- InChI
- InChI=1S/C6H7N/c7-6-4-2-1-3-5-6/h1-5H,7H2
- InChI Key
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N
- Formula
- C6H7N
- SMILES
- Nc1ccccc1
- Molecular Weight1
- 93.13
- CAS
- 62-53-3
- Other Names
-
- Aminobenzene
- Aminophen
- Anilin
- Anilina
- Aniline Oil
- Aniline reagent
- Anyvim
- Benzenamine
- Benzene, amino-
- Benzeneamine
- Benzidam
- Blue Oil
- C.I. 76000
- C.I. Oxidation base 1
- Cyanol
- Huile D'aniline
- Krystallin
- Kyanol
- NCI-C03736
- Phenylamine
- Rcra waste number U012
- UN 1547
- 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).
- ΔcH°solid : Standard solid 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).
- 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).
- 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.
- 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).
- 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 | 0.3840 | KDB | |
| PAff | 882.50 | kJ/mol | NIST |
| Tig | 1043.15 | K | KDB |
| BasG | 850.60 | kJ/mol | NIST |
| ΔcH°liquid | [-3411.00; -3391.00] | kJ/mol |
|
| ΔcH°liquid | -3393.10 ± 1.00 | kJ/mol | NIST |
| ΔcH°liquid | -3392.00 | kJ/mol | NIST |
| ΔcH°liquid | -3392.30 | kJ/mol | NIST |
| ΔcH°liquid | -3391.00 ± 13.00 | kJ/mol | NIST |
| ΔcH°liquid | -3411.00 | kJ/mol | NIST |
| ΔcH°solid | -3391.00 | kJ/mol | NIST |
| μ | 1.60 | debye | KDB |
| LFL | 1.30 | % in Air | KDB |
| Tflash,cc | 348.71 | K | KDB |
| Tflash,oc | 343.15 | K | KDB |
| ΔfG° | 166.80 | kJ/mol | KDB |
| Rg | 3.3930 | KDB | |
| ΔfH°gas | [81.00; 87.03] | kJ/mol |
|
| ΔfH°gas | 86.92 | kJ/mol | KDB |
| ΔfH°gas | 87.03 ± 0.88 | kJ/mol | NIST |
| ΔfH°gas | 82.40 | kJ/mol | NIST |
| ΔfH°gas | 83.20 | kJ/mol | NIST |
| ΔfH°gas | 81.00 ± 3.00 | kJ/mol | NIST |
| ΔfH°gas | 85.40 | kJ/mol | NIST |
| ΔfH°liquid | [30.00; 33.00] | kJ/mol |
|
| ΔfH°liquid | 31.30 ± 0.84 | kJ/mol | NIST |
| ΔfH°liquid | 30.00 | kJ/mol | NIST |
| ΔfH°liquid | 30.80 | kJ/mol | NIST |
| ΔfH°liquid | 33.00 | kJ/mol | NIST |
| ΔfusH° | 10.53 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 41.87 | kJ/mol | Joback Calculated Property |
| IE | [7.48; 8.35] | eV |
|
| IE | 7.72 ± 0.00 | eV | NIST |
| IE | 7.74 ± 0.01 | eV | NIST |
| IE | 7.72 ± 0.00 | eV | NIST |
| IE | 7.72 ± 0.00 | eV | NIST |
| IE | 7.48 | eV | NIST |
| IE | 8.00 | eV | NIST |
| IE | Outlier 8.27 ± 0.05 | eV | NIST |
| IE | 7.80 | eV | NIST |
| IE | Outlier 8.35 | eV | NIST |
| IE | 7.71 ± 0.01 | eV | NIST |
| IE | 7.65 ± 0.02 | eV | NIST |
| IE | 7.60 ± 0.10 | eV | NIST |
| IE | 7.71 | eV | NIST |
| IE | 7.66 | eV | NIST |
| IE | 7.63 | eV | NIST |
| IE | 7.89 ± 0.03 | eV | NIST |
| IE | 8.10 ± 0.10 | eV | NIST |
| IE | 7.70 ± 0.01 | eV | NIST |
| IE | 7.89 | eV | NIST |
| IE | 7.61 ± 0.05 | eV | NIST |
| IE | 7.68 | eV | NIST |
| IE | 7.67 ± 0.03 | eV | NIST |
| IE | 7.70 | eV | NIST |
| IE | 7.70 ± 0.02 | eV | NIST |
| IE | 7.69 ± 0.02 | eV | NIST |
