | 1646.00 | NIST | |
| Tboil | [475.20; 477.01] | K |
|
| Tboil | Outlier 477.01 | K | Isobari... |
| Tboil | 475.29 | K | Measure... |
| Tboil | 475.44 | K | Separat... |
| Tboil | 476.05 | K | Separat... |
| Tboil | 475.45 | K | Vapor-L... |
| Tboil | 475.20 | K | NIST |
| Tc | [721.70; 721.80] | K |
|
| Tc | 721.70 ± 0.50 | K | NIST |
| Tc | 721.80 ± 0.40 | K | NIST |
| Tfus | [249.48; 249.68] | K |
|
| Tfus | 249.48 | K | Aq. Sol... |
| Tfus | 249.68 | K | (Solid ... |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [165.44; 412.40] | J/mol×K | [293.15; 353.15] |
|
| Cp,liquid | 165.44 | J/mol×K | 293.15 | Excess ... |
| Cp,liquid | 165.44 | J/mol×K | 293.15 | Excess ... |
| Cp,liquid | 307.80 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 412.40 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 166.22 | J/mol×K | 298.15 | Excess ... |
| Cp,liquid | 166.22 | J/mol×K | 298.15 | Excess ... |
| Cp,liquid | 174.83 | J/mol×K | 298.15 | Thermod... |
| Cp,liquid | 166.92 | J/mol×K | 303.15 | Excess ... |
| Cp,liquid | 166.00 | J/mol×K | 303.15 | Molar H... |
| Cp,liquid | 166.92 | J/mol×K | 303.15 | Excess ... |
| Cp,liquid | 167.21 | J/mol×K | 308.15 | Excess ... |
| Cp,liquid | 177.38 | J/mol×K | 308.15 | Thermod... |
| Cp,liquid | 167.00 | J/mol×K | 308.15 | Molar H... |
| Cp,liquid | 168.00 | J/mol×K | 313.15 | Molar H... |
| Cp,liquid | 179.94 | J/mol×K | 318.15 | Thermod... |
| Cp,liquid | 169.00 | J/mol×K | 318.15 | Molar H... |
| Cp,liquid | 170.00 | J/mol×K | 323.15 | Molar H... |
| Cp,liquid | 182.77 | J/mol×K | 328.15 | Thermod... |
| Cp,liquid | 172.00 | J/mol×K | 328.15 | Molar H... |
| Cp,liquid | 174.00 | J/mol×K | 333.15 | Molar H... |
| Cp,liquid | 175.00 | J/mol×K | 338.15 | Molar H... |
| Cp,liquid | 185.78 | J/mol×K | 338.15 | Thermod... |
| Cp,liquid | 176.00 | J/mol×K | 343.15 | Molar H... |
| Cp,liquid | 177.00 | J/mol×K | 348.15 | Molar H... |
| Cp,liquid | 189.27 | J/mol×K | 348.15 | Thermod... |
| Cp,liquid | 178.00 | J/mol×K | 353.15 | Molar H... |
| η | [0.0005320; 0.0021620] | Pa×s | [283.15; 423.15] |
|
| η | 0.0021620 | Pa×s | 283.15 | Viscome... |
| η | 0.0018220 | Pa×s | 293.15 | Viscome... |
| η | 0.0018110 | Pa×s | 293.15 | Densiti... |
| η | 0.0016670 | Pa×s | 298.15 | Densiti... |
| η | 0.0016600 | Pa×s | 298.15 | Influen... |
| η | 0.0016560 | Pa×s | 298.15 | Volumet... |
| η | 0.0016830 | Pa×s | 298.15 | Physica... |
| η | 0.0016630 | Pa×s | 298.15 | Densiti... |
| η | 0.0016950 | Pa×s | 298.15 | Viscome... |
| η | 0.0015544 | Pa×s | 303.15 | Thermod... |
| η | 0.0015430 | Pa×s | 303.15 | Densiti... |
| η | 0.0015540 | Pa×s | 303.15 | Densiti... |
| η | 0.0015580 | Pa×s | 303.15 | Physica... |
| η | 0.0014900 | Pa×s | 303.15 | Influen... |
| η | 0.0015210 | Pa×s | 303.15 | Densiti... |
| η | 0.0015540 | Pa×s | 303.15 | Thermod... |
| η | 0.0016080 | Pa×s | 303.15 | Viscome... |
| η | 0.0013900 | Pa×s | 308.15 | Influen... |
| η | 0.0014370 | Pa×s | 308.15 | Densiti... |
| η | 0.0014700 | Pa×s | 308.15 | Physica... |
| η | 0.0013650 | Pa×s | 308.15 | Densiti... |
| η | 0.0013370 | Pa×s | 313.10 | Physica... |
| η | 0.0013320 | Pa×s | 313.15 | Densiti... |
| η | 0.0013320 | Pa×s | 313.15 | Thermod... |
| η | 0.0013190 | Pa×s | 313.15 | Densiti... |
| η | 0.0013100 | Pa×s | 313.15 | Influen... |
| η | 0.0013830 | Pa×s | 313.15 | Viscome... |
| η | 0.0013220 | Pa×s | 313.15 | Volumet... |
| η | 0.0013321 | Pa×s | 313.15 | Thermod... |
| η | 0.0013430 | Pa×s | 313.15 | Densiti... |
| η | 0.0012100 | Pa×s | 318.15 | Densiti... |
| η | 0.0012480 | Pa×s | 318.15 | Physica... |
| η | 0.0012580 | Pa×s | 318.15 | Densiti... |
| η | 0.0011750 | Pa×s | 323.15 | Volumet... |
| η | 0.0011740 | Pa×s | 323.15 | Densiti... |
| η | 0.0011840 | Pa×s | 323.15 | Densiti... |
| η | 0.0011600 | Pa×s | 323.15 | Thermod... |
| η | 0.0011602 | Pa×s | 323.15 | Thermod... |
| η | 0.0011600 | Pa×s | 323.15 | Densiti... |
| η | 0.0012170 | Pa×s | 323.15 | Viscome... |
| η | 0.0011170 | Pa×s | 328.15 | Densiti... |
| η | 0.0010220 | Pa×s | 333.15 | Densiti... |
| η | 0.0010220 | Pa×s | 333.15 | Thermod... |
| η | 0.0010810 | Pa×s | 333.15 | Viscome... |
| η | 0.0010350 | Pa×s | 333.15 | Volumet... |
| η | 0.0010222 | Pa×s | 333.15 | Thermod... |
| η | 0.0010330 | Pa×s | 333.15 | Densiti... |
| η | 0.0009860 | Pa×s | 338.15 | Densiti... |
| η | 0.0009084 | Pa×s | 343.15 | Thermod... |
| η | 0.0009080 | Pa×s | 343.15 | Densiti... |
| η | 0.0009080 | Pa×s | 343.15 | Thermod... |
| η | 0.0009140 | Pa×s | 343.15 | Densiti... |
| η | 0.0010260 | Pa×s | 343.15 | Viscome... |
| η | 0.0009210 | Pa×s | 343.15 | Volumet... |
| η | 0.0008080 | Pa×s | 353.15 | Densiti... |
| η | 0.0008127 | Pa×s | 353.15 | Thermod... |
| η | 0.0009360 | Pa×s | 353.15 | Viscome... |
| η | 0.0008130 | Pa×s | 353.15 | Densiti... |
