Chemical Properties of BENZENAMINE, 2-METHYL- (CAS 95-53-4)

InChI

InChI=1S/C7H9N/c1-6-4-2-3-5-7(6)8/h2-5H,8H2,1H3

InChI Key

RNVCVTLRINQCPJ-UHFFFAOYSA-N

Formula

C7H9N

SMILES

Cc1ccccc1N

Molecular Weight¹

107.16

CAS

95-53-4

Other Names

• (2-methylphenyl)amine
• 1-Methyl-2-aminobenzene
• 1-amino-2-methylbenzene
• 2-amino-1-methylbenzene
• 2-aminotoluene
• 2-methyl-1-aminobenzene
• 2-methylaniline
• 2-methylbenzenamine
• 2-methylphenylamine
• 2-toluidine
• Aniline, 2-methyl-
• C.I. 37077
• NSC 15348
• Rcra waste number U328
• o-Aminotoluene
• o-Methylaniline
• o-Methylbenzenamine
• o-Toluide
• o-Toluidin
• o-Toluidyna
• o-Tolylamine
• o-toluidine
• ortho-aminotoluene
• ortho-methylaniline
• ortho-methylbenzenamine
• ortho-toluidine
• ortho-tolylamine

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid 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).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• 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).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (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.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.4017		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
PAff	890.90	kJ/mol	NIST
BasG	859.10	kJ/mol	NIST
ΔcH°liquid	[-4064.00; -4034.00]	kJ/mol
ΔcH°liquid	-4036.09 ± 0.88	kJ/mol	NIST
ΔcH°liquid	-4034.00	kJ/mol	NIST
ΔcH°liquid	-4064.00	kJ/mol	NIST
ΔfG°	177.29	kJ/mol	Joback Calculated Property
ΔfH°gas	[51.40; 54.80]	kJ/mol
ΔfH°gas	53.20 ± 0.50	kJ/mol	NIST
ΔfH°gas	54.80	kJ/mol	NIST
ΔfH°gas	51.40	kJ/mol	NIST
ΔfH°liquid	[-6.49; -4.72]	kJ/mol
ΔfH°liquid	-4.72 ± 0.96	kJ/mol	NIST
ΔfH°liquid	-6.49	kJ/mol	NIST
ΔfusH°	12.73	kJ/mol	Joback Calculated Property
ΔvapH°	[44.10; 63.10]	kJ/mol
ΔvapH°	57.30 ± 0.20	kJ/mol	NIST
ΔvapH°	57.90 ± 0.24	kJ/mol	NIST
ΔvapH°	57.90	kJ/mol	NIST
ΔvapH°	62.70 ± 0.50	kJ/mol	NIST
ΔvapH°	Outlier 44.10	kJ/mol	NIST
ΔvapH°	63.10	kJ/mol	NIST
ΔvapH°	56.20	kJ/mol	NIST
IE	[7.44; 7.84]	eV
IE	7.47 ± 0.04	eV	NIST
IE	7.58	eV	NIST
IE	7.45 ± 0.02	eV	NIST
IE	7.52	eV	NIST
IE	7.44 ± 0.02	eV	NIST
IE	7.60 ± 0.10	eV	NIST
IE	7.70 ± 0.10	eV	NIST
IE	7.69	eV	NIST
IE	7.75	eV	NIST
IE	7.84	eV	NIST
IE	7.83	eV	NIST
IE	7.83	eV	NIST
log10WS	[-2.21; -0.85]
log10WS	-0.85		Aq. Solubility Prediction
log10WS	-2.21		Estimated Solubility
logPoct/wat	1.577		Crippen Calculated Property
McVol	95.710	ml/mol	McGowan Calculated Property
Pc	[3749.02; 4700.00]	kPa
Pc	4700.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 9 Compiled value
Pc	4650.82	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3749.02 ± 253.31	kPa	NIST
Inp	[176.52; 1072.00]
Inp	1032.70		NIST
Inp	1040.50		NIST
Inp	1068.00		NIST
Inp	1072.00		NIST
Inp	1068.00		NIST
Inp	1068.00		NIST
Inp	1053.90		NIST
Inp	1053.90		NIST
Inp	1037.00		NIST
Inp	176.52		NIST
Inp	177.86		NIST
Inp	176.65		NIST
Inp	1053.90		NIST
Inp	1032.70		NIST
Inp	1068.00		NIST
Inp	176.52		NIST
Ip	[1789.00; 1814.00]
Ip	1796.00		NIST
Ip	1807.00		NIST
Ip	1808.00		NIST
Ip	1814.00		NIST
Ip	1789.00		NIST
Ip	1800.00		NIST
Ip	1796.00		NIST
Ip	1789.00		NIST
Tboil	[469.70; 473.85]	K
Tboil	473.40	K	NIST
Tboil	473.35 ± 0.50	K	NIST