| IE | 8.05 | eV | NIST |
| IE | 8.02 | eV | NIST |
| IE | 8.04 | eV | NIST |
| IE | 8.05 | eV | NIST |
| IE | 8.03 | eV | NIST |
| IE | 8.05 | eV | NIST |
| IE | 8.10 | eV | NIST |
| IE | 8.02 | eV | NIST |
| IE | 8.05 | eV | NIST |
| log10WS | [-0.41; -0.41] |
|
|
| log10WS | -0.41 | Aq. Sol... | |
| log10WS | -0.41 | Estimat... | |
| logPoct/wat | 1.269 | Crippen Calculated Property | |
| McVol | 81.620 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| NFPA Health | 3 | KDB | |
| Pc | [4890.00; 5319.56] | kPa |
|
| Pc | Outlier 4890.00 | kPa | KDB |
| Pc | 5310.00 ± 91.19 | kPa | NIST |
| Pc | 5300.00 ± 91.19 | kPa | NIST |
| Pc | 5299.30 ± 101.32 | kPa | NIST |
| Pc | 5294.23 ± 1.00 | kPa | NIST |
| Pc | 5304.36 ± 1.00 | kPa | NIST |
| Pc | 5319.56 ± 101.32 | kPa | NIST |
| ρc | 324.08 ± 4.66 | kg/m3 | NIST |
| Inp | [155.33; 999.00] |
|
|
| Inp | 939.10 | NIST | |
| Inp | 952.60 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 967.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 939.00 | NIST | |
| Inp | 983.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 999.00 | NIST | |
| Inp | 939.20 | NIST | |
| Inp | 980.00 | NIST | |
| Inp | 945.60 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | 971.00 | NIST | |
| Inp | 979.00 | NIST | |
| Inp | 977.00 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | 954.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 950.00 | NIST | |
| Inp | 952.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 946.00 | NIST | |
| Inp | 945.00 | NIST | |
| Inp | 946.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | Outlier 155.33 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 979.00 | NIST | |
| Inp | Outlier 155.33 | NIST | |
| Inp | 939.20 | NIST | |
| I | [1710.00; 1766.70] |
|
|
| I | 1752.00 | NIST | |
| I | 1764.50 | NIST | |
| I | 1717.00 | NIST | |
| I | 1754.00 | NIST | |
| I | 1747.00 | NIST | |
| I | 1759.00 | NIST | |
| I | 1761.00 | NIST | |
| I | 1766.70 | NIST | |
| I | 1710.00 | NIST | |
| I | 1740.00 | NIST | |
| I | 1710.00 | NIST | |
| S°liquid | [191.30; 191.60] | J/mol×K |
|
| S°liquid | 191.30 | J/mol×K | NIST |
| S°liquid | 191.60 | J/mol×K | NIST |
| Tboil | [455.00; 458.00] | K |
|
| Tboil | 457.32 | K | KDB |
| Tboil | 457.70 ± 0.40 | K | NIST |
| Tboil | 457.20 | K | NIST |
| Tboil | 457.20 | K | NIST |
| Tboil | 457.70 ± 0.50 | K | NIST |
| Tboil | 457.10 ± 0.40 | K | NIST |
| Tboil | 457.25 ± 0.30 | K | NIST |
| Tboil | 457.40 ± 0.60 | K | NIST |
| Tboil | 457.00 ± 0.30 | K | NIST |
| Tboil | 457.70 ± 0.40 | K | NIST |
| Tboil | 457.06 ± 0.15 | K | NIST |
| Tboil | 457.60 ± 0.40 | K | NIST |
| Tboil | 457.10 ± 9.20 | K | NIST |
| Tboil | 457.30 ± 0.40 | K | NIST |
| Tboil | 457.50 ± 0.40 | K | NIST |
| Tboil | 457.10 ± 0.40 | K | NIST |
| Tboil | 455.70 ± 2.00 | K | NIST |
| Tboil | 457.50 ± 0.40 | K | NIST |
| Tboil | 457.08 ± 0.07 | K | NIST |
| Tboil | 457.50 ± 0.30 | K | NIST |
