- 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-Methylazacyclopentane-2-one
- 1-Methylpyrrolidinone
- 1-methyl-2-pyrrolidinone
- 1-methyl-2-pyrrolidone
- 1-methyl-5-pyrrolidinone
- 1-methylazacyclopentan-2-one
- 1-methylpyrrolidin-2-one
- 1-methylpyrrolidone
- 2-Pyrrolidone, 1-methyl-
- Agsolex 1
- M-Pyrol
- Methylpyrrolidone
- Micropure ultra
- N 0131
- N-Methyl-gamma-butyrolactam
- N-Methyl-«alpha»-pyrrolidinone
- N-Methyl-«alpha»-pyrrolidone
- N-Methyl-«gamma»-butyrolactam
- N-Methylpyrrolid-2-one
- N-Methylpyrrolidinone
- N-Methylpyrrolidone-(2)
- N-methyl-.alpha.-pyrrolidinone
- N-methyl-.alpha.-pyrrolidone
- N-methyl-.gamma.-butyrolactam
- N-methyl-2-pyrrolidinone
- N-methyl-2-pyrrolidone
- N-methylpyrrolidin-2-one
- N-methylpyrrolidone
- NMP
- NSC 4594
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- 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).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- εr : Dielectric Constant (Relative permittivity).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- 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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- NFPA Safety : NFPA Safety Rating.
- Pc : Critical Pressure (kPa).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : 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).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
Temperature Dependent Properties
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 |
|---|---|---|---|---|
| Cp,gas | [93.34; 354.73] | J/mol×K | [273.00; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 2.78404e+01 | |||
| Coefficient B | -4.72471e+02 | |||
| Coefficient C | 5.87002e+00 | |||
| Coefficient D | 1.56386e-04 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 93.34 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 146.92 | J/mol×K | 409.33 | Calculated Property |
| Cp,gas | 190.15 | J/mol×K | 545.67 | Calculated Property |
| Cp,gas | 224.98 | J/mol×K | 682.00 | Calculated Property |
| Cp,gas | 253.86 | J/mol×K | 818.33 | Calculated Property |
| Cp,gas | 278.58 | J/mol×K | 954.67 | Calculated Property |
| Cp,gas | 300.32 | J/mol×K | 1091.00 | Calculated Property |
| Cp,gas | 319.91 | J/mol×K | 1227.33 | Calculated Property |
| Cp,gas | 337.91 | J/mol×K | 1363.67 | Calculated Property |
| Cp,gas | 354.73 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [160.39; 260.78] | J/mol×K | [306.45; 541.35] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 2.94250e+01 | |||
| Coefficient B | 4.27360e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 306.45 | |||
| Temperature range, max. | 541.35 | |||
| Cp,liquid | 160.39 | J/mol×K | 306.45 | Calculated Property |
| Cp,liquid | 171.54 | J/mol×K | 332.55 | Calculated Property |
| Cp,liquid | 182.70 | J/mol×K | 358.65 | Calculated Property |
| Cp,liquid | 193.85 | J/mol×K | 384.75 | Calculated Property |
| Cp,liquid | 205.01 | J/mol×K | 410.85 | Calculated Property |
| Cp,liquid | 216.16 | J/mol×K | 436.95 | Calculated Property |
| Cp,liquid | 227.31 | J/mol×K | 463.05 | Calculated Property |
| Cp,liquid | 238.47 | J/mol×K | 489.15 | Calculated Property |
| Cp,liquid | 249.62 | J/mol×K | 515.25 | Calculated Property |
| Cp,liquid | 260.78 | J/mol×K | 541.35 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0059241; 0.0002931] | Pa×s | [249.15; 477.42] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -2.84450e+01 | |||
| Coefficient B | 2.40560e+03 | |||
| Coefficient C | 2.47570e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 249.15 | |||
| Temperature range, max. | 477.42 | |||
| η | 0.0059241 | Pa×s | 249.15 | Calculated Property |
| η | 0.0030862 | Pa×s | 274.51 | Calculated Property |
| η | 0.0018304 | Pa×s | 299.88 | Calculated Property |
| η | 0.0011972 | Pa×s | 325.24 | Calculated Property |
| η | 0.0008444 | Pa×s | 350.60 | Calculated Property |
| η | 0.0006318 | Pa×s | 375.97 | Calculated Property |
| η | 0.0004956 | Pa×s | 401.33 | Calculated Property |
| η | 0.0004039 | Pa×s | 426.69 | Calculated Property |
| η | 0.0003397 | Pa×s | 452.06 | Calculated Property |
| η | 0.0002931 | Pa×s | 477.42 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [56.46; 11.09] | kJ/mol | [249.15; 721.60] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 6.53320e+01 | |||
| Coefficient B | 3.47360e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 7.26000e+02 | |||