Tboil	473.35 ± 0.30	K	NIST
Tboil	470.40 ± 0.50	K	NIST
Tboil	473.45 ± 0.07	K	NIST
Tboil	473.50 ± 0.30	K	NIST
Tboil	473.55 ± 0.30	K	NIST
Tboil	472.45 ± 0.60	K	NIST
Tboil	473.45 ± 0.30	K	NIST
Tboil	472.99 ± 0.20	K	NIST
Tboil	473.30 ± 0.50	K	NIST
Tboil	472.85 ± 0.50	K	NIST
Tboil	471.35 ± 0.30	K	NIST
Tboil	473.85 ± 0.20	K	NIST
Tboil	Outlier 469.70 ± 1.00	K	NIST
Tboil	472.65 ± 0.60	K	NIST
Tc	[694.15; 717.00]	K
Tc	717.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 9 Compiled value
Tc	710.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	694.15 ± 2.00	K	NIST
Tfus	[245.50; 257.70]	K
Tfus	253.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	253.55	K	Aq. Solubility Prediction
Tfus	250.00 ± 0.20	K	NIST
Tfus	249.50 ± 0.02	K	NIST
Tfus	257.70 ± 0.60	K	NIST
Tfus	256.75 ± 0.50	K	NIST
Tfus	249.47 ± 0.05	K	NIST
Tfus	256.75 ± 0.30	K	NIST
Tfus	245.50 ± 0.40	K	NIST
Tfus	256.90 ± 0.30	K	NIST
Tfus	248.75 ± 0.30	K	NIST
Tfus	248.75 ± 0.20	K	NIST
Ttriple	[258.73; 258.73]	K
Ttriple	258.73 ± 0.01	K	NIST
Ttriple	258.73 ± 0.01	K	NIST
Vc	[0.343; 0.346]	m3/kmol
Vc	0.346	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 9 Compiled value
Vc	0.343	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Zc	0.2730000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 9 Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[164.40; 211.30]	J/mol×K	[288.00; 303.15]
Cp,liquid	201.70	J/mol×K	288.00	NIST
Cp,liquid	211.30	J/mol×K	298.00	NIST
Cp,liquid	209.60	J/mol×K	302.50	NIST
Cp,liquid	209.60	J/mol×K	302.50	NIST
Cp,liquid	164.40	J/mol×K	303.15	NIST
ΔfusH	[8.08; 11.66]	kJ/mol	[249.55; 287.60]
ΔfusH	8.10	kJ/mol	249.55	NIST
ΔfusH	8.08	kJ/mol	249.60	NIST
ΔfusH	11.66	kJ/mol	287.60	NIST
ΔfusH	11.66	kJ/mol	287.60	NIST
ΔfusH	11.66	kJ/mol	287.60	NIST
ΔfusH	11.66	kJ/mol	287.60	NIST
ΔvapH	[42.70; 57.80]	kJ/mol	[403.50; 432.50]
ΔvapH	51.50	kJ/mol	403.50	NIST
ΔvapH	54.50	kJ/mol	403.50	NIST
ΔvapH	51.50	kJ/mol	403.50	NIST
ΔvapH	48.60	kJ/mol	403.50	NIST
ΔvapH	45.70	kJ/mol	403.50	NIST
ΔvapH	42.70	kJ/mol	403.50	NIST
ΔvapH	57.80	kJ/mol	403.50	NIST
ΔvapH	54.50	kJ/mol	403.50	NIST
ΔvapH	57.80	kJ/mol	403.50	NIST
ΔvapH	48.60	kJ/mol	403.50	NIST
ΔvapH	45.70	kJ/mol	403.50	NIST
ΔvapH	42.70	kJ/mol	403.50	NIST
ΔvapH	50.00	kJ/mol	432.50	NIST
Pvap	0.04	kPa	298.15	Thermodynamic Properties of Binary Mixtures of Tetrahydropyran with Anilines at 308.15 K
ρl	[986.06; 998.43]	kg/m3	[293.15; 308.15]
ρl	998.43	kg/m3	293.15	Thermodynamic Properties of Ternary Mixtures Containing Ionic Liquid and Organic Liquids: Excess Molar Volume and Excess Isentropic Compressibility
ρl	998.40	kg/m3	293.15	Excess Heat Capacities of Binary and Ternary Mixtures Containing 1-Ethyl-3-methylimidazolium Tetrafluoroborate and Anilines
ρl	994.28	kg/m3	298.15	Topological and thermodynamic investigations of binary mixtures: Molar excess volumes, molar excess enthalpies and isentropic compressibility changes of mixing
ρl	994.34	kg/m3	298.15	Thermodynamics of mixtures containing amines VI. Liquid liquid equilibria for mixtures of o-toluidine + selected alkanes