| Tboil | 457.40 ± 0.60 | K | NIST |
| Tboil | 457.50 ± 0.30 | K | NIST |
| Tboil | 457.50 ± 0.30 | K | NIST |
| Tboil | 457.82 ± 0.20 | K | NIST |
| Tboil | 457.20 ± 0.30 | K | NIST |
| Tboil | 457.60 ± 0.40 | K | NIST |
| Tboil | 457.60 ± 0.30 | K | NIST |
| Tboil | 457.50 ± 0.50 | K | NIST |
| Tboil | Outlier 455.00 ± 1.00 | K | NIST |
| Tboil | 457.50 ± 0.30 | K | NIST |
| Tboil | 457.60 ± 0.40 | K | NIST |
| Tboil | 457.50 ± 0.50 | K | NIST |
| Tboil | 457.60 ± 0.40 | K | NIST |
| Tboil | 457.70 ± 0.30 | K | NIST |
| Tboil | 455.90 ± 0.30 | K | NIST |
| Tboil | 456.00 ± 0.30 | K | NIST |
| Tboil | 458.00 ± 0.10 | K | NIST |
| Tboil | 457.00 ± 1.00 | K | NIST |
| Tboil | 457.60 ± 0.30 | K | NIST |
| Tboil | 457.60 ± 0.40 | K | NIST |
| Tboil | 457.60 ± 0.40 | K | NIST |
| Tboil | 457.60 ± 0.50 | K | NIST |
| Tboil | 457.00 ± 1.50 | K | NIST |
| Tboil | 456.00 ± 2.00 | K | NIST |
| Tboil | Outlier 455.00 ± 1.50 | K | NIST |
| Tboil | Outlier 455.00 ± 5.00 | K | NIST |
| Tboil | Outlier 455.10 ± 11.11 | K | NIST |
| Tc | 699.00 | K | KDB |
| Tfus | [265.00; 279.33] | K |
|
| Tfus | 267.13 | K | KDB |
| Tfus | 267.00 | K | NIST |
| Tfus | 267.65 ± 0.40 | K | NIST |
| Tfus | 265.00 ± 1.00 | K | NIST |
| Tfus | 267.11 ± 0.10 | K | NIST |
| Tfus | 267.13 ± 0.07 | K | NIST |
| Tfus | Outlier 279.25 ± 0.40 | K | NIST |
| Tfus | 267.05 ± 0.30 | K | NIST |
| Tfus | 267.20 ± 0.50 | K | NIST |
| Tfus | 267.12 ± 0.10 | K | NIST |
| Tfus | 267.15 ± 0.05 | K | NIST |
| Tfus | 267.25 ± 0.50 | K | NIST |
| Tfus | 267.00 ± 0.15 | K | NIST |
| Tfus | 266.85 ± 0.05 | K | NIST |
| Tfus | 267.05 ± 0.30 | K | NIST |
| Tfus | 267.00 ± 1.50 | K | NIST |
| Tfus | 267.10 ± 0.05 | K | NIST |
| Tfus | 266.91 ± 0.10 | K | NIST |
| Tfus | 266.65 ± 0.20 | K | NIST |
| Tfus | 266.99 ± 0.20 | K | NIST |
| Tfus | 266.95 ± 0.25 | K | NIST |
| Tfus | Outlier 279.33 ± 0.30 | K | NIST |
| Tfus | 266.95 ± 0.30 | K | NIST |
| Tfus | 267.05 ± 0.20 | K | NIST |
| Tfus | 265.00 ± 2.00 | K | NIST |
| Ttriple | [266.90; 267.30] | K |
|
| Ttriple | 267.13 ± 0.02 | K | NIST |
| Ttriple | 267.30 ± 0.20 | K | NIST |
| Ttriple | 266.90 ± 0.10 | K | NIST |
| Vc | 0.287 | m3/kmol | KDB |
| Zc | [0.2414780; 0.2600000] |
|
|
| Zc | 0.2414780 | KDB | |
| Zc | 0.2600000 ± 0.0030000 | NIST | |
| Zra | 0.26 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [149.06; 202.11] | J/mol×K | [435.89; 666.01] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 150 160 170 180 190 200 500 600 | ||||
| Cp,gas | 149.06 | J/mol×K | 435.89 | Joback Calculated Property |
| Cp,gas | 159.56 | J/mol×K | 474.24 | Joback Calculated Property |
| Cp,gas | 169.35 | J/mol×K | 512.60 | Joback Calculated Property |
| Cp,gas | 178.46 | J/mol×K | 550.95 | Joback Calculated Property |
| Cp,gas | 186.94 | J/mol×K | 589.30 | Joback Calculated Property |
| Cp,gas | 194.81 | J/mol×K | 627.66 | Joback Calculated Property |
