- InChI
- InChI=1S/CH3NO2/c1-2(3)4/h1H3
- InChI Key
- LYGJENNIWJXYER-UHFFFAOYSA-N
- Formula
- CH3NO2
- SMILES
- C[N+](=O)[O-]
- Molecular Weight1
- 61.04
- CAS
- 75-52-5
- Other Names
-
- CH3NO2
- NM
- NSC 428
- Nitrocarbol
- Nitrometan
- Nitromethane
- UN 1261
- nitromethane [NM]
- 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).
- EA : Electron affinity (eV).
- LFL : Lower Flammability Limit (% in Air).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- Rg : Radius of Gyration.
- 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).
- ν : Kinematic viscosity (m2/s).
- 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).
- 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.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- ΔvapS : Entropy of vaporization at a given temperature (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3100 | KDB | |
| PAff | 754.60 | kJ/mol | NIST |
| Tig | 691.48 | K | KDB |
| BasG | 721.60 | kJ/mol | NIST |
| ΔcH°liquid | [-733.25; -703.00] | kJ/mol |
|
| ΔcH°liquid | -709.60 ± 0.40 | kJ/mol | NIST |
| ΔcH°liquid | -703.00 ± 1.00 | kJ/mol | NIST |
| ΔcH°liquid | -709.15 ± 0.59 | kJ/mol | NIST |
| ΔcH°liquid | -733.25 ± 0.75 | kJ/mol | NIST |
| ΔcH°liquid | -709.20 | kJ/mol | NIST |
| μ | 3.10 | debye | KDB |
| EA | [0.01; 0.96] | eV |
|
| EA | 0.17 ± 0.01 | eV | NIST |
| EA | 0.26 ± 0.08 | eV | NIST |
| EA | 0.01 | eV | NIST |
| EA | 0.50 ± 0.02 | eV | NIST |
| EA | 0.49 ± 0.11 | eV | NIST |
| EA | 0.45 ± 0.05 | eV | NIST |
| EA | 0.44 ± 0.20 | eV | NIST |
| EA | Outlier 0.96 ± 0.01 | eV | NIST |
| LFL | 7.30 | % in Air | KDB |
| Tflash,cc | 316.48 | K | KDB |
| Tflash,oc | 308.15 | K | KDB |
| ΔfG° | -6.95 | kJ/mol | KDB |
| Rg | 2.3060 | KDB | |
| ΔfH°gas | [-81.00; -74.78] | kJ/mol |
|
| ΔfH°gas | -74.78 | kJ/mol | KDB |
| ΔfH°gas | -81.00 ± 1.00 | kJ/mol | NIST |
| ΔfH°liquid | [-113.10; -89.04] | kJ/mol |
|
| ΔfH°liquid | -113.00 ± 0.40 | kJ/mol | NIST |
| ΔfH°liquid | -113.10 ± 0.63 | kJ/mol | NIST |
| ΔfH°liquid | -89.04 ± 0.75 | kJ/mol | NIST |
| ΔfusH° | 9.71 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [34.50; 38.37] | kJ/mol |
|
| ΔvapH° | 38.36 | kJ/mol | NIST |
| ΔvapH° | 37.20 | kJ/mol | NIST |
| ΔvapH° | 38.37 | kJ/mol | NIST |
| ΔvapH° | 38.00 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 38.00 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 38.30 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | Outlier 34.50 ± 0.08 | kJ/mol | NIST |
| IE | [10.70; 11.80] | eV |
|
| IE | 11.08 ± 0.04 | eV | NIST |
| IE | 11.07 | eV | NIST |
| IE | 11.10 ± 0.05 | eV | NIST |
| IE | Outlier 10.70 | eV | NIST |
| IE | 11.12 | eV | NIST |
| IE | 11.05 | eV | NIST |
| IE | 11.28 ± 0.08 | eV | NIST |
| IE | 11.28 | eV | NIST |
| IE | 11.10 | eV | NIST |
| IE | 11.28 ± 0.08 | eV | NIST |
| IE | 11.07 ± 0.01 | eV | NIST |
| IE | 11.04 ± 0.02 | eV | NIST |