ρl	994.20	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	994.35	kg/m3	298.15	Thermodynamic and topological investigations of ternary mixtures with o-toluidine, tetrahydropyran, and picolines: Excess molar volume and excess isentropic compressibility
ρl	994.36	kg/m3	298.15	Thermodynamic Properties of Ternary Mixtures Containing Ionic Liquid and Organic Liquids: Excess Molar Volume and Excess Isentropic Compressibility
ρl	994.35	kg/m3	298.15	Thermodynamic studies of molecular interactions in mixtures of o-toulidine with pyridine and picolines: Excess molar volumes, excess molar enthalpies, and excess isentropic compressibilities
ρl	994.40	kg/m3	298.15	Excess Heat Capacities of Binary and Ternary Mixtures Containing 1-Ethyl-3-methylimidazolium Tetrafluoroborate and Anilines
ρl	994.28	kg/m3	298.15	Molar Excess Volumes and Excess Isentropic Compressibilities of Ternary Mixtures of o-Toluidine
ρl	994.28	kg/m3	298.15	Molar Excess Volumes and Excess Isentropic Compressibilities of {2-Methylaniline (i) + Benzene (j) + Methylbenzene}, {2-Methylaniline (i) + Benzene (j) + 1,2-Dimethylbenzene (k)}, and {2-Methylaniline (i) + Benzene (j) + 1,4-Dimethylbenzene (k)} at T = 308.15 K
ρl	990.23	kg/m3	303.15	Thermodynamic Properties of Ternary Mixtures Containing Ionic Liquid and Organic Liquids: Excess Molar Volume and Excess Isentropic Compressibility
ρl	990.20	kg/m3	303.15	Excess Heat Capacities of Binary and Ternary Mixtures Containing 1-Ethyl-3-methylimidazolium Tetrafluoroborate and Anilines
ρl	986.06	kg/m3	308.15	Thermodynamic Properties of Ternary Mixtures Containing Ionic Liquid and Organic Liquids: Excess Molar Volume and Excess Isentropic Compressibility
ρl	986.10	kg/m3	308.15	Excess Heat Capacities of Binary and Ternary Mixtures Containing 1-Ethyl-3-methylimidazolium Tetrafluoroborate and Anilines
ΔfusS	32.00	J/mol×K	249.55	NIST
csound,fluid	[1501.00; 1602.60]	m/s	[298.15; 323.15]
csound,fluid	1602.60	m/s	298.15	Topological investigations of molecular interactions of binary and ternary mixtures containing tetrahydropyran, o-toluidine and N-methyl formamide
csound,fluid	1579.00	m/s	303.15	Thermodynamic and acoustic properties of binary mixtures of ethers. III. Diisopropyl ether or oxolane with o- or m-toluidines at 303.15, 313.15 and 323.15 K
csound,fluid	1577.80	m/s	303.15	Topological investigations of molecular interactions of binary and ternary mixtures containing tetrahydropyran, o-toluidine and N-methyl formamide
csound,fluid	1558.38	m/s	308.15	Topological investigations of molecular interactions of binary and ternary mixtures containing tetrahydropyran, o-toluidine and N-methyl formamide
csound,fluid	1558.40	m/s	308.15	Topological investigations of molecular interactions of binary and ternary mixtures containing tetrahydropyran, o-toluidine and N-methyl formamide
csound,fluid	1539.00	m/s	313.15	Thermodynamic and acoustic properties of binary mixtures of ethers. III. Diisopropyl ether or oxolane with o- or m-toluidines at 303.15, 313.15 and 323.15 K
csound,fluid	1501.00	m/s	323.15	Thermodynamic and acoustic properties of binary mixtures of ethers. III. Diisopropyl ether or oxolane with o- or m-toluidines at 303.15, 313.15 and 323.15 K

