- InChI
- InChI=1S/C6H5NO2/c8-7(9)6-4-2-1-3-5-6/h1-5H
- InChI Key
- LQNUZADURLCDLV-UHFFFAOYSA-N
- Formula
- C6H5NO2
- SMILES
- O=[N+]([O-])c1ccccc1
- Molecular Weight1
- 123.11
- CAS
- 98-95-3
- Other Names
-
- Essence of Mirbane
- Essence of Myrbane
- Mirbane oil
- NCI-C60082
- NITROBENZENE
- NITROBENZOL
- NSC 9573
- Nitrobenzeen
- Nitrobenzen
- Oil of Mirbane
- Oil of Myrbane
- Rcra waste number U169
- UN 1662
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- EA : Electron affinity (eV).
- 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).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- 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).
- Tboil : Normal Boiling Point Temperature (K).
- Tboil : Boiling point at given pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Tfus : Melting point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| PAff | 800.30 | kJ/mol | NIST |
| BasG | 769.50 | kJ/mol | NIST |
| ΔcH°liquid | [-3096.00; -3073.80] | kJ/mol |
|
| ΔcH°liquid | -3088.08 ± 0.42 | kJ/mol | NIST |
| ΔcH°liquid | -3096.00 | kJ/mol | NIST |
| ΔcH°liquid | -3073.80 | kJ/mol | NIST |
| η | 0.0016860 | Pa×s | Ion Pai... |
| EA | [0.40; 1.18] | eV |
|
| EA | 1.00 ± 0.01 | eV | NIST |
| EA | 1.01 ± 0.10 | eV | NIST |
| EA | 1.00 ± 0.06 | eV | NIST |
| EA | 1.00 ± 0.02 | eV | NIST |
| EA | 1.02 ± 0.05 | eV | NIST |
| EA | 1.18 ± 0.05 | eV | NIST |
| EA | 1.10 | eV | NIST |
| EA | 0.70 ± 0.20 | eV | NIST |
| EA | Outlier 0.40 | eV | NIST |
| ΔfG° | 147.60 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | 68.53 ± 0.67 | kJ/mol | NIST |
| ΔfH°liquid | [-16.00; 12.50] | kJ/mol |
|
| ΔfH°liquid | 12.50 ± 0.54 | kJ/mol | NIST |
| ΔfH°liquid | -16.00 | kJ/mol | NIST |
| ΔfusH° | 16.70 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [54.50; 56.10] | kJ/mol |
|
| ΔvapH° | 54.50 | kJ/mol | NIST |
| ΔvapH° | 55.01 ± 0.02 | kJ/mol | NIST |
| ΔvapH° | 55.00 | kJ/mol | NIST |
| ΔvapH° | 56.10 ± 1.70 | kJ/mol | NIST |
| IE | [9.60; 10.80] | eV |
|
| IE | 9.94 ± 0.08 | eV | NIST |
| IE | 9.67 | eV | NIST |
| IE | 9.80 | eV | NIST |
| IE | 10.16 ± 0.08 | eV | NIST |
| IE | 9.92 | eV | NIST |
| IE | 10.16 ± 0.08 | eV | NIST |
| IE | 9.87 ± 0.05 | eV | NIST |
| IE | 9.93 | eV | NIST |
| IE | 9.60 | eV | NIST |
| IE | 9.99 | eV | NIST |
| IE | 9.99 ± 0.01 | eV | NIST |
| IE | 9.85 ± 0.03 | eV | NIST |
| IE | 9.94 ± 0.03 | eV | NIST |
| IE | 9.90 | eV | NIST |
| IE | 9.86 ± 0.05 | eV | NIST |
| IE | 9.90 ± 0.03 | eV | NIST |
| IE | 10.16 ± 0.04 | eV | NIST |
| IE | 9.70 ± 0.10 | eV | NIST |
| IE | 9.92 | eV | NIST |
| IE | 9.86 | eV | NIST |
| IE | 9.90 | eV | NIST |
| IE | 9.92 | eV | NIST |
| IE | 9.93 | eV | NIST |
| IE | Outlier 10.80 | eV | NIST |
| IE | 9.93 | eV | NIST |
| IE | 10.10 ± 0.10 | eV | NIST |
| IE | 9.88 ± 0.01 | eV | NIST |
| IE | 10.26 | eV | NIST |
| log10WS | [-1.81; -1.80] |
|
|
| log10WS | -1.81 | Aq. Sol... | |
| log10WS | -1.80 | Estimat... | |
| logPoct/wat | 1.595 | Crippen Calculated Property | |
| McVol | 89.060 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| NFPA Health | 3 | KDB | |
| NFPA Safety | 2 | KDB | |
| Pc | 4749.69 | kPa | Joback Calculated Property |
| Inp | [180.05; 1114.00] |
|
|
| Inp | 1049.40 | NIST | |
| Inp | 1058.30 | NIST | |
| Inp | 1066.70 | NIST | |
| Inp | 1049.20 | NIST | |
| Inp | 1057.40 | NIST | |