| IE | 11.23 ± 0.01 | eV | NIST |
| IE | 11.13 ± 0.01 | eV | NIST |
| IE | 11.08 ± 0.03 | eV | NIST |
| IE | 11.29 | eV | NIST |
| IE | 11.47 | eV | NIST |
| IE | 11.31 | eV | NIST |
| IE | Outlier 11.80 | eV | NIST |
| IE | 11.29 | eV | NIST |
| IE | 11.31 ± 0.01 | eV | NIST |
| log10WS | [0.26; 0.26] |
|
|
| log10WS | 0.26 | Aq. Sol... | |
| log10WS | 0.26 | Estimat... | |
| logPoct/wat | -0.107 | Crippen Calculated Property | |
| McVol | 42.370 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 1 | KDB | |
| NFPA Safety | 4 | KDB | |
| Pc | [5870.00; 6310.00] | kPa |
|
| Pc | 5870.00 | kPa | KDB |
| Pc | 5870.00 ± 58.65 | kPa | NIST |
| Pc | 6310.00 ± 103.42 | kPa | NIST |
| ρc | 352.20 ± 3.05 | kg/m3 | NIST |
| Inp | [487.00; 565.00] |
|
|
| Inp | 527.85 | NIST | |
| Inp | 528.16 | NIST | |
| Inp | 528.60 | NIST | |
| Inp | 531.15 | NIST | |
| Inp | 530.05 | NIST | |
| Inp | 529.26 | NIST | |
| Inp | 528.66 | NIST | |
| Inp | 528.15 | NIST | |
| Inp | 527.88 | NIST | |
| Inp | 527.75 | NIST | |
| Inp | 526.13 | NIST | |
| Inp | 556.00 | NIST | |
| Inp | 500.00 | NIST | |
| Inp | 500.00 | NIST | |
| Inp | 536.00 | NIST | |
| Inp | 565.00 | NIST | |
| Inp | 565.00 | NIST | |
| Inp | 565.00 | NIST | |
| Inp | 512.00 | NIST | |
| Inp | 543.60 | NIST | |
| Inp | 531.00 | NIST | |
| Inp | 521.00 | NIST | |
| Inp | Outlier 487.00 | NIST | |
| Inp | 526.00 | NIST | |
| Inp | 531.00 | NIST | |
| Inp | 521.00 | NIST | |
| Inp | 526.00 | NIST | |
| Inp | 565.00 | NIST | |
| Inp | 536.00 | NIST | |
| Inp | 565.00 | NIST | |
| Inp | 531.00 | NIST | |
| I | [1154.00; 1190.20] |
|
|
| I | 1187.80 | NIST | |
| I | 1188.50 | NIST | |
| I | 1190.20 | NIST | |
| I | 1178.50 | NIST | |
| I | 1179.20 | NIST | |
| I | 1180.60 | NIST | |
| I | 1182.90 | NIST | |
| I | 1184.70 | NIST | |
| I | 1172.00 | NIST | |
| I | 1159.00 | NIST | |
| I | 1160.90 | NIST | |
| I | 1177.00 | NIST | |
| I | 1177.00 | NIST | |
| I | Outlier 1154.00 | NIST | |
| I | 1159.00 | NIST | |
| I | 1187.80 | NIST | |
| I | 1180.60 | NIST | |
| S°liquid | 171.75 | J/mol×K | NIST |
| Tboil | [373.13; 374.85] | K |
|
| Tboil | 374.34 | K | KDB |
| Tboil | 373.35 ± 0.50 | K | NIST |
| Tboil | 373.35 ± 0.50 | K | NIST |
| Tboil | 374.40 | K | NIST |
| Tboil | 374.43 ± 0.30 | K | NIST |
| Tboil | 374.17 ± 0.25 | K | NIST |
| Tboil | 374.35 ± 0.05 | K | NIST |
| Tboil | 374.85 ± 0.30 | K | NIST |
| Tboil | 374.22 ± 0.08 | K | NIST |
| Tboil | Outlier 373.13 ± 0.07 | K | NIST |
| Tboil | 374.40 ± 0.50 | K | NIST |
| Tboil | 374.15 ± 1.50 | K | NIST |
| Tboil | 374.40 ± 0.50 | K | NIST |
| Tboil | 374.25 ± 0.30 | K | NIST |
| Tboil | 374.30 ± 0.50 | K | NIST |
| Tboil | 374.17 ± 0.30 | K | NIST |
| Tboil | 374.15 ± 1.00 | K | NIST |
| Tboil | 374.15 ± 2.00 | K | NIST |
| Tc | [588.00; 588.00] | K |
|
| Tc | 588.00 | K | KDB |
| Tc | 588.00 | K | NIST |