| η | 0.0008127 | Pa×s | 353.15 | Thermod... |
| η | 0.0008310 | Pa×s | 363.15 | Viscome... |
| η | 0.0007570 | Pa×s | 373.15 | Viscome... |
| η | 0.0007110 | Pa×s | 383.15 | Viscome... |
| η | 0.0006520 | Pa×s | 393.15 | Viscome... |
| η | 0.0006060 | Pa×s | 403.15 | Viscome... |
| η | 0.0005670 | Pa×s | 413.15 | Viscome... |
| η | 0.0005320 | Pa×s | 423.15 | Viscome... |
| ΔfusH | 18.10 | kJ/mol | 248.50 | NIST |
| ΔvapH | [47.70; 55.30] | kJ/mol | [295.00; 427.50] |
|
| ΔvapH | 55.30 | kJ/mol | 295.00 | NIST |
| ΔvapH | 53.10 | kJ/mol | 351.50 | NIST |
| ΔvapH | 49.30 | kJ/mol | 403.00 | NIST |
| ΔvapH | 53.40 | kJ/mol | 408.00 | NIST |
| ΔvapH | 47.70 | kJ/mol | 408.00 | NIST |
| ΔvapH | 49.20 | kJ/mol | 419.00 | NIST |
| ΔvapH | 49.50 | kJ/mol | 427.50 | NIST |
| Pvap | [0.50; 101.30] | kPa | [333.15; 476.05] |
|
| Pvap | 0.50 | kPa | 333.15 | Thermod... |
| Pvap | 1.29 | kPa | 352.27 | Vapor-L... |
| Pvap | 1.30 | kPa | 352.48 | Vapor-L... |
| Pvap | 1.30 | kPa | 353.15 | Thermod... |
| Pvap | 1.34 | kPa | 353.15 | Vapor-L... |
| Pvap | 1.82 | kPa | 359.26 | Vapor-L... |
| Pvap | 2.19 | kPa | 363.15 | Vapor-L... |
| Pvap | 2.22 | kPa | 363.36 | Vapor-L... |
| Pvap | 2.78 | kPa | 368.27 | Vapor-L... |
| Pvap | 3.44 | kPa | 373.09 | Vapor-L... |
| Pvap | 3.46 | kPa | 373.15 | Vapor-L... |
| Pvap | 3.60 | kPa | 373.15 | Thermod... |
| Pvap | 4.23 | kPa | 377.86 | Vapor-L... |
| Pvap | 4.74 | kPa | 380.73 | Vapor P... |
| Pvap | 5.24 | kPa | 383.12 | Vapor P... |
| Pvap | 5.98 | kPa | 386.38 | Vapor P... |
| Pvap | 6.36 | kPa | 387.92 | Vapor P... |
| Pvap | 6.86 | kPa | 389.88 | Vapor P... |
| Pvap | 7.78 | kPa | 393.04 | Vapor P... |
| Pvap | 10.29 | kPa | 400.46 | Vapor P... |
| Pvap | 11.62 | kPa | 403.85 | Vapor P... |
| Pvap | 12.87 | kPa | 406.68 | Vapor P... |
| Pvap | 13.96 | kPa | 408.96 | Vapor P... |
| Pvap | 15.22 | kPa | 411.42 | Vapor P... |
| Pvap | 16.50 | kPa | 413.77 | Vapor P... |
| Pvap | 18.28 | kPa | 416.81 | Vapor P... |
| Pvap | 20.97 | kPa | 420.94 | Vapor P... |
| Pvap | 23.65 | kPa | 424.65 | Vapor P... |
| Pvap | 25.96 | kPa | 427.56 | Vapor P... |
| Pvap | 28.10 | kPa | 430.09 | Vapor-l... |
| Pvap | 30.08 | kPa | 432.29 | Vapor P... |
| Pvap | 33.54 | kPa | 435.85 | Vapor P... |
| Pvap | 34.20 | kPa | 436.50 | Vapor-l... |
| Pvap | 36.99 | kPa | 439.12 | Vapor P... |
| Pvap | 39.96 | kPa | 441.74 | Vapor P... |
| Pvap | 40.00 | kPa | 441.80 | Isobari... |
| Pvap | 41.30 | kPa | 442.88 | Vapor-l... |
| Pvap | 42.73 | kPa | 444.04 | Vapor P... |
| Pvap | 46.02 | kPa | 446.64 | Vapor P... |
| Pvap | 47.90 | kPa | 448.05 | Vapor-l... |
| Pvap | 52.18 | kPa | 451.08 | Vapor P... |
| Pvap | 53.70 | kPa | 452.13 | Vapor-l... |
| Pvap | 60.50 | kPa | 456.48 | Vapor-l... |
| Pvap | 62.11 | kPa | 457.46 | Vapor P... |
| Pvap | 68.60 | kPa | 461.17 | Vapor-l... |
| Pvap | 76.40 | kPa | 465.29 | Vapor-l... |
| Pvap | 81.20 | kPa | 467.66 | Vapor-l... |
| Pvap | 88.70 | kPa | 471.15 | Vapor-l... |
| Pvap | 95.30 | kPa | 474.01 | Vapor-l... |
| Pvap | 95.30 | kPa | 474.01 | Activit... |
| Pvap | 99.40 | kPa | 475.72 | Vapor P... |
| Pvap | 101.30 | kPa | 476.05 | Separat... |
| n0 | [1.45590; 1.47060] | [293.10; 323.15] |
|
|
| n0 | 1.46860 | 293.10 | Extract... | |
| n0 | 1.46860 | 293.10 | Liquid-... | |
| n0 | 1.46860 | 293.10 | Solubil... | |
| n0 | 1.46770 | 293.10 | Densiti... | |
| n0 | 1.46960 | 293.10 | Liquid ... | |
| n0 | 1.46900 | 293.15 | Experim... | |
| n0 | 1.46910 | 293.15 | Density... | |
| n0 | 1.47060 | 293.15 | Density... | |
| n0 | 1.47030 | 293.15 | Vapor L... | |
| n0 | 1.46740 | 298.15 | Excess ... | |
| n0 | 1.46876 | 298.15 | Liquid ... | |
| n0 | 1.46740 | 298.15 | Excess ... | |
| n0 | 1.46740 | 298.15 | Isobari... | |
| n0 | 1.46770 | 298.15 | A study... | |
| n0 | 1.46800 | 298.15 | Density... | |
| n0 | 1.46900 | 298.15 | Experim... | |
| n0 | 1.46640 | 303.15 | Density... | |
| n0 | 1.46470 | 303.15 | Density... | |
| n0 | 1.46210 | 313.15 | Density... | |
| n0 | 1.46030 | 313.15 | Density... | |
| n0 | 1.45760 | 323.15 | Density... | |
| n0 | 1.45590 | 323.15 | Density... | |
| ρl | [1004.79; 1037.30] | kg/m3 | [288.15; 323.15] |
|
| ρl | 1037.30 | kg/m3 | 288.15 | Volumet... |
| ρl | 1028.29 | kg/m3 | 288.15 | Applica... |
| ρl | 1037.30 | kg/m3 | 288.15 | Volumet... |
| ρl | 1033.23 | kg/m3 | 293.15 | Thermod... |
| ρl | 1024.76 | kg/m3 | 293.15 | Applica... |
| ρl | 1032.84 | kg/m3 | 293.15 | Volumet... |
| ρl | 1033.23 | kg/m3 | 293.15 | Thermod... |
| ρl | 1032.84 | kg/m3 | 293.15 | Volumet... |
| ρl | 1033.28 | kg/m3 | 293.15 | Excess ... |
| ρl | 1033.30 | kg/m3 | 293.15 | Excess ... |
| ρl | 1032.66 | kg/m3 | 293.15 | Volumet... |
| ρl | 1026.00 | kg/m3 | 298.00 | Densiti... |
| ρl | 1027.91 | kg/m3 | 298.15 | Excess ... |