| Cp,gas | 202.11 | J/mol×K | 666.01 | Joback Calculated Property |
| Cp,liquid | [109.20; 197.50] | J/mol×K | [267.30; 323.00] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 120 140 160 180 200 280 300 320 | ||||
| Cp,liquid | 109.20 | J/mol×K | 267.30 | NIST |
| Cp,liquid | 183.70 | J/mol×K | 288.00 | NIST |
| Cp,liquid | 192.00 | J/mol×K | 293.00 | NIST |
| Cp,liquid | 193.70 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 192.50 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 194.10 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 192.05 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 191.01 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 178.80 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 190.92 | J/mol×K | 298.20 | NIST |
| Cp,liquid | 193.38 | J/mol×K | 298.20 | NIST |
| Cp,liquid | 197.50 | J/mol×K | 323.00 | NIST |
| η | [0.0019500; 0.0043800] | Pa×s | [293.15; 323.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 2.00e-3 2.50e-3 3.00e-3 3.50e-3 4.00e-3 4.50e-3 300 310 320 | ||||
| η | 0.0043800 | Pa×s | 293.15 | Thermod... |
| η | 0.0036900 | Pa×s | 298.15 | Excess ... |
| η | 0.0032400 | Pa×s | 303.15 | Thermod... |
| η | 0.0031900 | Pa×s | 303.15 | Excess ... |
| η | 0.0028000 | Pa×s | 308.15 | Excess ... |
| η | 0.0024700 | Pa×s | 313.15 | Thermod... |
| η | 0.0024200 | Pa×s | 313.15 | Excess ... |
| η | 0.0019500 | Pa×s | 323.15 | Thermod... |
| ΔfusH | [10.54; 10.92] | kJ/mol | [266.80; 267.30] |
|
|
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 10.6 10.7 10.8 10.9 266.8 267 267.20000000000005 | ||||
| ΔfusH | 10.56 | kJ/mol | 266.80 | NIST |
| ΔfusH | 10.54 | kJ/mol | 267.10 | NIST |
| ΔfusH | 10.54 | kJ/mol | 267.10 | NIST |
| ΔfusH | 10.54 | kJ/mol | 267.13 | NIST |
| ΔfusH | 10.92 | kJ/mol | 267.30 | NIST |
| ΔvapH | [41.84; 54.00] | kJ/mol | [293.00; 506.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 42 44 46 48 50 52 54 300 400 500 | ||||
| ΔvapH | 52.90 | kJ/mol | 293.00 | NIST |
| ΔvapH | 52.20 | kJ/mol | 305.50 | NIST |
| ΔvapH | 53.00 | kJ/mol | 333.00 | NIST |
| ΔvapH | 51.40 | kJ/mol | 349.50 | NIST |
| ΔvapH | 54.00 | kJ/mol | 380.50 | NIST |
| ΔvapH | 53.60 | kJ/mol | 394.50 | NIST |
| ΔvapH | 48.60 | kJ/mol | 415.50 | NIST |
| ΔvapH | 48.00 ± 0.20 | kJ/mol | 424.50 | NIST |
| ΔvapH | 42.20 ± 0.40 | kJ/mol | 424.50 | NIST |
| ΔvapH | 45.20 ± 0.20 | kJ/mol | 424.50 | NIST |
| ΔvapH | 51.00 ± 0.20 | kJ/mol | 424.50 | NIST |
| ΔvapH | 42.44 | kJ/mol | 457.20 | NIST |
| ΔvapH | 41.84 | kJ/mol | 457.20 | KDB |
| ΔvapH | 46.30 | kJ/mol | 489.00 | NIST |
| ΔvapH | 45.80 | kJ/mol | 506.00 | NIST |
| Pvap | [0.09; 96.15] | kPa | [298.15; 455.40] |
|
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 300 350 400 450 | ||||
| Pvap | 0.09 | kPa | 298.15 | Thermod... |
| Pvap | 0.88 | kPa | 333.15 | An equi... |
| Pvap | 3.82 | kPa | 363.15 | An equi... |
| Pvap | 85.00 | kPa | 450.25 | Experim... |