| Inp | 1068.50 | NIST | |
| Inp | 1048.20 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1103.00 | NIST | |
| Inp | 1103.00 | NIST | |
| Inp | 1085.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1114.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1088.00 | NIST | |
| Inp | 1100.00 | NIST | |
| Inp | 1100.00 | NIST | |
| Inp | 1088.80 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | Outlier 180.05 | NIST | |
| Inp | 1100.00 | NIST | |
| Inp | 1049.40 | NIST | |
| Inp | 1068.50 | NIST | |
| Inp | 1085.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1088.80 | NIST | |
| I | [1683.00; 1683.00] |
|
|
| I | 1683.00 | NIST | |
| I | 1683.00 | NIST | |
| I | 1683.00 | NIST | |
| S°liquid | 224.30 | J/mol×K | NIST |
| Tboil | [478.15; 485.09] | K |
|
| Tboil | 483.90 | K | KDB |
| Tboil | 483.80 ± 0.40 | K | NIST |
| Tboil | 484.00 ± 1.00 | K | NIST |
| Tboil | 484.20 ± 0.50 | K | NIST |
| Tboil | 483.70 ± 0.50 | K | NIST |
| Tboil | 484.00 | K | NIST |
| Tboil | 483.70 ± 0.50 | K | NIST |
| Tboil | 483.55 ± 0.40 | K | NIST |
| Tboil | 483.71 ± 0.40 | K | NIST |
| Tboil | 483.95 ± 0.70 | K | NIST |
| Tboil | 481.10 ± 1.00 | K | NIST |
| Tboil | 483.95 ± 0.50 | K | NIST |
| Tboil | 485.09 ± 0.25 | K | NIST |
| Tboil | 482.15 ± 1.00 | K | NIST |
| Tboil | 483.90 ± 0.50 | K | NIST |
| Tboil | 483.90 ± 0.30 | K | NIST |
| Tboil | 483.95 ± 0.30 | K | NIST |
| Tboil | 483.90 ± 0.30 | K | NIST |
| Tboil | 483.90 ± 0.50 | K | NIST |
| Tboil | 482.65 ± 0.50 | K | NIST |
| Tboil | 484.00 ± 0.40 | K | NIST |
| Tboil | 482.15 ± 2.00 | K | NIST |
| Tboil | 482.00 ± 2.00 | K | NIST |
| Tboil | 484.00 ± 0.35 | K | NIST |
| Tboil | 483.95 ± 1.00 | K | NIST |
| Tboil | Outlier 478.15 ± 1.50 | K | NIST |
| Tc | 769.26 | K | Joback Calculated Property |
| Tfus | [278.81; 278.82] | K |
|
| Tfus | 278.81 | K | KDB |
| Tfus | 278.82 | K | Aq. Sol... |
| Vc | 0.345 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [180.20; 230.26] | J/mol×K | [515.20; 769.26] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 180 190 200 210 220 230 600 700 | ||||
| Cp,gas | 180.20 | J/mol×K | 515.20 | Joback Calculated Property |
| Cp,gas | 190.50 | J/mol×K | 557.54 | Joback Calculated Property |
| Cp,gas | 199.95 | J/mol×K | 599.89 | Joback Calculated Property |
| Cp,gas | 208.60 | J/mol×K | 642.23 | Joback Calculated Property |
| Cp,gas | 216.51 | J/mol×K | 684.57 | Joback Calculated Property |
| Cp,gas | 223.71 | J/mol×K | 726.92 | Joback Calculated Property |
| Cp,gas | 230.26 | J/mol×K | 769.26 | Joback Calculated Property |
| Cp,liquid | [176.00; 188.70] | J/mol×K | [293.00; 335.50] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 176 178 180 182 184 186 188 300 310 320 330 | ||||
| Cp,liquid | 179.90 | J/mol×K | 293.00 | NIST |
| Cp,liquid | 180.20 | J/mol×K | 293.00 | NIST |
| Cp,liquid | 179.95 | J/mol×K | 293.15 | NIST |
| Cp,liquid | 186.73 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 177.80 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 186.69 | J/mol×K | 298.10 | NIST |
| Cp,liquid | 181.13 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 176.00 | J/mol×K | 303.00 | NIST |
| Cp,liquid | 177.40 | J/mol×K | 303.00 | NIST |
| Cp,liquid | 177.30 | J/mol×K | 303.15 | NIST |
| Cp,liquid | 188.70 | J/mol×K | 335.50 | NIST |
