Chemical Properties of Aniline (CAS 62-53-3)

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).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• Δ_cH°_solid : Standard solid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• LFL : Lower Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

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°	52.83	kJ/mol	Relay (1.0) 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. Solubility Prediction
log10WS	-0.41		Estimated Solubility
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]
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]
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	194.10	J/mol×K	298.00	NIST
Cp,liquid	193.70	J/mol×K	298.00	NIST
Cp,liquid	192.50	J/mol×K	298.00	NIST
Cp,liquid	191.01	J/mol×K	298.15	NIST
Cp,liquid	192.05	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]
η	0.0043800	Pa×s	293.15	Thermodynamic and theoretical investigations on [Emim][Bf4]/[Bmim][Bf4] and aniline binary mixtures
η	0.0036900	Pa×s	298.15	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
η	0.0032400	Pa×s	303.15	Thermodynamic and theoretical investigations on [Emim][Bf4]/[Bmim][Bf4] and aniline binary mixtures
η	0.0031900	Pa×s	303.15	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
η	0.0028000	Pa×s	308.15	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
η	0.0024700	Pa×s	313.15	Thermodynamic and theoretical investigations on [Emim][Bf4]/[Bmim][Bf4] and aniline binary mixtures
η	0.0024200	Pa×s	313.15	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
η	0.0019500	Pa×s	323.15	Thermodynamic and theoretical investigations on [Emim][Bf4]/[Bmim][Bf4] and aniline binary mixtures
ΔfusH	[10.54; 10.92]	kJ/mol	[266.80; 267.30]
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]
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	45.20 ± 0.20	kJ/mol	424.50	NIST
ΔvapH	42.20 ± 0.40	kJ/mol	424.50	NIST
ΔvapH	48.00 ± 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]
Pvap	0.09	kPa	298.15	Thermodynamic Properties of Binary Mixtures of Tetrahydropyran with Anilines at 308.15 K
Pvap	0.88	kPa	333.15	An equipment for dynamic measurements of vapour liquid equilibria and results in binary systems containing cyclohexylamine
Pvap	3.82	kPa	363.15	An equipment for dynamic measurements of vapour liquid equilibria and results in binary systems containing cyclohexylamine
Pvap	85.00	kPa	450.25	Experimental Vapor-Liquid Equilibria and Thermodynamic Modeling of the Methanol + n-Heptane and 1-Butanol + Aniline Binary Systems
Pvap	96.15	kPa	455.40	Vapor Liquid Equilibrium Data for Binary Mixtures of Acetic Acid + Anisole, Acetone + Anisole, and Isopropanol + Anisole at Pressure 96.15 kPa
n0	[1.58360; 1.59620]		[293.15; 298.15]
n0	1.59620		293.15	Vapor liquid equilibria in ternary systems of associating components (water, aniline, cyclohexylamine) and hydrocarbons (octane or toluene)
n0	1.58620		293.15	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
n0	1.58620		293.15	Ternary Liquid-Liquid(-Liquid) Equilibria of Aniline + Cyclohexylamine + Water, Aniline + Cyclohexylamine + Octane, Aniline + Water + Toluene, and Aniline + Water + Octane
n0	1.58360		298.15	Activity coefficients and excess Gibbs energy of binary mixtures of N,N-dimethyl formamide with selected compounds at 95.5 kPa
ρl	[987.00; 1026.10]	kg/m3	[288.15; 333.15]
ρl	1025.93	kg/m3	288.15	Volumetric properties of dichloromethane with aniline or nitrobenzene at different temperatures: A theoretical and experimental study
ρl	1026.10	kg/m3	288.15	Excess molar volumes and viscosity behaviour of binary mixtures of aniline/or N,N-dimethylaniline with imidazolium ionic liquids having triflate or bistriflamide anion
ρl	1022.00	kg/m3	293.00	KDB
ρl	1021.71	kg/m3	293.15	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
ρl	1021.70	kg/m3	293.15	Excess Heat Capacities of Binary and Ternary Mixtures Containing 1-Ethyl-3-methylimidazolium Tetrafluoroborate and Anilines
ρl	1021.70	kg/m3	293.15	Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρl	1021.70	kg/m3	293.15	Excess molar volumes and viscosity behaviour of binary mixtures of aniline/or N,N-dimethylaniline with imidazolium ionic liquids having triflate or bistriflamide anion
ρl	1021.69	kg/m3	293.15	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
ρl	1021.04	kg/m3	293.15	Volumetric properties of dichloromethane with aniline or nitrobenzene at different temperatures: A theoretical and experimental study
ρl	1017.20	kg/m3	298.15	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
ρl	1017.39	kg/m3	298.15	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
ρl	1017.42	kg/m3	298.15	(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
ρl	1017.42	kg/m3	298.15	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
ρl	1017.40	kg/m3	298.15	Excess molar volumes and viscosity behaviour of binary mixtures of aniline/or N,N-dimethylaniline with imidazolium ionic liquids having triflate or bistriflamide anion
ρl	1017.40	kg/m3	298.15	Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρl	1017.10	kg/m3	298.15	Volumetric properties of dichloromethane with aniline or nitrobenzene at different temperatures: A theoretical and experimental study
ρl	1017.46	kg/m3	298.15	Thermodynamics of Ketone + Amine Mixtures. Part VIII. Molar Excess Enthalpies at 298.15 K for n-Alkanone + Aniline or + N-Methylaniline Systems
ρl	1017.44	kg/m3	298.15	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
ρl	1017.50	kg/m3	298.15	Excess Heat Capacities of Binary and Ternary Mixtures Containing 1-Ethyl-3-methylimidazolium Tetrafluoroborate and Anilines
ρl	1017.38	kg/m3	298.15	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
ρl	1017.30	kg/m3	298.15	Bubble point measurements of binary mixtures formed by 1-hexanol with selected nitro-compounds and substituted benzenes at 95.6 kPa
ρl	1017.10	kg/m3	298.15	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