| Pvap | 96.15 | kPa | 455.40 | Vapor L... |
| n0 | [1.58360; 1.59620] | [293.15; 298.15] |
|
|
| n0 | 1.59620 | 293.15 | Vapor l... | |
| n0 | 1.58620 | 293.15 | Activit... | |
| n0 | 1.58620 | 293.15 | Ternary... | |
| n0 | 1.58360 | 298.15 | Activit... | |
| ρl | [987.00; 1026.10] | kg/m3 | [288.15; 333.15] |
|
|
T(K) Liquid Density (kg/m3) 990 1000 1010 1020 1030 300 320 | ||||
| ρl | 1026.10 | kg/m3 | 288.15 | Excess ... |
| ρl | 1025.93 | kg/m3 | 288.15 | Volumet... |
| ρl | 1022.00 | kg/m3 | 293.00 | KDB |
| ρl | 1021.69 | kg/m3 | 293.15 | Thermod... |
| ρl | 1021.04 | kg/m3 | 293.15 | Volumet... |
| ρl | 1021.70 | kg/m3 | 293.15 | Excess ... |
| ρl | 1021.70 | kg/m3 | 293.15 | Studies... |
| ρl | 1021.71 | kg/m3 | 293.15 | Densiti... |
| ρl | 1021.70 | kg/m3 | 293.15 | Excess ... |
| ρl | 1017.40 | kg/m3 | 298.15 | Studies... |
| ρl | 1017.46 | kg/m3 | 298.15 | Thermod... |
| ρl | 1017.50 | kg/m3 | 298.15 | Excess ... |
| ρl | 1017.20 | kg/m3 | 298.15 | Thermod... |
| ρl | 1017.39 | kg/m3 | 298.15 | Cloud P... |
| ρl | 1017.30 | kg/m3 | 298.15 | Bubble ... |
| ρl | 1017.10 | kg/m3 | 298.15 | Volumet... |
| ρl | 1017.40 | kg/m3 | 298.15 | Excess ... |
| ρl | 1017.38 | kg/m3 | 298.15 | Liquid-... |
| ρl | 1017.42 | kg/m3 | 298.15 | Binary ... |
| ρl | 1017.44 | kg/m3 | 298.15 | Densiti... |
| ρl | 1017.10 | kg/m3 | 298.15 | Thermop... |
| ρl | 1017.42 | kg/m3 | 298.15 | (Liquid... |
| ρl | 1012.78 | kg/m3 | 303.15 | Study o... |
| ρl | 1012.81 | kg/m3 | 303.15 | Compara... |
| ρl | 1013.04 | kg/m3 | 303.15 | Thermod... |
| ρl | 1012.70 | kg/m3 | 303.15 | Thermop... |
| ρl | 1012.84 | kg/m3 | 303.15 | Volumet... |
| ρl | 1013.00 | kg/m3 | 303.15 | Volumet... |
| ρl | 1013.17 | kg/m3 | 303.15 | Densiti... |
| ρl | 1013.20 | kg/m3 | 303.15 | Studies... |
| ρl | 1013.10 | kg/m3 | 303.15 | Excess ... |
| ρl | 1013.00 | kg/m3 | 303.15 | Excess ... |
| ρl | 1008.64 | kg/m3 | 308.15 | Study o... |
| ρl | 1008.91 | kg/m3 | 308.15 | Compara... |
| ρl | 1008.90 | kg/m3 | 308.15 | Densiti... |
| ρl | 1009.00 | kg/m3 | 308.15 | Studies... |
| ρl | 1008.40 | kg/m3 | 308.15 | Thermop... |
| ρl | 1008.70 | kg/m3 | 308.15 | Excess ... |
| ρl | 1008.70 | kg/m3 | 308.15 | Excess ... |
| ρl | 1008.70 | kg/m3 | 308.15 | Volumet... |
| ρl | 1004.40 | kg/m3 | 313.15 | Excess ... |
| ρl | 1004.63 | kg/m3 | 313.15 | Densiti... |
| ρl | 1004.59 | kg/m3 | 313.15 | Compara... |
| ρl | 1004.40 | kg/m3 | 313.15 | Volumet... |
| ρl | 1004.70 | kg/m3 | 313.15 | Studies... |
| ρl | 1004.10 | kg/m3 | 313.15 | Thermop... |
| ρl | 1004.49 | kg/m3 | 313.15 | Study o... |
| ρl | 1004.36 | kg/m3 | 313.15 | Thermod... |
| ρl | 1000.36 | kg/m3 | 318.15 | Densiti... |
| ρl | 999.70 | kg/m3 | 318.15 | Thermop... |
| ρl | 1000.40 | kg/m3 | 318.15 | Studies... |
| ρl | 1000.21 | kg/m3 | 318.15 | Compara... |
| ρl | 1000.00 | kg/m3 | 318.15 | Excess ... |