| Tc | 588.00 ± 3.00 | K | NIST |
| Tfus | [243.11; 244.60] | K |
|
| Tfus | 244.32 | K | Aq. Sol... |
| Tfus | 244.60 | K | KDB |
| Tfus | 243.36 | K | Efficie... |
| Tfus | 244.60 ± 0.05 | K | NIST |
| Tfus | 244.55 ± 0.40 | K | NIST |
| Tfus | 243.11 ± 0.05 | K | NIST |
| Tfus | 244.00 ± 2.00 | K | NIST |
| Tfus | 243.95 ± 0.30 | K | NIST |
| Ttriple | 244.77 ± 0.02 | K | NIST |
| Vc | 0.173 | m3/kmol | KDB |
| Zc | 0.2077160 | KDB | |
| Zra | 0.23 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [67.43; 90.47] | J/mol×K | [374.12; 587.84] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 70 75 80 85 90 400 450 500 550 | ||||
| Cp,gas | 67.43 | J/mol×K | 374.12 | Joback Calculated Property |
| Cp,gas | 71.78 | J/mol×K | 409.74 | Joback Calculated Property |
| Cp,gas | 75.92 | J/mol×K | 445.36 | Joback Calculated Property |
| Cp,gas | 79.86 | J/mol×K | 480.98 | Joback Calculated Property |
| Cp,gas | 83.59 | J/mol×K | 516.60 | Joback Calculated Property |
| Cp,gas | 87.12 | J/mol×K | 552.22 | Joback Calculated Property |
| Cp,gas | 90.47 | J/mol×K | 587.84 | Joback Calculated Property |
| Cp,liquid | [100.00; 108.80] | J/mol×K | [293.15; 318.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 100 102 104 106 108 300 310 | ||||
| Cp,liquid | 106.60 | J/mol×K | 293.15 | Excess ... |
| Cp,liquid | 100.00 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 106.90 | J/mol×K | 298.15 | Excess ... |
| Cp,liquid | 105.98 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 107.30 | J/mol×K | 303.15 | Excess ... |
| Cp,liquid | 106.22 | J/mol×K | 308.00 | NIST |
| Cp,liquid | 107.70 | J/mol×K | 308.15 | Excess ... |
| Cp,liquid | 108.80 | J/mol×K | 313.00 | NIST |
| Cp,liquid | 108.20 | J/mol×K | 313.15 | Excess ... |
| Cp,liquid | 108.60 | J/mol×K | 318.15 | Excess ... |
| ΔfusH | [9.70; 9.70] | kJ/mol | [244.77; 244.80] |
|
| ΔfusH | 9.70 | kJ/mol | 244.77 | NIST |
| ΔfusH | 9.70 | kJ/mol | 244.80 | NIST |
| ΔfusH | 9.70 | kJ/mol | 244.80 | NIST |
| ΔvapH | [33.99; 38.27] | kJ/mol | [298.15; 440.50] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 34 35 36 37 38 300 350 400 | ||||
| ΔvapH | 38.27 | kJ/mol | 298.15 | NIST |
| ΔvapH | 37.20 ± 0.10 | kJ/mol | 318.00 | NIST |
| ΔvapH | 36.30 ± 0.10 | kJ/mol | 335.00 | NIST |
| ΔvapH | 35.20 ± 0.10 | kJ/mol | 353.00 | NIST |
| ΔvapH | 36.80 | kJ/mol | 369.00 | NIST |
| ΔvapH | 34.41 | kJ/mol | 374.00 | KDB |
| ΔvapH | 34.00 ± 0.10 | kJ/mol | 374.00 | NIST |
| ΔvapH | 33.99 | kJ/mol | 374.40 | NIST |
| ΔvapH | 35.20 | kJ/mol | 440.50 | NIST |
| ν | [0.0000005; 0.0000006] | m2/s | [293.15; 308.15] |
|
|
T(K) Kinematic viscosity (m2/s) 4.80e-7 5.00e-7 5.20e-7 5.40e-7 5.60e-7 5.80e-7 6.00e-7 295 300 305 | ||||
| ν | 0.0000006 | m2/s | 293.15 | Densiti... |
| ν | 0.0000006 | m2/s | 295.15 | Densiti... |
| ν | 0.0000006 | m2/s | 298.15 | Densiti... |
| ν | 0.0000005 | m2/s | 300.15 | Densiti... |