| η | [0.0015286; 0.0019834] | Pa×s | [293.15; 308.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 1.50e-3 1.60e-3 1.70e-3 1.80e-3 1.90e-3 2.00e-3 295 300 305 | ||||
| η | 0.0019834 | Pa×s | 293.15 | Densiti... |
| η | 0.0017910 | Pa×s | 298.15 | Thermop... |
| η | 0.0016860 | Pa×s | 298.15 | Thermop... |
| η | 0.0018095 | Pa×s | 298.15 | Densiti... |
| η | 0.0016595 | Pa×s | 303.15 | Densiti... |
| η | 0.0016187 | Pa×s | 303.15 | Thermop... |
| η | 0.0015543 | Pa×s | 308.15 | Thermop... |
| η | 0.0015430 | Pa×s | 308.15 | Thermop... |
| η | 0.0015286 | Pa×s | 308.15 | Densiti... |
| ΔfusH | [10.81; 12.12] | kJ/mol | [278.80; 278.90] |
|
| ΔfusH | 12.12 | kJ/mol | 278.80 | NIST |
| ΔfusH | 12.12 | kJ/mol | 278.80 | NIST |
| ΔfusH | 12.12 | kJ/mol | 278.80 | NIST |
| ΔfusH | 10.81 | kJ/mol | 278.90 | NIST |
| ΔvapH | [48.50; 56.10] | kJ/mol | [287.50; 445.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 48 50 52 54 56 300 350 400 | ||||
| ΔvapH | 54.70 | kJ/mol | 287.50 | NIST |
| ΔvapH | 56.10 ± 0.42 | kJ/mol | 291.00 | NIST |
| ΔvapH | 52.50 | kJ/mol | 293.00 | NIST |
| ΔvapH | 54.30 | kJ/mol | 303.00 | NIST |
| ΔvapH | 48.90 | kJ/mol | 425.00 | NIST |
| ΔvapH | 48.50 | kJ/mol | 445.00 | NIST |
| Pvap | [95.30; 95.50] | kPa | [481.45; 483.05] |
|
| Pvap | 95.50 | kPa | 481.45 | Vapor-l... |
| Pvap | 95.30 | kPa | 483.05 | Vapor-l... |
| n0 | [1.54005; 1.55488] | [293.15; 318.15] |
|
|
|
T(K) Refractive Index 1.54 1.55 1.55 1.56 300 310 | ||||
| n0 | 1.55488 | 293.15 | A study... | |
| n0 | 1.54900 | 293.15 | Volumet... | |
| n0 | 1.55000 | 298.15 | Excess ... | |
| n0 | 1.55000 | 298.15 | Bubble ... | |
| n0 | 1.54930 | 298.15 | Physico... | |
| n0 | 1.54992 | 298.15 | Volumet... | |
| n0 | 1.55000 | 298.15 | Bubble ... | |
| n0 | 1.54746 | 303.15 | Volumet... | |
| n0 | 1.54760 | 303.15 | Excess ... | |
| n0 | 1.54500 | 308.15 | Volumet... | |
| n0 | 1.54250 | 313.15 | Volumet... | |
| n0 | 1.54005 | 318.15 | Volumet... | |
| ρl | [1163.32; 1212.99] | kg/m3 | [283.15; 333.15] |
|
|
T(K) Liquid Density (kg/m3) 1160 1170 1180 1190 1200 1210 300 320 | ||||
| ρl | 1212.99 | kg/m3 | 283.15 | The den... |
| ρl | 1211.53 | kg/m3 | 288.15 | Volumet... |
| ρl | 1208.01 | kg/m3 | 288.15 | The den... |
| ρl | 1198.80 | kg/m3 | 293.15 | Isobari... |
| ρl | 1203.05 | kg/m3 | 293.15 | Theoret... |
| ρl | 1203.05 | kg/m3 | 293.15 | The den... |
| ρl | 1202.61 | kg/m3 | 293.15 | Volumet... |
| ρl | 1198.12 | kg/m3 | 298.15 | A combi... |
| ρl | 1198.01 | kg/m3 | 298.15 | Volumet... |
| ρl | 1198.91 | kg/m3 | 298.15 | Partial... |
| ρl | 1198.00 | kg/m3 | 298.15 | Bubble ... |
| ρl | 1198.36 | kg/m3 | 298.15 | Ionic s... |
| ρl | 1198.00 | kg/m3 | 298.15 | Bubble ... |
| ρl | 1198.20 | kg/m3 | 298.15 | The den... |
| ρl | 1198.20 | kg/m3 | 298.15 | The phy... |
| ρl | 1193.25 | kg/m3 | 303.15 | The den... |
| ρl | 1193.45 | kg/m3 | 303.15 | Studies... |
| ρl | 1193.50 | kg/m3 | 303.15 | Volumet... |
| ρl | 1193.15 | kg/m3 | 303.15 | Theoret... |
| ρl | 1193.40 | kg/m3 | 303.15 | Studies... |
| ρl | 1193.25 | kg/m3 | 303.15 | The phy... |
| ρl | 1189.60 | kg/m3 | 303.15 | Density... |
| ρl | 1188.29 | kg/m3 | 308.15 | Studies... |
| ρl | 1189.40 | kg/m3 | 308.15 | Density... |
| ρl | 1188.17 | kg/m3 | 308.15 | The phy... |
| ρl | 1183.69 | kg/m3 | 313.15 | Studies... |
| ρl | 1183.21 | kg/m3 | 313.15 | Theoret... |