| ρl | 1000.36 | kg/m3 | 318.15 | Study o... |
| ρl | 995.70 | kg/m3 | 323.15 | Excess ... |
| ρl | 995.66 | kg/m3 | 323.15 | Thermod... |
| ρl | 995.50 | kg/m3 | 323.15 | Studies... |
| ρl | 995.40 | kg/m3 | 323.15 | Thermop... |
| ρl | 996.43 | kg/m3 | 323.15 | Study o... |
| ρl | 991.40 | kg/m3 | 328.15 | Excess ... |
| ρl | 987.00 | kg/m3 | 333.15 | Excess ... |
| ΔfusS | 39.57 | J/mol×K | 266.80 | NIST |
| csound,fluid | [1548.00; 1657.01] | m/s | [293.15; 323.15] |
|
|
T(K) Speed of sound in fluid (m/s) 1540 1560 1580 1600 1620 1640 1660 300 310 320 | ||||
| csound,fluid | 1657.01 | m/s | 293.15 | Thermod... |
| csound,fluid | 1637.80 | m/s | 298.15 | Thermod... |
| csound,fluid | 1615.00 | m/s | 303.15 | Thermod... |
| csound,fluid | 1619.30 | m/s | 303.15 | Thermod... |
| csound,fluid | 1615.00 | m/s | 303.15 | Thermod... |
| csound,fluid | 1583.00 | m/s | 313.15 | Thermod... |
| csound,fluid | 1581.00 | m/s | 313.15 | Thermod... |
| csound,fluid | 1558.00 | m/s | 323.15 | Thermod... |
| csound,fluid | 1548.00 | m/s | 323.15 | Thermod... |
| γ | 0.04 | N/m | 293.20 | KDB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [344.38; 484.57] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.48032e+01 | |||
| Coefficient B | -3.84464e+03 | |||
| Coefficient C | -7.95140e+01 | |||
| Temperature range, min. | 344.38 | |||
| Temperature range, max. | 484.57 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 1.33 | kPa | 344.38 | Calculated Property |
| Pvap | 2.99 | kPa | 359.96 | Calculated Property |
| Pvap | 6.14 | kPa | 375.53 | Calculated Property |
| Pvap | 11.76 | kPa | 391.11 | Calculated Property |
| Pvap | 21.16 | kPa | 406.69 | Calculated Property |
| Pvap | 36.09 | kPa | 422.26 | Calculated Property |
| Pvap | 58.78 | kPa | 437.84 | Calculated Property |
| Pvap | 91.90 | kPa | 453.42 | Calculated Property |
| Pvap | 138.65 | kPa | 468.99 | Calculated Property |
| Pvap | 202.67 | kPa | 484.57 | Calculated Property |
| Pvap | [3.83e-03; 5226.64] | kPa | [267.13; 699.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.66081e+02 | |||
| Coefficient B | -1.30797e+04 | |||
| Coefficient C | -2.21132e+01 | |||
| Coefficient D | 1.23327e-05 | |||
| Temperature range, min. | 267.13 | |||
| Temperature range, max. | 699.00 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 400 600 | ||||
| Pvap | 3.83e-03 | kPa | 267.13 | Calculated Property |
| Pvap | 0.24 | kPa | 315.12 | Calculated Property |
| Pvap | 3.80 | kPa | 363.10 | Calculated Property |
| Pvap | 25.87 | kPa | 411.09 | Calculated Property |
| Pvap | 104.85 | kPa | 459.07 | Calculated Property |
| Pvap | 305.57 | kPa | 507.06 | Calculated Property |
| Pvap | 721.50 | kPa | 555.04 | Calculated Property |
| Pvap | 1492.58 | kPa | 603.03 | Calculated Property |
| Pvap | 2852.67 | kPa | 651.01 | Calculated Property |
| Pvap | 5226.64 | kPa | 699.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Aniline.