| ν | 0.0000005 | m2/s | 303.15 | Densiti... |
| ν | 0.0000005 | m2/s | 305.15 | Densiti... |
| ν | 0.0000005 | m2/s | 308.15 | Densiti... |
| n0 | [1.37930; 1.37990] | [298.15; 298.15] |
|
|
|
T(K) Refractive Index 1.38 1.38 1.38 1.38 1.38 1.38 1.38 | ||||
| n0 | 1.37956 | 298.15 | Isother... | |
| n0 | 1.37960 | 298.15 | Density... | |
| n0 | 1.37990 | 298.15 | Physico... | |
| n0 | 1.37930 | 298.15 | Isother... | |
| n0 | 1.37940 | 298.15 | Isother... | |
| ρl | [1103.39; 1158.25] | kg/m3 | [278.15; 318.15] |
|
|
T(K) Liquid Density (kg/m3) 1100 1110 1120 1130 1140 1150 1160 280 290 300 310 | ||||
| ρl | 1158.25 | kg/m3 | 278.15 | Water a... |
| ρl | 1144.75 | kg/m3 | 288.15 | Water a... |
| ρl | 1138.00 | kg/m3 | 293.00 | KDB |
| ρl | 1140.20 | kg/m3 | 293.15 | Density... |
| ρl | 1131.10 | kg/m3 | 298.15 | Asymmet... |
| ρl | 1133.40 | kg/m3 | 298.15 | Density... |
| ρl | 1131.18 | kg/m3 | 298.15 | Water a... |
| ρl | 1130.15 | kg/m3 | 298.15 | Ionic s... |
| ρl | 1130.15 | kg/m3 | 298.15 | Explora... |
| ρl | 1130.90 | kg/m3 | 298.15 | Volumet... |
| ρl | 1130.86 | kg/m3 | 298.15 | Volumet... |
| ρl | 1130.76 | kg/m3 | 298.15 | Volumet... |
| ρl | 1130.95 | kg/m3 | 298.15 | Volumet... |
| ρl | 1130.91 | kg/m3 | 298.15 | Volumet... |
| ρl | 1130.90 | kg/m3 | 298.15 | Volumet... |
| ρl | 1126.60 | kg/m3 | 303.15 | Density... |
| ρl | 1117.29 | kg/m3 | 308.15 | Volumet... |
| ρl | 1117.28 | kg/m3 | 308.15 | Volumet... |
| ρl | 1117.53 | kg/m3 | 308.15 | Water a... |
| ρl | 1119.70 | kg/m3 | 308.15 | Density... |
| ρl | 1117.32 | kg/m3 | 308.15 | Volumet... |
| ρl | 1117.23 | kg/m3 | 308.15 | Volumet... |
| ρl | 1117.24 | kg/m3 | 308.15 | Volumet... |
| ρl | 1117.14 | kg/m3 | 308.15 | Volumet... |
| ρl | 1112.90 | kg/m3 | 313.15 | Density... |
| ρl | 1103.55 | kg/m3 | 318.15 | Volumet... |
| ρl | 1103.48 | kg/m3 | 318.15 | Volumet... |
| ρl | 1103.79 | kg/m3 | 318.15 | Water a... |
| ρl | 1103.39 | kg/m3 | 318.15 | Volumet... |
| ρl | 1103.57 | kg/m3 | 318.15 | Volumet... |
| ρl | 1103.50 | kg/m3 | 318.15 | Volumet... |
| ρl | 1103.53 | kg/m3 | 318.15 | Volumet... |
| ρl | 1106.00 | kg/m3 | 318.15 | Density... |
| ΔfusS | 39.64 | J/mol×K | 244.77 | NIST |
| csound,fluid | [1242.39; 1321.74] | m/s | [298.15; 318.15] |
|
|
T(K) Speed of sound in fluid (m/s) 1240 1260 1280 1300 1320 300 305 310 315 | ||||
| csound,fluid | 1321.26 | m/s | 298.15 | Speeds ... |
| csound,fluid | 1321.74 | m/s | 298.15 | Speeds ... |
| csound,fluid | 1321.50 | m/s | 298.15 | Speeds ... |
| csound,fluid | 1321.16 | m/s | 298.15 | Speeds ... |
| csound,fluid | 1321.49 | m/s | 298.15 | Speeds ... |
| csound,fluid | 1321.20 | m/s | 298.15 | Speeds ... |
| csound,fluid | 1321.62 | m/s | 298.15 | Speeds ... |
| csound,fluid | 1321.18 | m/s | 298.15 | Speeds ... |
| csound,fluid | 1321.33 | m/s | 298.15 | Speeds ... |