| ρl | 1187.20 | kg/m3 | 313.15 | Density... |
| ρl | 1183.21 | kg/m3 | 313.15 | The phy... |
| ρl | 1178.24 | kg/m3 | 318.15 | The phy... |
| ρl | 1177.32 | kg/m3 | 318.15 | Studies... |
| ρl | 1173.26 | kg/m3 | 323.15 | The phy... |
| ρl | 1173.27 | kg/m3 | 323.15 | Theoret... |
| ρl | 1163.32 | kg/m3 | 333.15 | Theoret... |
| ΔfusS | [38.80; 43.48] | J/mol×K | [278.80; 278.90] |
|
| ΔfusS | 43.48 | J/mol×K | 278.80 | NIST |
| ΔfusS | 38.80 | J/mol×K | 278.90 | NIST |
| γ | [0.04; 0.04] | N/m | [303.15; 323.15] |
|
| γ | 0.04 | N/m | 303.15 | Thermo ... |
| γ | 0.04 | N/m | 313.15 | Thermo ... |
| γ | 0.04 | N/m | 323.15 | Thermo ... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil | 483.05 | K | 95.30 | Excess ... |
| Tfus | [299.74; 614.38] | K | [100000.00; 3000000.00] |
|
|
P(kPa) Melting point (K) 300 350 400 450 500 550 600 1000000 2000000 3000000 | ||||
| Tfus | 299.74 | K | 100000.00 | Fusion ... |
| Tfus | 320.77 | K | 200000.00 | Fusion ... |
| Tfus | 340.02 | K | 300000.00 | Fusion ... |
| Tfus | 360.41 | K | 400000.00 | Fusion ... |
| Tfus | 378.61 | K | 500000.00 | Fusion ... |
| Tfus | 395.90 | K | 600000.00 | Fusion ... |
| Tfus | 412.30 | K | 700000.00 | Fusion ... |
| Tfus | 427.24 | K | 800000.00 | Fusion ... |
| Tfus | 442.98 | K | 900000.00 | Fusion ... |
| Tfus | 462.61 | K | 1000000.00 | Fusion ... |
| Tfus | 516.38 | K | 1500000.00 | Fusion ... |
| Tfus | 565.62 | K | 2000000.00 | Fusion ... |
| Tfus | 595.88 | K | 2500000.00 | Fusion ... |
| Tfus | 614.38 | K | 3000000.00 | Fusion ... |
Datasets
Speed of sound, m/s
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Frequency, MHz - Liquid | Speed of sound, m/s - Liquid |
| 303.15 | 100.00 | 2.0 | 1445.6 |
| Reference | |||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [359.28; 513.96] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.53379e+01 | |||
| Coefficient B | -4.64614e+03 | |||
| Coefficient C | -5.05750e+01 | |||
| Temperature range, min. | 359.28 | |||
| Temperature range, max. | 513.96 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
| Pvap | 1.33 | kPa | 359.28 | Calculated Property |
| Pvap | 2.95 | kPa | 376.47 | Calculated Property |
| Pvap | 6.02 | kPa | 393.65 | Calculated Property |
| Pvap | 11.49 | kPa | 410.84 | Calculated Property |
| Pvap | 20.67 | kPa | 428.03 | Calculated Property |
| Pvap | 35.33 | kPa | 445.21 | Calculated Property |
| Pvap | 57.75 | kPa | 462.40 | Calculated Property |
| Pvap | 90.75 | kPa | 479.59 | Calculated Property |
| Pvap | 137.72 | kPa | 496.77 | Calculated Property |
| Pvap | 202.63 | kPa | 513.96 | Calculated Property |
| Pvap | [6.43e-03; 4167.87] | kPa | [278.91; 719.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.29288e+02 | |||
| Coefficient B | -1.14658e+04 | |||
| Coefficient C | -1.66824e+01 | |||
| Coefficient D | 9.14721e-06 | |||
| Temperature range, min. | 278.91 | |||
| Temperature range, max. | 719.00 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 400 600 | ||||
| Pvap | 6.43e-03 | kPa | 278.91 | Calculated Property |
| Pvap | 0.26 | kPa | 327.81 | Calculated Property |
| Pvap | 3.31 | kPa | 376.71 | Calculated Property |
| Pvap | 20.44 | kPa | 425.61 | Calculated Property |
| Pvap | 80.01 | kPa | 474.51 | Calculated Property |
| Pvap | 232.70 | kPa | 523.40 | Calculated Property |