Mixtures
- Aniline + 1-Propanol
- Aniline + Isopropyl Alcohol
- Aniline + 1-Propanol, 2-methyl-
- 2-Propanol, 2-methyl- + Aniline
- Aniline + Cyclohexylamine
- Aniline + Toluene + Water
- Aniline + Octane + Water
- Aniline + Toluene + Cyclohexylamine
- Aniline + Octane + Cyclohexylamine
- Aniline + Cyclohexylamine + Water
- Aniline + Formamide, N,N-dimethyl-
- Aniline + 1-Hexanol
- Aniline + Benzyl alcohol
- Aniline + Methylene chloride
- Aniline + Thiophene, tetrahydro-, 1,1-dioxide
- Diethyl carbonate + Aniline
- Aniline + Propanoic acid, 2-hydroxy-, ethyl ester
- Aniline + Tetrahydrofuran
- 1,3-Dioxolane + Aniline
- Aniline + 2-Pentanol
Find more mixtures with Aniline.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K
- An equipment for dynamic measurements of vapour liquid equilibria and results in binary systems containing cyclohexylamine
- Deuterium isotope effects in liquid liquid phase diagrams of aniline + cyclohexane mixtures
- Vapor liquid equilibria in ternary systems of associating components (water, aniline, cyclohexylamine) and hydrocarbons (octane or toluene)
- Activity coefficients and excess Gibbs energy of binary mixtures of N,N-dimethyl formamide with selected compounds 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
- Liquid-liquid equilibria of {n-heptane + toluene + aniline} ternary system: Experimental data and correlation
- The ionic liquid effect on solubility of aniline, a simple aromatic amine: Perspective of solvents' mixture
- Liquid-liquid equilibria of imidazolium ionic liquids having bistriflamide or triflate anions with aromatic non-polar and polar compounds
- Spectroscopic and ultrasonic studies on the molecular interaction of certain aromatic amines with p-chloranil
- VLE and LLE in ternary systems of two associating components (water, aniline, and cyclohexylamine) and a hydrocarbon (cyclohexane or methylcyclohexane)
- Study on thermo physical properties of binary mixture containing aromatic alcohol with aromatic, substituted aromatic amines at different temperatures interms of FT-IR, 1H NMR spectroscopic and DFT method
- Ternary (liquid + liquid) equilibria for mixtures of (methanol + aniline + n-octane or n-dodecane) at T = 298.15 K
- Volumetric properties of dichloromethane with aniline or nitrobenzene at different temperatures: A theoretical and experimental study
- Volumetric and transport properties of binary liquid mixtures of sulfolane with aniline, N,N-dimethylaniline and N,N-diethylaniline at different temperatures and atmospheric pressure
- Thermodynamic and volumetric behavior of green solvent 1-butyl-3-methylimidazolium tetrafluoroborate with aniline from T = (293.15 to 323.15) K at atmospheric pressure
- Thermophysical and optical studies of molecular interactions in binary mixtures of diethyl carbonate with aromatic compounds at temperatures from 298.15 to 323.15 K
- Comparative studies of intermolecular interaction of aromatic amines with ethyl lactate at different temperatures
- Physicochemical properties of green solvent 1-ethyl-3- methylimidazolium tetrafluoroborate with aniline from T = (293.15 to 323.15) K at atmospheric pressure
- Excess molar volumes and viscosity behaviour of binary mixtures of aniline/or N,N-dimethylaniline with imidazolium ionic liquids having triflate or bistriflamide anion
- Thermodynamic and theoretical investigations on [Emim][Bf4]/[Bmim][Bf4] and aniline binary mixtures
- Topological and thermodynamic investigations of molecular interactions of aniline and o-toluidine with chloroform
- Thermodynamic and acoustic properties of binary mixtures of oxolane with aniline and substituted anilines at 303.15, 313.15 and 323.15 K