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[119.65; 294.87]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			-1.65900e+01
Coefficient B			5.92320e-01
Coefficient C			-3.64560e-04
Coefficient D			8.37000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	119.65	J/mol×K	273.00	Calculated Property
Cp,gas	151.04	J/mol×K	353.78	Calculated Property
Cp,gas	178.83	J/mol×K	434.56	Calculated Property
Cp,gas	203.29	J/mol×K	515.33	Calculated Property
Cp,gas	224.68	J/mol×K	596.11	Calculated Property
Cp,gas	243.27	J/mol×K	676.89	Calculated Property
Cp,gas	259.32	J/mol×K	757.67	Calculated Property
Cp,gas	273.09	J/mol×K	838.44	Calculated Property
Cp,gas	284.85	J/mol×K	919.22	Calculated Property
Cp,gas	294.87	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[2.25e-04; 3812.83]	kPa	[249.47; 694.15]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			1.43007e+02
Coefficient B			-1.23010e+04
Coefficient C			-1.86082e+01
Coefficient D			9.77089e-06
Coefficient E			0.00000e+00
Temperature range, min.			249.47
Temperature range, max.			694.15
Pvap	2.25e-04	kPa	249.47	Calculated Property
Pvap	0.04	kPa	298.88	Calculated Property
Pvap	0.96	kPa	348.29	Calculated Property
Pvap	9.38	kPa	397.70	Calculated Property
Pvap	48.68	kPa	447.11	Calculated Property
Pvap	168.72	kPa	496.51	Calculated Property
Pvap	449.65	kPa	545.92	Calculated Property
Pvap	1009.54	kPa	595.33	Calculated Property
Pvap	2029.90	kPa	644.74	Calculated Property
Pvap	3812.83	kPa	694.15	Calculated Property
Pvap	[7.59; 101.39]	kPa	[391.61; 473.50]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42569e+01
Coefficient B			-3.72381e+03
Coefficient C			-8.71260e+01
Reference			Dreisbach and Shrader, 1949
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			391.61
Temperature range, max.			473.50
Pvap	7.59	kPa	391.61	Calculated Property
Pvap	10.82	kPa	400.71	Calculated Property
Pvap	15.13	kPa	409.81	Calculated Property
Pvap	20.76	kPa	418.91	Calculated Property
Pvap	28.01	kPa	428.01	Calculated Property
Pvap	37.22	kPa	437.10	Calculated Property
Pvap	48.73	kPa	446.20	Calculated Property
Pvap	62.97	kPa	455.30	Calculated Property
Pvap	80.37	kPa	464.40	Calculated Property
Pvap	101.39	kPa	473.50	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.02]	N/m	[256.65; 473.15]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			7.27526e-02
Coefficient B			-1.09400e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			256.65
Temperature range, max.			473.15
γ	0.04	N/m	256.65	Calculated Property
γ	0.04	N/m	280.71	Calculated Property
γ	0.04	N/m	304.76	Calculated Property
γ	0.04	N/m	328.82	Calculated Property
γ	0.03	N/m	352.87	Calculated Property
γ	0.03	N/m	376.93	Calculated Property
γ	0.03	N/m	400.98	Calculated Property
γ	0.03	N/m	425.04	Calculated Property
γ	0.02	N/m	449.09	Calculated Property
γ	0.02	N/m	473.15	Calculated Property