| Pvap | 556.46 | kPa | 572.30 | Calculated Property |
| Pvap | 1169.96 | kPa | 621.20 | Calculated Property |
| Pvap | 2264.56 | kPa | 670.10 | Calculated Property |
| Pvap | 4167.87 | kPa | 719.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzene, nitro-.
Mixtures
- Benzene, nitro- + Triethylene glycol
- Benzene, nitro- + Ethanol, 2,2'-oxybis-
- Benzene, nitro- + Benzaldehyde
- Benzene, nitro- + Benzene, bromo-
- Benzene, nitro- + Formamide, N,N-dimethyl-
- Benzene, nitro- + Phenol, 2-methyl-
- Benzene, nitro- + Phenol, 3-methyl-
- Benzene, nitro- + p-Cresol
- Benzene, nitro- + Dimethyl Sulfoxide
- Benzene, nitro- + 2-Propenenitrile
- Benzene, nitro- + 1-Hexanol
- Benzene, nitro- + Tetrabutylammonium hexafluorophosphate
- Benzene, nitro- + Benzene
- Benzene, nitro- + Toluene
- Benzene, nitro- + Ethylbenzene
- Benzene, nitro- + Styrene
- Benzene, nitro- + o-Xylene
- Benzene, nitro- + Benzene, 1,3-dimethyl-
- Benzene, nitro- + p-Xylene
- Benzene, nitro- + Methyl Alcohol
Find more mixtures with Benzene, nitro-.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Thermophysical Properties For Diethylene Glycol + Nitrobenzene and Triethylene Glycol + (Chloro-, Bromo-, Nitro-) Benzene Systems at Different Temperatures
- Density, Viscosity, Sound Speed, and Thermoacoustical Parameters of Benzaldehyde with Chlorobenzene or Nitrobenzene at 303.15 K, 308.15 K, and 313.15 K
- Excess Gibbs energies of binary mixtures formed by nitrobenzene with selected compounds at 94.95 kPa
- Solution thermodynamics near the liquid liquid critical point I. First-order excess derivatives
- Vapor-liquid equilibrium for the binary mixtures of dimethylsulfoxide with substituted benzenes
- Excess enthalpies of dimethylsulfoxide with substituted benzenes at 298.15K
- Vapor-liquid equilibrium and excess Gibbs energies of some binary mixtures of acrylonitrile at 95.5 kPa
- Bubble point measurements of binary mixtures formed by 1-hexanol with selected nitro-compounds and substituted benzenes at 95.6 kPa
- Ionic solvation of tetrabutylammonium hexafluorophosphate in pure nitromethane, 1, 3-dioxolane and nitrobenzene: A comparative physicochemical study
- The liquid-liquid coexistence curves of {x nitrobenzene + (1 - x) 2-methylpentane} and {x nitrobenzene + (1 - x) isooctane} in the critical region
- Liquid-liquid equilibrium data for binary systems containing o-dichlorobenzene and nitrobenzene
- A study of densities and volumetric properties of binary mixtures containing nitrobenzene at T = (293.15 to 353.15) K
- Bubble point temperatures of the binary mixtures of nitrobenzene with C1 C4 aliphatic alcohols at 94.95 kPa
- Bubble points of the binary mixtures formed by ethylbenzene with some chloroaliphatics and substituted benzenes at p = 94.7 kPa
- Volumetric properties of dichloromethane with aniline or nitrobenzene at different temperatures: A theoretical and experimental study
- Volumetric properties of binary mixtures of tributylamine with benzene derivatives and comparison with ERAS model results at temperatures from (293.15 to 333.15) K
- 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
- Enthalpies of formation of nitromethane and nitrobenzene: New experiments vs. quantum chemical calculations
- The density, refractive index, and thermodynamic behaviour of binary mixtures of 1,3-Diethenyl-1,1,3,3-tetramethyldisiloxane with aromatic hydrocarbons