| ρl | 1028.17 | kg/m3 | 298.15 | Volumet... |
| ρl | 1028.26 | kg/m3 | 298.15 | Excess ... |
| ρl | 1025.90 | kg/m3 | 298.15 | Tempera... |
| ρl | 1028.38 | kg/m3 | 298.15 | Volumet... |
| ρl | 1028.30 | kg/m3 | 298.15 | Density... |
| ρl | 1028.23 | kg/m3 | 298.15 | Excess ... |
| ρl | 1027.10 | kg/m3 | 298.15 | Thermod... |
| ρl | 1028.23 | kg/m3 | 298.15 | Thermod... |
| ρl | 1028.38 | kg/m3 | 298.15 | Volumet... |
| ρl | 1019.79 | kg/m3 | 298.15 | Applica... |
| ρl | 1028.55 | kg/m3 | 298.15 | Excess ... |
| ρl | 1028.30 | kg/m3 | 298.15 | Excess ... |
| ρl | 1030.45 | kg/m3 | 298.15 | Experim... |
| ρl | 1028.23 | kg/m3 | 298.15 | Thermod... |
| ρl | 1022.00 | kg/m3 | 303.00 | Densiti... |
| ρl | 1022.64 | kg/m3 | 303.15 | Thermod... |
| ρl | 1023.60 | kg/m3 | 303.15 | Volumet... |
| ρl | 1023.46 | kg/m3 | 303.15 | Thermod... |
| ρl | 1023.93 | kg/m3 | 303.15 | Volumet... |
| ρl | 1023.40 | kg/m3 | 303.15 | Excess ... |
| ρl | 1015.48 | kg/m3 | 303.15 | Applica... |
| ρl | 1023.46 | kg/m3 | 303.15 | Thermod... |
| ρl | 1023.92 | kg/m3 | 303.15 | Volumet... |
| ρl | 1023.50 | kg/m3 | 303.15 | Excess ... |
| ρl | 1023.49 | kg/m3 | 303.15 | Excess ... |
| ρl | 1018.00 | kg/m3 | 308.00 | Densiti... |
| ρl | 1019.46 | kg/m3 | 308.15 | Volumet... |
| ρl | 1019.46 | kg/m3 | 308.15 | Volumet... |
| ρl | 1018.66 | kg/m3 | 308.15 | Thermod... |
| ρl | 1019.49 | kg/m3 | 308.15 | Volumet... |
| ρl | 1019.03 | kg/m3 | 308.15 | Thermod... |
| ρl | 1018.18 | kg/m3 | 308.15 | Thermod... |
| ρl | 1018.66 | kg/m3 | 308.15 | Thermod... |
| ρl | 1013.72 | kg/m3 | 313.15 | Thermod... |
| ρl | 1015.00 | kg/m3 | 313.15 | Volumet... |
| ρl | 1015.00 | kg/m3 | 313.15 | Volumet... |
| ρl | 1014.74 | kg/m3 | 313.15 | Volumet... |
| ρl | 1010.20 | kg/m3 | 318.15 | Volumet... |
| ρl | 1010.53 | kg/m3 | 318.15 | Volumet... |
| ρl | 1009.25 | kg/m3 | 318.15 | Thermod... |
| ρl | 1010.53 | kg/m3 | 318.15 | Volumet... |
| ρl | 1005.89 | kg/m3 | 323.15 | Volumet... |
| ρl | 1006.06 | kg/m3 | 323.15 | Volumet... |
| ρl | 1006.06 | kg/m3 | 323.15 | Volumet... |
| ρl | 1004.79 | kg/m3 | 323.15 | Thermod... |
| csound,fluid | [1478.00; 1565.52] | m/s | [293.15; 318.15] |
|
| csound,fluid | 1565.52 | m/s | 293.15 | Thermod... |
| csound,fluid | 1531.45 | m/s | 298.15 | Isentro... |
| csound,fluid | 1546.02 | m/s | 298.15 | Thermod... |
| csound,fluid | 1546.00 | m/s | 298.15 | Thermod... |
| csound,fluid | 1552.80 | m/s | 303.15 | Densiti... |
| csound,fluid | 1527.24 | m/s | 303.15 | Thermod... |
| csound,fluid | 1526.40 | m/s | 308.15 | Densiti... |
| csound,fluid | 1508.00 | m/s | 308.15 | Thermod... |
| csound,fluid | 1507.41 | m/s | 308.15 | Thermod... |
| csound,fluid | 1501.00 | m/s | 313.15 | Densiti... |
| csound,fluid | 1478.00 | m/s | 318.15 | Densiti... |
| γ | [0.04; 0.04] | N/m | [277.84; 337.88] |
|
| γ | 0.04 | N/m | 277.84 | Surface... |
| γ | 0.04 | N/m | 287.80 | Surface... |
| γ | 0.04 | N/m | 293.15 | Density... |
| γ | 0.04 | N/m | 293.15 | Density... |
| γ | 0.04 | N/m | 297.81 | Surface... |
| γ | 0.04 | N/m | 298.15 | Density... |
| γ | 0.04 | N/m | 303.15 | Density... |
| γ | 0.04 | N/m | 303.15 | Density... |
| γ | 0.04 | N/m | 303.15 | Density... |
| γ | 0.04 | N/m | 307.85 | Surface... |
| γ | 0.04 | N/m | 313.15 | Density... |
| γ | 0.04 | N/m | 313.15 | Density... |
| γ | 0.04 | N/m | 313.15 | Density... |
| γ | 0.04 | N/m | 317.85 | Surface... |
| γ | 0.04 | N/m | 323.15 | Density... |
| γ | 0.04 | N/m | 323.15 | Density... |
| γ | 0.04 | N/m | 323.15 | Density... |
| γ | 0.04 | N/m | 327.89 | Surface... |
| γ | 0.04 | N/m | 337.88 | Surface... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 354.70 | K | 1.30 | NIST |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 100.00 | 1036.8 |
| 288.15 | 500.00 | 1036.9 |
| 288.15 | 1000.00 | 1037.2 |
| 288.15 | 1500.00 | 1037.4 |
| 288.15 | 2000.00 | 1037.7 |
| 288.15 | 2500.00 | 1037.9 |
| 288.15 | 3000.00 | 1038.2 |
| 288.15 | 3500.00 | 1038.4 |
| 288.15 | 4000.00 | 1038.7 |
| 288.15 | 4500.00 | 1038.9 |
| 288.15 | 5000.00 | 1039.2 |
| 288.15 | 5500.00 | 1039.4 |
| 288.15 | 6000.00 | 1039.6 |
| 288.15 | 6500.00 | 1039.9 |
| 288.15 | 7000.00 | 1040.2 |
| 288.15 | 7500.00 | 1040.4 |
| 288.15 | 8000.00 | 1040.7 |
| 288.15 | 8500.00 | 1041.0 |
| 288.15 | 9000.00 | 1041.2 |
| 288.15 | 9500.00 | 1041.4 |
| 288.15 | 10000.00 | 1041.7 |
| 288.15 | 10500.00 | 1042.0 |
| 288.15 | 11000.00 | 1042.2 |
| 288.15 | 11500.00 | 1042.5 |
| 288.15 | 12100.00 | 1042.7 |
| 288.15 | 12500.00 | 1042.9 |
| 288.15 | 13000.00 | 1043.1 |
| 288.15 | 13500.00 | 1043.4 |
| 288.15 | 14000.00 | 1043.6 |
| 288.15 | 14500.00 | 1043.8 |
| 288.15 | 15000.00 | 1044.1 |
| 288.15 | 15500.00 | 1044.3 |
| 288.15 | 16000.00 | 1044.5 |
| 288.15 | 16500.00 | 1044.8 |
| 288.15 | 17000.00 | 1045.0 |
| 288.15 | 17500.00 | 1045.2 |