| csound,fluid | 1281.75 | m/s | 308.15 | Speeds ... |
| csound,fluid | 1281.77 | m/s | 308.15 | Speeds ... |
| csound,fluid | 1282.03 | m/s | 308.15 | Speeds ... |
| csound,fluid | 1281.90 | m/s | 308.15 | Speeds ... |
| csound,fluid | 1281.87 | m/s | 308.15 | Speeds ... |
| csound,fluid | 1281.78 | m/s | 308.15 | Speeds ... |
| csound,fluid | 1282.12 | m/s | 308.15 | Speeds ... |
| csound,fluid | 1242.49 | m/s | 318.15 | Speeds ... |
| csound,fluid | 1242.50 | m/s | 318.15 | Speeds ... |
| csound,fluid | 1242.45 | m/s | 318.15 | Speeds ... |
| csound,fluid | 1242.46 | m/s | 318.15 | Speeds ... |
| csound,fluid | 1242.76 | m/s | 318.15 | Speeds ... |
| csound,fluid | 1242.47 | m/s | 318.15 | Speeds ... |
| csound,fluid | 1242.39 | m/s | 318.15 | Speeds ... |
| csound,fluid | 1242.60 | m/s | 318.15 | Speeds ... |
| γ | 0.04 | N/m | 293.20 | KDB |
| ΔvapS | 128.36 | J/mol×K | 298.15 | NIST |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 100.00 | 298.15 | 1130.15 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.14; 6410.96] | kPa | [244.60; 588.15] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.53705e+01 | |||
| Coefficient B | -3.66507e+03 | |||
| Coefficient C | -3.32310e+01 | |||
| Temperature range, min. | 244.60 | |||
| Temperature range, max. | 588.15 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 7000 300 400 500 | ||||
| Pvap | 0.14 | kPa | 244.60 | Calculated Property |
| Pvap | 1.98 | kPa | 282.77 | Calculated Property |
| Pvap | 13.90 | kPa | 320.94 | Calculated Property |
| Pvap | 61.80 | kPa | 359.12 | Calculated Property |
| Pvap | 200.98 | kPa | 397.29 | Calculated Property |
| Pvap | 522.48 | kPa | 435.46 | Calculated Property |
| Pvap | 1150.98 | kPa | 473.63 | Calculated Property |
| Pvap | 2235.35 | kPa | 511.81 | Calculated Property |
| Pvap | 3935.82 | kPa | 549.98 | Calculated Property |
| Pvap | 6410.96 | kPa | 588.15 | Calculated Property |
| Pvap | [0.14; 6066.19] | kPa | [244.60; 588.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 8.31812e+01 | |||
| Coefficient B | -7.21717e+03 | |||
| Coefficient C | -1.02078e+01 | |||
| Coefficient D | 8.36912e-06 | |||
| Temperature range, min. | 244.60 | |||
| Temperature range, max. | 588.15 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 300 400 500 | ||||
| Pvap | 0.14 | kPa | 244.60 | Calculated Property |
| Pvap | 2.03 | kPa | 282.77 | Calculated Property |
| Pvap | 14.07 | kPa | 320.94 | Calculated Property |
| Pvap | 60.62 | kPa | 359.12 | Calculated Property |
| Pvap | 189.81 | kPa | 397.29 | Calculated Property |
| Pvap | 477.23 | kPa | 435.46 | Calculated Property |
| Pvap | 1029.09 | kPa | 473.63 | Calculated Property |
| Pvap | 1991.26 | kPa | 511.81 | Calculated Property |
| Pvap | 3569.52 | kPa | 549.98 | Calculated Property |
| Pvap | 6066.19 | kPa | 588.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Methane, nitro-.