- A combined experimental and computational investigation of excess molar enthalpies of (nitrobenzene + alkanol) mixtures
- Ultrasonic and 31P NMR investigations of an acidic nuclear extractant with some monosubstituted benzenes
- The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
- Theoretical and experimental study on volumetric and electromagnetic properties of binary systems consisting of 1,2-dichloroethane with benzene and its derivatives at T = (293.15 to 333.15) K
- Studies on the importance of nature of substituent on the thermodynamic and transport properties of liquid mixtures at various temperatures
- Volumetric and refractive properties of 1,3,5,7-tetravinyl-1,3,5,7-tetramethylcyclotetrasiloxane with methoxybenzene, chlorobenzene, tert-butylbenzene and nitrobenzene at T = (298.15-318.15) K
- Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
- Volumetric and electromagnetic properties of binary mixtures consist of benzene derivatives at different temperature and ternary mixtures with 1,2-dichloroethane at T = 293.15 K with application of the Prigogine-Flory-Patterson theory and PC-SAFT
- Bubble Temperature Measurements on the Binary Mixtures of n-Heptane or Nitrobenzene or Chlorobenzene with Some Chloroethanes and Chloroethylenes at (94.6 to 95.8) kPa
- Thermophysical Properties of Binary Mixtures of Cyclohexane + Nitrobenzene, Cyclohexanone + Nitrobenzene, and Cyclohexane + Cyclohexanone at (298.15, 303.15, and 308.15) K
- Temperature Dependences of Limiting Activity Coefficients and Henry s Law Constants for Nitrobenzene, Aniline, and Cyclohexylamine in Water
- Thermodynamics of Dissolution for Bis(triazine)-Bipyridine-Class Ligands in Different Diluents and Its Reflection on Extraction
- Densities and Viscosities of Binary and Ternary Mixtures of (Nitrobenzene + 1-Bromobutane), (1-Bromobutane + Methylcyclohexane), (Nitrobenzene + Methylcyclohexane), and (Methylcyclohexane + Nitrobenzene + 1-Bromobutane) from (293.15 to 308.15) K
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Isobaric Vapor Liquid Equilibrium Data of Acrylonitrile (1) + Heptan-1-ol (2), Acrylonitrile (1) + Ethanol (2), and Nitrobenzene (1) + Heptan-1-ol (2) at 96.5 kPa
- Excess Volumes of Binary Solutions of Methyl Formate, Ethyl Formate, Propyl Formate, and Benzyl Acetate with Bromo-, Chloro-, and Nitrobenzenes at (303.15, 308.15, and 313.15) K
- Fusion Curves and Enthalpy and Internal Energy Changes of Benzene, Nitrobenzene, Bromobenzene, and Chlorobenzene at Pressures up to 3500 MPa
- Thermo Physical Properties of 4-Hydroxy 4-Methyl Pentanone with Nitrobenzene or Ethyl Benzene at Temperatures of (303.15, 313.15, and 323.15) K and a Pressure of 0.1 MPa
- Assessing the Salting-Out Behavior of Nitrobenzene, 2-Nitrotoluene, and 3-Nitrotoluene from Solubility Values in Pure Water and Seawater at Temperatures between (277 and 314) K
- Liquid-Liquid Equilibria of Nitrobenzene-Inorganic Acid Systems at 298.15 K
- Ion Pair and Triple Ion Formation by Some Tetraalkylammonium Iodides in Binary Mixtures of Carbon Tetrachloride + Nitrobenzene
- Partial Molar Volumes of Butyltriethylammonium Iodide in Single Nonaqueous Solvents at 298.15 K
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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