| Temperature range, min. | 249.15 | |||
| Temperature range, max. | 721.60 | |||
| ΔvapH | 56.46 | kJ/mol | 249.15 | Calculated Property |
| ΔvapH | 54.21 | kJ/mol | 301.64 | Calculated Property |
| ΔvapH | 51.78 | kJ/mol | 354.14 | Calculated Property |
| ΔvapH | 49.12 | kJ/mol | 406.63 | Calculated Property |
| ΔvapH | 46.15 | kJ/mol | 459.13 | Calculated Property |
| ΔvapH | 42.77 | kJ/mol | 511.62 | Calculated Property |
| ΔvapH | 38.79 | kJ/mol | 564.12 | Calculated Property |
| ΔvapH | 33.85 | kJ/mol | 616.61 | Calculated Property |
| ΔvapH | 26.98 | kJ/mol | 669.11 | Calculated Property |
| ΔvapH | 11.09 | kJ/mol | 721.60 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [364.05; 503.60] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| 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 |
| Pvap | [5.39e-04; 4517.96] | kPa | [249.15; 721.60] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 6.15682e+01 | |||
| Coefficient B | -8.46790e+03 | |||
| Coefficient C | -6.36220e+00 | |||
| Coefficient D | 3.22350e-18 | |||
| Coefficient E | 6.00000e+00 | |||
| Temperature range, min. | 249.15 | |||
| Temperature range, max. | 721.60 | |||
| Pvap | 5.39e-04 | kPa | 249.15 | Calculated Property |
| Pvap | 0.06 | kPa | 301.64 | Calculated Property |
| Pvap | 1.38 | kPa | 354.14 | Calculated Property |
| Pvap | 12.61 | kPa | 406.63 | Calculated Property |
| Pvap | 64.01 | kPa | 459.13 | Calculated Property |
| Pvap | 219.25 | kPa | 511.62 | Calculated Property |
| Pvap | 575.38 | kPa | 564.12 | Calculated Property |
| Pvap | 1261.63 | kPa | 616.61 | Calculated Property |
| Pvap | 2464.77 | kPa | 669.11 | Calculated Property |
| Pvap | 4517.96 | kPa | 721.60 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1064.45; 319.79] | kg/m3 | [249.15; 721.60] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 8.24493e+01 | |||
| Coefficient B | 2.57820e-01 | |||
| Coefficient C | 7.21600e+02 | |||
| Coefficient D | 2.82690e-01 | |||
| Temperature range, min. | 249.15 | |||
| Temperature range, max. | 721.60 | |||
| ρl | 1064.45 | kg/m3 | 249.15 | Calculated Property |
| ρl | 1023.35 | kg/m3 | 301.64 | Calculated Property |
| ρl | 980.19 | kg/m3 | 354.14 | Calculated Property |
| ρl | 934.48 | kg/m3 | 406.63 | Calculated Property |
| ρl | 885.47 | kg/m3 | 459.13 | Calculated Property |
| ρl | 832.02 | kg/m3 | 511.62 | Calculated Property |
| ρl | 772.15 | kg/m3 | 564.12 | Calculated Property |
| ρl | 701.85 | kg/m3 | 616.61 | Calculated Property |
| ρl | 610.23 | kg/m3 | 669.11 | Calculated Property |
| ρl | 319.79 | kg/m3 | 721.60 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.02; 0.08] | W/m×K | [477.42; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | 6.33190e-05 | |||
| Coefficient B | 1.11230e+00 | |||
| Coefficient C | 7.14730e+02 | |||
| Coefficient D | 0.00000e+00 | |||
| Temperature range, min. | 477.42 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.02 | W/m×K | 477.42 | Calculated Property |
| λgas | 0.03 | W/m×K | 535.48 | Calculated Property |
| λgas | 0.03 | W/m×K | 593.55 | Calculated Property |
| λgas | 0.04 | W/m×K | 651.61 | Calculated Property |
| λgas | 0.05 | W/m×K | 709.68 | Calculated Property |
| λgas | 0.05 | W/m×K | 767.74 | Calculated Property |
| λgas | 0.06 | W/m×K | 825.81 | Calculated Property |
| λgas | 0.07 | W/m×K | 883.87 | Calculated Property |
| λgas | 0.07 | W/m×K | 941.94 | Calculated Property |
| λgas | 0.08 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.14; 0.10] | W/m×K | [249.15; 477.42] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λliquid in W/m×K, T in K | |||
| Coefficient A | 1.88850e-01 | |||
| Coefficient B | -1.84000e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 249.15 | |||
| Temperature range, max. | 477.42 | |||
| λliquid | 0.14 | W/m×K | 249.15 | Calculated Property |
| λliquid | 0.14 | W/m×K | 274.51 | Calculated Property |
| λliquid | 0.13 | W/m×K | 299.88 | Calculated Property |
| λliquid | 0.13 | W/m×K | 325.24 | Calculated Property |
| λliquid | 0.12 | W/m×K | 350.60 | Calculated Property |
| λliquid | 0.12 | W/m×K | 375.97 | Calculated Property |
| λliquid | 0.12 | W/m×K | 401.33 | Calculated Property |
| λliquid | 0.11 | W/m×K | 426.69 | Calculated Property |
| λliquid | 0.11 | W/m×K | 452.06 | Calculated Property |
| λliquid | 0.10 | W/m×K | 477.42 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Pyrrolidinone, 1-methyl-.