| 288.15 | 18000.00 | 1045.4 |
| 288.15 | 18600.00 | 1045.7 |
| 288.15 | 19000.00 | 1046.0 |
| 288.15 | 19500.00 | 1046.2 |
| 288.15 | 20000.00 | 1046.4 |
| 298.15 | 100.00 | 1028.0 |
| 298.15 | 500.00 | 1028.1 |
| 298.15 | 1000.00 | 1028.4 |
| 298.15 | 1500.00 | 1028.7 |
| 298.15 | 2000.00 | 1028.9 |
| 298.15 | 2500.00 | 1029.2 |
| 298.15 | 3000.00 | 1029.4 |
| 298.15 | 3500.00 | 1029.7 |
| 298.15 | 4000.00 | 1030.0 |
| 298.15 | 4500.00 | 1030.2 |
| 298.15 | 5000.00 | 1030.5 |
| 298.15 | 5500.00 | 1030.7 |
| 298.15 | 5900.00 | 1031.0 |
| 298.15 | 6500.00 | 1031.3 |
| 298.15 | 6900.00 | 1031.5 |
| 298.15 | 7500.00 | 1031.8 |
| 298.15 | 8000.00 | 1032.0 |
| 298.15 | 8500.00 | 1032.3 |
| 298.15 | 9000.00 | 1032.5 |
| 298.15 | 9600.00 | 1032.9 |
| 298.15 | 10000.00 | 1033.1 |
| 298.15 | 10500.00 | 1033.3 |
| 298.15 | 11000.00 | 1033.6 |
| 298.15 | 11500.00 | 1033.8 |
| 298.15 | 12000.00 | 1034.1 |
| 298.15 | 12500.00 | 1034.3 |
| 298.15 | 13000.00 | 1034.6 |
| 298.15 | 13500.00 | 1034.8 |
| 298.15 | 14000.00 | 1035.1 |
| 298.15 | 14400.00 | 1035.3 |
| 298.15 | 14900.00 | 1035.5 |
| 298.15 | 15500.00 | 1035.8 |
| 298.15 | 16000.00 | 1036.0 |
| 298.15 | 16500.00 | 1036.3 |
| 298.15 | 17000.00 | 1036.5 |
| 298.15 | 17500.00 | 1036.7 |
| 298.15 | 17900.00 | 1037.0 |
| 298.15 | 18500.00 | 1037.2 |
| 298.15 | 19000.00 | 1037.4 |
| 298.15 | 19500.00 | 1037.7 |
| 298.15 | 20000.00 | 1037.9 |
| 308.15 | 100.00 | 1019.3 |
| 308.15 | 500.00 | 1019.5 |
| 308.15 | 1000.00 | 1019.8 |
| 308.15 | 1500.00 | 1020.0 |
| 308.15 | 2000.00 | 1020.3 |
| 308.15 | 2500.00 | 1020.6 |
| 308.15 | 3000.00 | 1020.9 |
| 308.15 | 3500.00 | 1021.1 |
| 308.15 | 4000.00 | 1021.4 |
| 308.15 | 4500.00 | 1021.6 |
| 308.15 | 5000.00 | 1021.8 |
| 308.15 | 5500.00 | 1022.2 |
| 308.15 | 6000.00 | 1022.4 |
| 308.15 | 6400.00 | 1022.6 |
| 308.15 | 7100.00 | 1023.0 |
| 308.15 | 7500.00 | 1023.1 |
| 308.15 | 8100.00 | 1023.5 |
| 308.15 | 8500.00 | 1023.7 |
| 308.15 | 9000.00 | 1024.0 |
| 308.15 | 9500.00 | 1024.3 |
| 308.15 | 10000.00 | 1024.6 |
| 308.15 | 10400.00 | 1024.8 |
| 308.15 | 11100.00 | 1025.1 |
| 308.15 | 11500.00 | 1025.3 |
| 308.15 | 12000.00 | 1025.5 |
| 308.15 | 12500.00 | 1025.8 |
| 308.15 | 13000.00 | 1026.0 |
| 308.15 | 13500.00 | 1026.3 |
| 308.15 | 14000.00 | 1026.5 |
| 308.15 | 14500.00 | 1026.8 |
| 308.15 | 15000.00 | 1027.0 |
| 308.15 | 15500.00 | 1027.3 |
| 308.15 | 16000.00 | 1027.5 |
| 308.15 | 16500.00 | 1027.7 |
| 308.15 | 17000.00 | 1028.0 |
| 308.15 | 17500.00 | 1028.3 |
| 308.15 | 18000.00 | 1028.5 |
| 308.15 | 18500.00 | 1028.7 |
| 308.15 | 19000.00 | 1029.0 |
| 308.15 | 19500.00 | 1029.2 |
| 308.15 | 20000.00 | 1029.4 |
| 318.15 | 100.00 | 1011.0 |
| 318.15 | 500.00 | 1011.1 |
| 318.15 | 1000.00 | 1011.4 |
| 318.15 | 1500.00 | 1011.7 |
| 318.15 | 2000.00 | 1012.1 |
| 318.15 | 2500.00 | 1012.4 |
| 318.15 | 3000.00 | 1012.7 |
| 318.15 | 3500.00 | 1012.9 |
| 318.15 | 4000.00 | 1013.2 |
| 318.15 | 4500.00 | 1013.5 |
| 318.15 | 5000.00 | 1013.8 |
| 318.15 | 5500.00 | 1014.0 |
| 318.15 | 6000.00 | 1014.4 |
| 318.15 | 6500.00 | 1014.6 |
| 318.15 | 7000.00 | 1014.9 |
| 318.15 | 7500.00 | 1015.2 |
| 318.15 | 8000.00 | 1015.5 |
| 318.15 | 8500.00 | 1015.8 |
| 318.15 | 9000.00 | 1016.0 |
| 318.15 | 9500.00 | 1016.3 |
| 318.15 | 10000.00 | 1016.6 |
| 318.15 | 10500.00 | 1016.9 |
| 318.15 | 11000.00 | 1017.3 |
| 318.15 | 11400.00 | 1017.6 |
| 318.15 | 12000.00 | 1017.8 |
| 318.15 | 12500.00 | 1018.0 |
| 318.15 | 12900.00 | 1018.3 |
| 318.15 | 13500.00 | 1018.5 |
| 318.15 | 14000.00 | 1018.8 |
| 318.15 | 14500.00 | 1019.1 |
| 318.15 | 15000.00 | 1019.4 |
| 318.15 | 15500.00 | 1019.7 |
| 318.15 | 16000.00 | 1019.9 |
| 318.15 | 16500.00 | 1020.2 |
| 318.15 | 17000.00 | 1020.4 |
| 318.15 | 17500.00 | 1020.7 |
| 318.15 | 18000.00 | 1021.0 |
| 318.15 | 18500.00 | 1021.3 |
| 318.15 | 19000.00 | 1021.5 |
| 318.15 | 19600.00 | 1021.9 |
| 318.15 | 20000.00 | 1022.0 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [364.05; 503.60] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.37367e+01 | |||
| Coefficient B | -3.14760e+03 | |||
| Coefficient C | -1.30008e+02 | |||
| Temperature range, min. | 364.05 | |||
| Temperature range, max. | 503.60 | |||
| Pvap | 1.33 | kPa | 364.05 | Calculated Property |
| Pvap | 3.08 | kPa | 379.56 | Calculated Property |
| Pvap | 6.43 | kPa | 395.06 | Calculated Property |
| Pvap | 12.40 | kPa | 410.57 | Calculated Property |
| Pvap | 22.32 | kPa | 426.07 | Calculated Property |
| Pvap | 37.88 | kPa | 441.58 | Calculated Property |
| Pvap | 61.15 | kPa | 457.08 | Calculated Property |
| Pvap | 94.52 | kPa | 472.59 | Calculated Property |
| Pvap | 140.71 | kPa | 488.09 | Calculated Property |
| Pvap | 202.66 | kPa | 503.60 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Pyrrolidinone, 1-methyl-.