Mixtures
- Tetrabutylammonium hexafluorophosphate + Methane, nitro-
- Pentane, 1-chloro- + Methane, nitro-
- n-Butyl ether + Methane, nitro-
- Hexane, 1-ethoxy- + Methane, nitro-
- Pentane, 1-propoxy- + Methane, nitro-
- Methane, nitro- + Ethane, 1,1,2,2-tetrachloro-
- Ethane, 1,1,1-trichloro- + Methane, nitro-
- Trichloromethane + Methane, nitro-
- Ethane, 1,2-dichloro- + Methane, nitro-
- Methane, nitro- + Propane, 1,3-dichloro-
- Butane, 1,4-dichloro- + Methane, nitro-
- Butane, 1-chloro- + Methane, nitro-
- Methane, nitro- + Water
- Benzene, nitro- + Methane, nitro-
- Acetic acid, pentyl ester + Methane, nitro-
- Methane, nitro- + 3-Pentanol
- 1-Pentanol + Methane, nitro-
- Methane, nitro- + Tetrabutylammonium tetrafluoroborate
- Carbon dioxide + Methane, nitro-
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Isothermal vapour liquid equilibria for 1,2-dichloroethane + nitromethane and + nitroethane binary systems at temperatures between 333.15 and 353.15K
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Ionic solvation of tetrabutylammonium hexafluorophosphate in pure nitromethane, 1, 3-dioxolane and nitrobenzene: A comparative physicochemical study
- Isothermal vapor liquid equilibria and excess Gibbs free energies in some binary nitroalkane + chloroalkane mixtures at temperatures from 298.15 K to 318.15 K
- Liquid-liquid equilibrium in binary systems of isomeric C8 aliphatic monoethers with nitromethane
- Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
- Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
- Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
- Density and refractive index in mixtures of ionic liquids and organic solvents: Correlations and predictions
- Efficient determination of crystallisation and melting points at low cooling and heating rates with novel computer controlled equipment
- Excess molar properties for binary systems of alkylimidazolium-based ionic liquids + nitromethane. Experimental results and ERAS-model calculations
- Water as a solute in nitromethane: Effect of H2O-D2O isotope substitution on the solution volumetric properties between 278.15 K and 318.15 K
- Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
- Solubilities of some organic solutes in 1-ethyl-3-methylimidazolium acetate. Chromatographic measurements and predictions from COSMO-RS
- Physico-chemical studies of sodium tetraphenylborate and tetrabutylammonium tetraphenylborate in pure nitrobenzene and nitromethane and their binaries probed by conductometry, refractometry and FT-IR spectroscopy
- Isothermal (vapour + liquid) equilibria for (nitromethane or nitroethane + 1,4-dichlorobutane) binary systems at temperatures between (343.15 and 363.15) K
- Henry s constants and activity coefficients of some organic solutes in 1-butyl,3-methylimidazolium hydrogen sulfate and in 1-methyl,3-trimethylsilylmethylimidazolium chloride
- Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
- Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
- Enthalpies of formation of nitromethane and nitrobenzene: New experiments vs. quantum chemical calculations
- Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
- Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
- Asymmetric liquid-liquid criticality in the ideal volumetric mixing approximation
- Exploration of Solvation Consequence of Ionic Liquid [Bu4PCH3SO3] in Various Solvent Systems by Conductance and FTIR Study
- High-Pressure Vapor-Liquid Equilbria of Some Carbon Dioxide + Organic Binary Systems
- Densities, Viscosities, and Speeds of Sound of the Nitromethane + 1-Pentanol System near the Critical Demixing Temperature: Effect of Deuterium Substitution
- Volumetric Properties for (Ionic Liquid + Methanol or Ethanol or 1-Propanol + Nitromethane) at 298.15 K and Atmospheric Pressure
- Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
- Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
- Isothermal Vapor Liquid Equilibria for Nitromethane and Nitroethane + 1,3-Dichloropropane Binary Systems at Temperatures between (343.15 and 363.15) K
- Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
- Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
- Activity Coefficients at Infinite Dilution for Organic Compounds Dissolved in 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Having Six-, Eight-, and Ten-Carbon Alkyl Chains
- Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
- Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
- Role of Anions (Tetrafluoroborate, Perchlorate) of Tetrabutylammonium Salts in Determining Solvation Effects Prevailing in Industrially Essential Solvents Probed by Conductance and FT-IR Spectra
- Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
- Density and Heat Capacity as a Function of Temperature for Binary Mixtures of 1-Butyl-3-methylpyridinium Tetrafluoroborate + Water, + Ethanol, and + Nitromethane
- Densities and Excess Enthalpies for Ionic Liquids + Ethanol or + Nitromethane
- Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
- Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
- Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
- Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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