Mixtures
- 2-Pyrrolidinone, 1-methyl- + Acetone
- 1,2-Ethanediol + 2-Pyrrolidinone, 1-methyl-
- Ethanol + 2-Pyrrolidinone, 1-methyl-
- 2-Pyrrolidinone, 1-methyl- + Ethyl Acetate + Water
- Benzene + 1-Hexene + 2-Pyrrolidinone, 1-methyl-
- Benzene + n-Hexane + 2-Pyrrolidinone, 1-methyl- + Cyclohexane
- Benzene + 2-Pyrrolidinone, 1-methyl- + Cyclohexane
- Benzene + n-Hexane + 2-Pyrrolidinone, 1-methyl-
- Benzene + 2-Pyrrolidinone, 1-methyl-
- Benzene + 2-Pyrrolidinone, 1-methyl- + Water
- 2-Pyrrolidinone, 1-methyl- + 1-Butanol
- 2-Pyrrolidinone, 1-methyl- + 1-Butanol + Water
- Trichloromethane + 2-Pyrrolidinone, 1-methyl-
- n-Hexane + 2-Pyrrolidinone, 1-methyl- + Cyclohexane
- 2-Pyrrolidinone, 1-methyl- + Cyclohexane
- 2-Pyrrolidinone, 1-methyl- + Acetic acid
- 2-Pyrrolidinone, 1-methyl- + Acetic acid + Water
- n-Hexane + 2-Pyrrolidinone, 1-methyl-
- 2-Propanol + 2-Pyrrolidinone, 1-methyl-
- 1-Hexene + 2-Pyrrolidinone, 1-methyl-
Find more mixtures with 2-Pyrrolidinone, 1-methyl-.
Sources
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 11 ChEDL chemicals 1.5.2, from Ambrose, D.; Tsonopoulos, C.; Nikitin, E. D. Vapor-Liquid Critical Properties of Elements and Compounds. 11. Organic Compounds Containing B + O; Halogens + N, + O, + O + S, + S, + Si; N + O; and O + S, + Si. J. Chem. Eng. Data 2009, 54, 669-689.
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- 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
- Enthalpies of solution, partial molar volumes and isentropic compressibilities of polycyclic aromatic hydrocarbons in 1-methyl-2-pyrrolidone at 298.15K
- 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
- Dissolution Properties of Ammonium Dipicrylamide in Dimethyl Sulfoxide and N-methl Pyrrolidone
- 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
- Solvation of N-methyl-2-pyrrolidone and N,N-dimethylpropanamide in cyclohexane, heptane, n-alkan-1-ols(C1-C4) and water at 298.15K
- Densities, Viscosities, Sound Speed, and IR Studies of N-methyl-2- pyrrolidone with Cyclohexylamine, Cyclohexanol, and Cyclohexene at different Temperatures.
- Thermochemistry of hydrogen bonding of linear and cyclic amides inproton acceptors media
- 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 Terephthaldialdehyde in N-Methyl-2-pyrrolidone and Solid-Liquid Phase Equilibrium for Ternary Systems of Terephthalic Acid + Terephthaldialdehyde + N,N-Dimethylformamide/N-Methyl-2-pyrrolidone
- 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
- Dissolution Properties of 1,2,4-Triazole Nitrate in N-Methyl Pyrrolidone
- 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
- NCMS SOLV-DB
- The Yaws Handbook of Vapor Pressure
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