Mixtures
- 2-Pyrrolidinone, 1-methyl- + Di-n-propyl ether
- 2-Pyrrolidinone, 1-methyl- + n-Butyl ether
- 2-Pyrrolidinone, 1-methyl- + n-Amyl ether
- 2-Pyrrolidinone, 1-methyl- + Propane, 2-methoxy-2-methyl-
- Butane, 2-methoxy-2-methyl- + 2-Pyrrolidinone, 1-methyl-
- 2-Pyrrolidinone, 1-methyl- + Butane, 2-ethoxy-2-methyl-
- 2-Pyrrolidinone, 1-methyl- + Tetrahydrofuran
- 2-Pyrrolidinone, 1-methyl- + Tetrahydropyran
- 2-Pyrrolidinone, 1-methyl- + 1,4-Dioxane
- 2-Pyrrolidinone, 1-methyl- + 1,4,7,10,13,16-Hexaoxacyclooctadecane
- Dodecane + 2-Pyrrolidinone, 1-methyl-
- 2-Pyrrolidinone, 1-methyl- + Tetradecane
- Heptadecane + 2-Pyrrolidinone, 1-methyl-
- Dodecane + 2-Pyrrolidinone, 1-methyl- + Benzene, propyl-
- 2-Pyrrolidinone, 1-methyl- + Benzene, propyl- + Tetradecane
- Heptadecane + 2-Pyrrolidinone, 1-methyl- + Benzene, propyl-
- 2-Pyrrolidinone, 1-methyl- + Phenol
- 2-Pyrrolidinone, 1-methyl- + Phenol, 3,5-dimethyl-
- 2-Pyrrolidinone, 1-methyl- + Acetic acid
- 2-Pyrrolidinone, 1-methyl- + Acetic acid + Water
Find more mixtures with 2-Pyrrolidinone, 1-methyl-.
Sources
- Crippen Method
- Dortmund Data Bank Vapor-Liquid Equilibrium Data
- (Solid + liquid) phase equilibria of binary mixtures containing N-methyl-2-pyrrolidinone and ethers at atmospheric pressure
- Liquid liquid equilibria for n-alkanes (C12, C14, C17) + propylbenzene +NMP mixtures at temperatures between 298 and 328K
- (Solid + liquid) phase equilibria and solid-compound formation in (N-methyl-2-pyrrolidinone + phenol, or 3,5-dimethylphenol)
- Thermodynamics of binary mixtures containing N-methyl-2-pyrrolidinone VLE measurements for systems with ethers Comparison with the Mod. UNIFAC (Do) and DISQUAC models Predictions for VLE, GE m, HEm and SLE?
- Isobaric vapor liquid equilibria for water + acetic acid + (N-methyl pyrrolidone or N-methyl acetamide)
- Excess volumes and excess enthalpies of N-methyl-2-pyrrolidone with branched alcohols
- Salting effect on the liquid liquid equilibria for the ternary system water +N-methyl-2-pyrrolidone + 1-pentanol
- Liquid liquid equilibria of lactam containing binary systems
- Viscometric and volumetric behaviour of binary mixtures of sulfolane and N-methylpyrrolidone with monoethanolamine and diethanolamine in the range 303 373 K
- Temperature dependences of limiting activity coefficients and Henry s law constants for N-methylpyrrolidone, pyridine, and piperidine in water
- Measurements and correlation of saturated vapor pressures of diethoxy(methyl)(o-tolyl)silane, diethoxy(methyl)(m-tolyl)silane and diethoxy(methyl)(p-tolyl)silane
- Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
- Salting-out effect of sodium, potassium, carbonate, sulfite, tartrate and thiosulfate ions on aqueous mixtures of acetonitrile or 1-methyl-2-pyrrolidone: A liquid-liquid equilibrium study
- Experimental and theoretical study of CO2 solubility in N-methyl-2-pyrrolidone (NMP)
- Vapor-liquid equilibrium measurement of1,1,1,3,3-pentafluoropropane + N,N-dimethylformamide/diethyleneglycol dimethyl ether/N-methyl-2-pyrrolidone working fluids forabsorption power cycle
- Solubilities of CO2 capture absorbents 2-ethoxyethyl ether, 2-butoxyethyl acetate and 2-(2-ethoxyethoxy)ethyl acetate
- Thermo-physical properties of ammonium-based ionic liquid + N-methyl-2-pyrrolidone mixtures at 298.15 K
- Experimental measurement and thermodynamic modeling of propylene and propane solubility in N-methyl pyrrolidone (NMP)
- Separation of benzene and thiophene with a mixture of N-methyl-2- pyrrolidinone (NMP) and ionic liquid as the entrainer
- Determination and prediction of solid-liquid phase equilibrium for quaternary system of terephthalic acid + isophthalic acid + phthalic acid + N-methyl-2-pyrrolidone at 303.15 K and 313.15 K
- Experimental measurements and modelling of volumetric properties, refractive index and viscosity of binary systems of ethyl lactate with methyl ethyl ketone, toluene and n-methyl-2-pirrolidone at 288.15 323.15 K and atmospheric pressure. New UNIFAC VISCO and ASOG VISCO interaction parameters
- Isothermal vapor-liquid equilibrium measurements and assessments of 1,1,1,3,3,3-hexafluoropropane+N,N-dimethylformamide/N-methyl-2-pyrrolidone working pairs for absorption power cycles
- Understanding ion-ion and ion-solvent interactions in aqueous solutions of NMP based protic ionic liquids through partial molar properties and DFT calculations
- Solubility of 1,1-diamino-2,2-dinitroethylene in different pure solvents and binary mixtures (dimethyl sulfoxide p water) and (N,N-dimethylformamide p water) at different temperatures
- Experimental measurement of carbon dioxide solubility in 1-methylpyrrolidin-2-one (NMP) + 1-butyl-3-methyl-1H-imidazol-3-ium tetrafluoroborate ([bmim][BF4]) mixtures using a new static-synthetic cell
- Thermodynamics of binary mixtures of N-methyl-2-pyrrolidinone and ketone. Experimental results and modelling of the solid-liquid equilibrium and vapou-liquid equilibrium. The Modified UNIFAC (Do) model characterization
- Extraction of pentylbenzene from high molar mass alkanes (C14 and C17) by N-methyl-2-pyrrolidone
- Densities and volumetric properties of N-methyl-2-pyrrolidone with aromatic hydrocarbon at different temperature
- Thermodynamic properties of binary mixtures of N-methyl-2-pyrrolidinone with cyclohexane, benzene, toluene at (303.15 to 353.15) K and atmospheric pressure
- A study of densities and volumetric properties of binary mixtures of N-methyl-2-pyrrolidone with xylene at different temperatures and atmospheric pressure
- Isentropic compressibilities of (amide + water) mixtures: A comparative study
- Excess enthalpies and isothermal (vapour + liquid) equilibria of (1-methyl-2-pyrrolidone + 1-chloroalkane or +,?-dichloroalkane) mixtures
- Thermodynamic properties of mixtures of N-methyl-2-pyrrolidinone and methanol at temperatures between 298.15 K and 343.15 K and pressures up to 60 MPa
- Application of Prigogine Flory Patterson theory to excess molar volume of mixtures of 1-butyl-3-methylimidazolium ionic liquids with N-methyl-2-pyrrolidinone