- Thermodynamic properties of liquid mixtures containing 1,3-dioxolane and anilines: Excess molar volumes, excess molar enthalpies, excess Gibb's free energy and isentropic compressibilities changes of mixing
- Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
- Vapor Liquid Equilibrium Data for Binary Mixtures of Acetic Acid + Anisole, Acetone + Anisole, and Isopropanol + Anisole at Pressure 96.15 kPa
- Experimental Vapor-Liquid Equilibria and Thermodynamic Modeling of the Methanol + n-Heptane and 1-Butanol + Aniline Binary Systems
- Thermodynamic Interactions Study of Some Ethylene Glycols in Aqueous Aniline Solutions at Different Temperatures: An Acoustical and Volumetric Approach
- Excess Molar Volumes and Deviations in Viscosity of Binary Mixtures of N,N-Dimethylformamide with Aniline and Benzonitrile at (298.15, 303.15, 308.15, and 313.15) K
- Measurement and Correlation of Mutual Solubilities for High Viscosity Binary Systems: Aniline + Methylcyclohexane, Phenol + Heptane, Phenol + Octane, and Glycerol + 1-Pentanol
- Activity Coefficients at Infinite Dilution of Cylcohexylamine + Octane, Toluene, Ethylbenzene, or Aniline and Excess Molar Volumes in Binary Mixtures of Cyclohexylamine + Heptane, Octane, Nonane, Decane, Undecane, Aniline, or Water
- Ternary Liquid-Liquid(-Liquid) Equilibria of Aniline + Cyclohexylamine + Water, Aniline + Cyclohexylamine + Octane, Aniline + Water + Toluene, and Aniline + Water + Octane
- Temperature Dependences of Limiting Activity Coefficients and Henry s Law Constants for Nitrobenzene, Aniline, and Cyclohexylamine in Water
- Thermodynamics of Ketone + Amine Mixtures. Part III. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for 2-Butanone + Aniline, + N-Methylaniline, or + Pyridine Systems
- Thermodynamic Properties of Binary Mixtures of Tetrahydropyran with Anilines at 308.15 K
- Thermodynamic and Acoustic Properties of Binary Mixtures of Ethers. 2. Diisopropyl Ether with Arylamines at (303.15, 313.15, and 323.15) K and Application of ERAS Model to Aniline Mixtures with Diisopropyl Ether and Oxolane
- Thermodynamics of Ketone + Amine Mixtures. Part VIII. Molar Excess Enthalpies at 298.15 K for n-Alkanone + Aniline or + N-Methylaniline Systems
- Determination and Correlation of Pyridazin-3-amine Solubility in Eight Organic Solvents at Temperatures Ranging from (288.05 to 333.35) K
- Excess Heat Capacities of Binary and Ternary Mixtures Containing 1-Ethyl-3-methylimidazolium Tetrafluoroborate and Anilines
- Cloud Point Phenomena in the (Aniline or N,N-Dimethylaniline + Water) Solutions, and Cosolvent Effects of Liquid Poly(ethylene glycol) Addition: Experimental Measurements and Modeling
- Limiting Binary Diffusivities of Aniline, Styrene, and Mesitylene in Supercritical Carbon Dioxide
- High-Pressure Solubility Data of Methane in Aniline and Aqueous Aniline Systems
- Liquid-Liquid Equilibria for Binary System of Ethanol + Hexadecane at Elevated Temperature and the Ternary Systems of Ethanol + Heterocyclic Nitrogen Compounds + Hexadecane at 298.15 K
- Binary Liquid-Liquid Equilibrium (LLE) for N-Methylformamide (NMF) + Hexadecane between (288.15 and 318.15) K and Ternary LLE for Systems of NMF + Heterocyclic Nitrogen Compounds + Hexadecane at 298.15 K
- (Liquid + Liquid) Equilibrium for (N,N-Dimethylformamide (DMF) + Hexadecane) at Temperatures between (293.15 and 313.15) K and Ternary Mixtures of (DMF + Hexadecane) with Either Quinoline, or Pyridine, or Pyrrole, or Aniline, or Indole at T = 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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