ρl	1013.00	kg/m3	303.15	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
ρl	1012.78	kg/m3	303.15	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
ρl	1013.04	kg/m3	303.15	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
ρl	1012.70	kg/m3	303.15	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
ρl	1013.17	kg/m3	303.15	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
ρl	1013.10	kg/m3	303.15	Excess Heat Capacities of Binary and Ternary Mixtures Containing 1-Ethyl-3-methylimidazolium Tetrafluoroborate and Anilines
ρl	1013.00	kg/m3	303.15	Excess molar volumes and viscosity behaviour of binary mixtures of aniline/or N,N-dimethylaniline with imidazolium ionic liquids having triflate or bistriflamide anion
ρl	1013.20	kg/m3	303.15	Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρl	1012.81	kg/m3	303.15	Comparative studies of intermolecular interaction of aromatic amines with ethyl lactate at different temperatures
ρl	1012.84	kg/m3	303.15	Volumetric properties of dichloromethane with aniline or nitrobenzene at different temperatures: A theoretical and experimental study
ρl	1008.91	kg/m3	308.15	Comparative studies of intermolecular interaction of aromatic amines with ethyl lactate at different temperatures
ρl	1009.00	kg/m3	308.15	Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρl	1008.90	kg/m3	308.15	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
ρl	1008.70	kg/m3	308.15	Excess Heat Capacities of Binary and Ternary Mixtures Containing 1-Ethyl-3-methylimidazolium Tetrafluoroborate and Anilines
ρl	1008.64	kg/m3	308.15	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
ρl	1008.70	kg/m3	308.15	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
ρl	1008.70	kg/m3	308.15	Excess molar volumes and viscosity behaviour of binary mixtures of aniline/or N,N-dimethylaniline with imidazolium ionic liquids having triflate or bistriflamide anion
ρl	1008.40	kg/m3	308.15	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
ρl	1004.36	kg/m3	313.15	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
ρl	1004.70	kg/m3	313.15	Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρl	1004.10	kg/m3	313.15	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
ρl	1004.40	kg/m3	313.15	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
ρl	1004.59	kg/m3	313.15	Comparative studies of intermolecular interaction of aromatic amines with ethyl lactate at different temperatures
ρl	1004.40	kg/m3	313.15	Excess molar volumes and viscosity behaviour of binary mixtures of aniline/or N,N-dimethylaniline with imidazolium ionic liquids having triflate or bistriflamide anion
ρl	1004.63	kg/m3	313.15	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
ρl	1004.49	kg/m3	313.15	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
ρl	1000.36	kg/m3	318.15	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
ρl	1000.21	kg/m3	318.15	Comparative studies of intermolecular interaction of aromatic amines with ethyl lactate at different temperatures
ρl	1000.40	kg/m3	318.15	Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρl	999.70	kg/m3	318.15	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
ρl	1000.00	kg/m3	318.15	Excess molar volumes and viscosity behaviour of binary mixtures of aniline/or N,N-dimethylaniline with imidazolium ionic liquids having triflate or bistriflamide anion
ρl	1000.36	kg/m3	318.15	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
ρl	995.50	kg/m3	323.15	Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρl	995.40	kg/m3	323.15	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
ρl	995.66	kg/m3	323.15	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
ρl	995.70	kg/m3	323.15	Excess molar volumes and viscosity behaviour of binary mixtures of aniline/or N,N-dimethylaniline with imidazolium ionic liquids having triflate or bistriflamide anion
ρl	996.43	kg/m3	323.15	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
ρl	991.40	kg/m3	328.15	Excess molar volumes and viscosity behaviour of binary mixtures of aniline/or N,N-dimethylaniline with imidazolium ionic liquids having triflate or bistriflamide anion
ρl	987.00	kg/m3	333.15	Excess molar volumes and viscosity behaviour of binary mixtures of aniline/or N,N-dimethylaniline with imidazolium ionic liquids having triflate or bistriflamide anion
ΔfusS	39.57	J/mol×K	266.80	NIST
csound,fluid	[1548.00; 1657.01]	m/s	[293.15; 323.15]
csound,fluid	1657.01	m/s	293.15	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
csound,fluid	1637.80	m/s	298.15	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
csound,fluid	1615.00	m/s	303.15	Thermodynamic and acoustic properties of binary mixtures of oxolane with aniline and substituted anilines at 303.15, 313.15 and 323.15 K
csound,fluid	1619.30	m/s	303.15	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
csound,fluid	1615.00	m/s	303.15	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
csound,fluid	1583.00	m/s	313.15	Thermodynamic and acoustic properties of binary mixtures of oxolane with aniline and substituted anilines at 303.15, 313.15 and 323.15 K
csound,fluid	1581.00	m/s	313.15	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
csound,fluid	1558.00	m/s	323.15	Thermodynamic and acoustic properties of binary mixtures of oxolane with aniline and substituted anilines at 303.15, 313.15 and 323.15 K
csound,fluid	1548.00	m/s	323.15	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
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 Yaws Handbook of Vapor Pressure
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
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 Vapor Pressure Data
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
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
• Cheméo Relay (1.0)
• 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

Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.
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