- Isobaric (vapour + liquid) equilibrium for N-methyl-2-pyrrolidone with branched alcohols
- Excess molar volumes and ultrasonic studies of N-methyl-2-pyrrolidone with ketones at T = 303.15 K
- Thermodynamic, transport, and spectroscopic studies for mixtures of isomeric butanediol and N-methyl-2-pyrrolidinone
- Thermodynamic and topological investigations of molecular interactions in binary and ternary mixtures containing 1-methyl pyrrolidin-2-one at T = 308.15 K
- Temperature dependence measurements and molecular interactions for ammonium ionic liquid with N-methyl-2-pyrrolidone
- Density, speed of sound, viscosity, refractive index and surface tension of N-methyl-2-pyrrolidone + diethanolamine (or triethanolamine) from T = (293.15 to 323.15) K
- Activity coefficients at infinite dilution of organic solutes in N-formylmorpholine and N-methylpyrrolidone from gas-liquid chromatography
- Excess molar enthalpies for [emim][BF4] + pyrrolidin-2-one or 1-methyl pyrrolidin-2-one + pyridine or water mixtures
- Solubilities of carbon dioxide in 2-methoxyethyl acetate, 1-methoxy-2-propyl acetate and 3-methoxybutyl acetate
- Excess heat capacities of (binary + ternary) mixtures containing [emim][BF4] and organic liquids
- Excess heat capacities of mixtures containing 1-methylpyrrolidin-2-one, chlorotoluenes and benzene
- Thermodynamic properties of ternary mixtures containing 1-ethyl-3-methylimidazolium tetrafluoroborate with cyclic amides and cyclopentanone or cyclohexanone at T = (293.15, 298.15, 303.15 and 308.15) K
- Volumetric and viscosimetric properties of N-methyl-2-pyrrolidone with .gamma.-butyrolactone and propylene carbonate
- Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
- Thermodynamic, excess and optical studies on the intermolecular interactions of binary liquid mixtures of imidazolium based ILs
- Determination and modeling of binary and ternary solid-liquid phase equilibrium for the systems formed by 1,8-dinitronaphthalene and 1,5-dinitronaphthalene and N-methyl-2-pyrrolidone
- Solubility determination and thermodynamic modeling of 3-methyl-4- nitrobenzoic acid in twelve organic solvents from T = (283.15-318.15) K and mixing properties of solutions
- Densities, ultrasonic speeds and refractive indices of phenetole with N-methyl-2-pyrrolidone, N,N-dimethylformamide and tetrahydrofuran binary mixtures at different temperatures
- Measurement and modelling of econazole nitrate in twelve pure organic solvents at temperatures from 278.15 K to 318.15 K
- Solubility determination and thermodynamic modelling of 3-amino-1,2,4-triazole in ten organic solvents from T = 283.15 K to T = 318.15 K and mixing properties of solutions
- Thermodynamic modelling for solubility of 5-chloro-1-methyl-4-nitroimidazole in eleven organic solvents from T = (283.15 to 318.15) K
- Solubility of 3-methyl-4-nitrobenzoic acid in binary solvent mixtures of {(1,4-dioxane, N-methyl-2-pyrrolidone, N,N-dimethylformamide) + methanol} from T = (283.15 to 318.15) K: Experimental determination and thermodynamic modelling
- Experimental solubility of diosgenin and estriol in various solvents between T = (293.2-328.2) K
- Solubility determination and thermodynamic modelling for 2-amino-4-chlorobenzoic acid in eleven organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
- Solubility of 2-nitro-p-phenylenediamine in nine pure solvents and mixture of (methanol + N-methyl-2-pyrrolidone) from T = (283.15 to 318.15) K: Determination and modelling
- Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes
- Equilibrium solubility, dissolution thermodynamics and preferential solvation of adenosine in aqueous solutions of N,N-dimethylformamide, N-methyl-2-pyrrolidone, dimethylsulfoxide and propylene glycol
- Separation of azeotrope (allyl alcohol + water): Isobaric vapour-liquid phase equilibrium measurements and extractive distillation
- Volumetric and transport properties of binary liquid mixtures with 1-ethyl-3-methylimidazolium ethyl sulfate as candidate solvents for regenerative flue gas desulfurization processes
- Equilibrium solubility, dissolution thermodynamics and preferential solvation of 6-methyl-2-thiouracil in aqueous co-solvent mixtures of methanol, N-methyl-2-pyrrolidone, N,N-dimethyl formamide and dimethylsulfoxide
- Solubilities of sulfuryl fluoride in propylene carbonate, tributyl phosphate and N-methylpyrrolidone
- Excess molar volumes and excess isentropic compressibilities of mixtures containing lactam, cyclic ethers and cyclic alkanones
- Solubility modelling and preferential solvation of adenine in solvent mixtures of (N,N-dimethylformamide, N-methyl pyrrolidone, propylene glycol and dimethyl sulfoxide) plus water
- Solubility modelling, solvent effect and preferential solvation of allopurinol in aqueous co-solvent mixtures of ethanol, isopropanol, N,N-dimethylformamide and 1-methyl-2-pyrrolidone
- Solubility modelling and thermodynamic aspect of d-aspartic acid in aqueous co-solvent mixtures of N-methyl-2-pyrrolidone, N,N-dimethylformamide, dimethyl sulfoxide and 1.4-dioxane
- Separation of azeotropic mixture (2, 2, 3, 3-Tetrafluoro-1-propanol + water) by extractive distillation: Entrainers selection and vapour-liquid equilibrium measurements
- Solubility of chloroxine in aqueous co-solvent mixtures of N,N-dimethylformamide, dimethyl sulfoxide, N-methyl-2-pyrrolidone and 1,4-dioxane: Determination, solvent effect and preferential solvation analysis
- Influence of temperature on thermophysical properties of ammonium ionic liquids with Nmethyl- 2-pyrrolidone
- Thermodynamic properties of ternary mixtures of 1-ethyl-3-methylimidazolium tetrafluoroborate with 1-methyl pyrrolidin-2-one or pyrrolidin-2-one + water
- Excess heat capacities of 1-methyl pyrrolidin-2-one and pyridine orpicolines mixtures
- Densities, Viscosities, Sound Speed, and IR Studies of N-methyl-2- pyrrolidone with Cyclohexylamine, Cyclohexanol, and Cyclohexene at different Temperatures.
- Solubility Measurement and Simulation of Rivaroxaban (Form I) in Solvent Mixtures from 273.15 to 323.15 K
- P-T-x Measurements for 1,1,1,2-Tetrafluoroethane (R134a) + N,N dimethylacetamide (DMA), and N-methyl-2-pyrrolidone (NMP)
- Measurement and Correlation of Isothermal Vapor Liquid Equilibrium of Fluoroethane + Dimethyl Ether Triethylene Glycol, 1,1-Difluoroethane + Dimethyl Ether Triethylene Glycol, and 1,1-Difluoroethane + N-Methyl-2-pyrrolidone Systems
- Solubility Measurement and Correlation for e-2,4,6,8,10,12-Hexanitro-2,4,6,8,10,12-hexaazaisowurtzitane in Five Organic Solvents at Temperatures between 283.15 and 333.15 K and Different Chloralkane + Ethyl Acetate Binary Solvents at Temperatures between 283.15 and 323.15 K
- 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
- Isothermal Vapor-Liquid Equilibria of the Absorption Working Pairs (R1234yf + NMP, R1234yf + DMETrEG) at Temperatures from 293.15 K to 353.15 K
- Solubility of Acetylene in Alcohols and Ketones
- Solubility Modeling and Solvent Effects of Allopurinol in 15 Neat Solvents
- Solubility Measurement and Thermodynamic Model Correlation and Evaluation of 2-Chloro-5-nitroaniline in 12 Pure Solvents
- Experiment and Application of the Solid-Liquid Phase Equilibrium for Ternary 2-Nitro-p-phenylenediamine + Ethyl Acetate + Isopropanol and 2-Nitro-p-phenylenediamine + 4-Nitro-o-phenylenediamine + N-Methyl-2-pyrrolidone systems
- Equilibrium Solubility of Biapenem in Different Neat and Binary Solvents: Experimental Determination and Model Correlation
- Solubility Modeling and Solvent Effect for Flubendazole in 12 Neat Solvents
- Solubility and Solution Thermodynamics of 3-Nitrophthalonitrile in 12 Neat Solvents at Temperatures from 278.15 to 323.15 K
- Solubility Determination, Modeling, and Preferential Solvation of Terephthalaldehydic Acid Dissolvend in Aqueous Solvent Mixtures of Methanol, Ethanol, Isopropanol, and N-Methyl-2-pyrrolidone
- Solid-Liquid Equilibrium of 5-Chloro-8-hydroxyquinoline and 5,7-Dichloro-8-hydroxyquinoline in Different Solvents and Mixing Properties of Solutions
- Solubility Determination and Modeling of p-Nitrobenzamide Dissolved in Twelve Neat Solvents from 283.15 to 328.15 K
- Isothermal Vapor-Liquid Equilibrium of the Absorption Working Pairs (HFC-32 + DMETrEG, HFC-32 + NMP) at Temperatures from 293.15 to 343.15 K
- Propylthiouracil Solubility in Aqueous Solutions of Ethylene Glycol, N,N-Dimethylformamide, N-Methyl-2-pyrrolidone, and Dimethylsulfoxide: Measurement and Thermodynamic Modeling
- Solubility Determination and Model Correlation of Pymetrozine and Evaluation of the Effect of Solvent Properties and Composition
- Measurement and Correlation of Solubilities of 5,5'-Dinitramino-3,3'-bi[1,2,4-triazolate] Carbohydrazide Salt (CBNT) in Various Pure Solvents and a Binary Mixture (Dimethyl Sulfoxide + Water) from 298.15 to 343.15 K
- Solubility and Solvent Effect of Acetamiprid in Thirteen Pure Solvents and Aqueous Solutions of Ethanol
- Solubility of d-Aspartic Acid in Several Neat Solvents: Determination, Modeling, and Solvent Effect Analysis
- Solubility Determination, Correlation, and Solute-Solvent Molecular Interactions of 5-Aminotetrazole in Various Pure Solvents
- Solubility, Solubility Modeling, and Antisolvent Precipitation of 1,3-Bis(9-carbazolyl)benzene in Organic Solvents
- Binary Equilibrium Solubility of Amidinothiourea in Monosolvents: Experimental Determination, Model Correlation, and Solvent Effect Analysis
- Solubility and Solvent Effect of 1-(2-Bromo-phenyl)-pyrrole-2,5-dione in 14 Pure Solvents from 278.15 to 323.15 K
- Determination and Modeling of d-Histidine Solubility in Several Pure Solvents from 293.15 to 333.15 K
- Solubility Determination of 2-Chloronicotinic Acid and Analysis of Solvent Effect
- Solubility and Solution Thermodynamics of 2,6-Dichloro-4-nitroaniline in 12 Pure Solvents at Temperatures from 278.15 to 323.15 K
- Thermodynamic Solubility and Mixing Properties of Phenformin in 14 Pure Solvents at Temperatures Ranging from 278.15 to 323.15 K
- Vapor-Liquid Equilibria and Excess Molar Enthalpies for N-Methyl-2-pyrrolidone with Chloroethanes and Chloroethenes
- Surface Tension of Pure Liquids and Binary Liquid Mixtures
- High Pressure Phase Behavior of Carbon Dioxide + 1-Methyl-2-pyrrolidinone and Carbon Dioxide + 1-Ethyl-2-pyrrolidinone Systems
- Surface Tension and Interfacial Tension of Binary Organic Liquid Mixtures
- Volumetric Properties and Viscosities for Aqueous N-Methyl-2-pyrrolidone Solutions from 25 deg C to 70 deg C
- Densities, Viscosities, Speeds of Sound, and Relative Permittivities for Water + Cyclic Amides (2-Pyrrolidinone, 1-Methyl-2-pyrrolidinone, and 1-Vinyl-2-pyrrolidinone) at Different Temperatures
- Vapor-Liquid Equilibrium for Propylene Glycol + 2-(2-Hexyloxyethoxy)ethanol and 1-Methyl-2-pyrrolidone + 1-Methoxypropan-2-ol
- Isothermal Vapor-Liquid Equilibrium and Excess Enthalpy Data for the Binary Systems Water + Sulfolane and Methanol + N-Methyl-2-pyrrolidone (NMP)
- Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
- 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
- Solubilities of 4-Carboxybenzaldehyde and 1,4-Benzenedicarboxylic Acid in N-Methyl-2-pyrrolidone in the Temperature Range from (343.2 to 468.2) K
- Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
- High-Pressure Vapor-Liquid Equilbria of Some Carbon Dioxide + Organic Binary Systems
- Measurement and Correlation of Phase Equilibria for Dodecane + sec-Butylbenzene + N-Methyl-2-pyrrolidone
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
- Liquid-Liquid Equilibria Measurements for Ternary System of Hexadecane + 1,3,5-Trimethylbenzene + N-Methyl-2-pyrrolidone
- 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
- Solubility of Sulpiride in Pure Organic Solvents between (278 and 333) K
- Density, Speed of Sound, Viscosity, Refractive Index, and Excess Volume of N-Methyl-2-pyrrolidone + Ethanol (or Water or Ethanolamine) from T = (293.15 to 323.15) K
- Density, Speed of Sound, Refractive Index, Viscosity, Surface Tension, and Excess Volume of N-Methyl-2-pyrrolidone + 1-Amino-2-propanol {or Bis(2-hydroxypropyl)amine} from T = (293.15 to 323.15) K
- Physical Properties of 1-Butyl-3-methylimidazolium Tetrafluoroborate/N-Methyl-2-pyrrolidone Mixtures and the Solubility of CO2 in the System at Elevated Pressures
- Densities and Viscosities of the Binary Mixtures of 1-Ethyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide with N-Methyl-2-pyrrolidone or Ethanol at T = (293.15 to 323.15) K
- Thermodynamic Properties and Crystal Structures of the Adductive 2,6-Naphthalenedicarboxylic Acid Crystallization with N,N-Dimethyl Acetamide and N-Methyl Pyrrolidone
- Solubility of Forms I and II of Clopidogrel Hydrogen Sulfate in Formic Acid, N-Methylpyrrolidone, and N,N-Dimethylformamide
- Density, Speed of Sound, Viscosity, Refractive Index, and Excess Volume of N-Methyl-2-pyrrolidone (NMP) + Water + Ethanol from T = (293.15 to 323.15) K
- Solubility of 2-Butyl-3-benzofuranyl 4-(2-(Diethylamino)ethoxy)-3,5-diiodophenyl Ketone Hydrochloride (Amiodarone HCl) in Ethanol + Water and N-Methyl-2-pyrrolidone + Water Mixtures at Various Temperatures
- Activity Coefficients and Excess Gibbs Energies for Binary Mixtures of N-Methyl-2-pyrrolidone with Some Substituted Ethanols
- Thermodynamic and Topological Studies of 1-Ethyl-3-methylimidazolium Tetrafluoroborate + Pyrrolidin-2-one and 1-Methyl-pyrrolidin-2-one Mixtures
- Density, Speed of Sound, and Viscosity of N-Methyl-2-pyrrolidone + Ethanolamine + Water from T = (293.15 to 323.15) K
- Isobaric Vapor Liquid Equilibria for Binary Systems Comprising 1-Chloro-2-ethylhexane, 2-Ethyl-1-hexanol, p-Xylene, and N-Methylpyrrolidone (NMP) at 40.0 kPa
- Solubility of Clonazepam and Diazepam in Polyethylene Glycol 200, Propylene Glycol, N-Methyl Pyrrolidone, Ethanol, and Water at (298.2 to 318.2) K and in Binary and Ternary Mixtures of Polyethylene Glycol 200, Propylene Glycol, and Water at 298.2 K
- Thermodynamic Properties of Ternary Mixtures Containing Ionic Liquids and Organic Solvents
- Solubilities of Octahydro-1,3,5,7-tetranitro-1,3,5,7-tetrazocine in ?-Butyrolactone + Water, Dimethylsulfoxide + Water, and N-Methyl pyrrolidone + Water
- Excess Heat Capacities for Lactam + Chlorotoluene Binary Mixtures
- Volumetric and Viscometric Behavior of Binary Systems 2-Butanol + PEG 200, + PEG 400, + Tetraethylene Glycol Dimethyl Ether, and + N-Methyl-2-pyrrolidone
- Comparative Study of the Solubilities of SO2 in Five Low Volatile Organic Solvents (Sulfolane, Ethylene Glycol, Propylene Carbonate, N-Methylimidazole, and N-Methylpyrrolidone)
- 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
- Vapor Liquid Equilibrium Data for 1-Methyl-2-Pyrrolidone + (1-Butanol or 1-Hexene or Water) Binary Mixtures
- Phase Equilibrium and Phase Diagram for the System of Benzene Dicarboxylic Acid + N-Methyl-2-pyrrolidone
- Isothermal Vapor-Liquid Equilibria of Binary Mixtures of Nitrogen with Dimethyl Sulfoxide, N-Methyl-2-pyrrolidone, and Diethylene Glycol Monobutyl Ether at Elevated Pressures
- Solubility of Sodium Cefotaxime in Different Solvents
- Solubility of Cyclotrimethylenetrinitramine (RDX) in Binary Solvent Mixtures
- Densities and Isothermal Compressibilities at Pressures up to 20 MPa of the Systems 1-Methyl-2-pyrrolidone + 1-Chloroalkane or + r,u-Dichloroalkane
- Vapor Pressures of 1-Methyl-2-pyrrolidone, 1-Methyl-azepan-2-one, and 1,2-Epoxy-3-chloropropane
- Solubility of 2-(4-Ethylbenzoyl)benzoic Acid in Eleven Organic Solvents between 279.55 K and 343.15 K
- Solubility of Dioxopromethazine Hydrochloride in Different Solvents
- Liquid Liquid Equilibria for the Quaternary Systems of Water + N-Methyl-2-pyrrolidone + 1-Hexanol + NaCl, + KCl, or + KAc
- Solubility of Terephthalic Acid in Aqueous N-Methyl Pyrrolidone and N,N-Dimethyl Acetamide Solvents at (303.2 to 363.2) K
- Densities and Viscosities of N,N-Dimethylformamide + N-Methyl-2-pyrrolidinone and + Dimethyl Sulfoxide in the Temperature Range (303.15 to 353.15) K
- Solubility of Naphthalene in Isobutyl Acetate, n-Butyric Acid, Ethyl Acetate, N-Methyl Pyrrolidone, N,N-Dimethylformamide, and Tetrahydrofuran
- Surface Tension of Aqueous Solutions of Short N-Alkyl-2-pyrrolidinones
- Molar Heat Capacity of Aqueous Sulfolane, 4-Formylmorpholine, 1-Methyl-2-pyrrolidinone, and Triethylene Glycol Dimethyl Ether Solutions from (303.15 to 353.15) K
- Solubility of Clonazepam, Diazepam, Lamotrigine, and Phenobarbital in N-Methyl-2-pyrrolidone + Water Mixtures at 298.2 K
- Solubility of 1,1-Diamino-2,2-dinitroethylene in N,N-Dimethylformamide, Dimethyl Sulfoxide, and N-Methyl-2-pyrrolidone
- Excess Molar Enthalpies and Vapor-Liquid Equilibrium for N-Methyl-2-pyrrolidone with Ketones
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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