Similar Compounds

Find more compounds similar to BENZENAMINE, 2-METHYL-.

Mixtures

• BENZENAMINE, 2-METHYL- + Cyclohexane
• n-Hexane + BENZENAMINE, 2-METHYL-
• BENZENAMINE, 2-METHYL- + Heptane
• Trichloromethane + BENZENAMINE, 2-METHYL-
• Benzene + BENZENAMINE, 2-METHYL- + 1,4-Dioxane
• Toluene + BENZENAMINE, 2-METHYL- + 1,4-Dioxane
• Benzene, 1,3-dimethyl- + BENZENAMINE, 2-METHYL- + 1,4-Dioxane
• p-Xylene + BENZENAMINE, 2-METHYL- + 1,4-Dioxane
• Tetrahydropyran + Pyridine, 2-methyl- + BENZENAMINE, 2-METHYL-
• Tetrahydropyran + BENZENAMINE, 2-METHYL- + Pyridine, 3-methyl-
• Pyridine, 4-methyl- + Tetrahydropyran + BENZENAMINE, 2-METHYL-
• Tetrahydropyran + Pyridine + BENZENAMINE, 2-METHYL-
• Benzene + Tetrahydropyran + BENZENAMINE, 2-METHYL-
• Toluene + Tetrahydropyran + BENZENAMINE, 2-METHYL-
• BENZENAMINE, 2-METHYL- + Dimethyl Sulfoxide
• Tetrahydropyran + BENZENAMINE, 2-METHYL-
• BENZENAMINE, 2-METHYL- + Formamide, N-methyl-
• Benzene + BENZENAMINE, 2-METHYL-
• Toluene + BENZENAMINE, 2-METHYL-
• BENZENAMINE, 2-METHYL- + o-Xylene

Find more mixtures with BENZENAMINE, 2-METHYL-.

Sources

• KDB Vapor Pressure Data
• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 9 ChEDL chemicals 1.5.2, from Marsh, K. N.; Young, C. L.; Morton, D. W.; Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 9. Organic Compounds Containing Nitrogen. J. Chem. Eng. Data 2006, 51, 305-314.
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• Crippen Method
• Thermodynamics of mixtures containing amines VI. Liquid liquid equilibria for mixtures of o-toluidine + selected alkanes
• Spectroscopic and ultrasonic studies on the molecular interaction of certain aromatic amines with p-chloranil
• Heat capacities of aqueous polar aromatic compounds over a wide range of conditions. Part I: phenol, cresols, aniline, and toluidines
• Thermodynamic studies of molecular interactions in mixtures of o-toulidine with pyridine and picolines: Excess molar volumes, excess molar enthalpies, and excess isentropic compressibilities
• Thermodynamic and topological investigations of ternary mixtures with o-toluidine, tetrahydropyran, and picolines: Excess molar volume and excess isentropic compressibility
• Molecular interactions in binary mixtures containing o-toluidine
• Topological and thermodynamic investigations of molecular interactions of aniline and o-toluidine with chloroform
• Topological and thermodynamic investigations of binary mixtures: Molar excess volumes, molar excess enthalpies and isentropic compressibility changes of mixing
• 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
• Thermodynamic and acoustic properties of binary mixtures of ethers. III. Diisopropyl ether or oxolane with o- or m-toluidines at 303.15, 313.15 and 323.15 K
• Topological investigations of molecular interactions of binary and ternary mixtures containing tetrahydropyran, o-toluidine and N-methyl formamide
• Excess Molar Enthalpies for Binary and Ternary Mixtures containing Cyclic Ether, 2-Methylaniline and Aromatic Hydrocarbons
• Excess molar enthalpies of ternary mixtures containing o-toluidine + tetrahydropyran with pyridine or isomeric picolines or benzene or toluene at 308.15K
• Excess molar enthalpies of ternary mixtures containing1-ethyl-3-methylimidazolium tetrafluoroborate and organic solvents
• Thermodynamic Properties of Binary Mixtures of Tetrahydropyran with Anilines at 308.15 K
• Thermodynamic Properties of Ternary Mixtures Containing Ionic Liquid and Organic Liquids: Excess Molar Volume and Excess Isentropic Compressibility
• Excess Heat Capacities of Binary and Ternary Mixtures Containing 1-Ethyl-3-methylimidazolium Tetrafluoroborate and Anilines
• Molar Excess Volumes and Excess Isentropic Compressibilities of Ternary Mixtures of o-Toluidine
• Molar Excess Volumes and Excess Isentropic Compressibilities of {2-Methylaniline (i) + Benzene (j) + Methylbenzene}, {2-Methylaniline (i) + Benzene (j) + 1,2-Dimethylbenzene (k)}, and {2-Methylaniline (i) + Benzene (j) + 1,4-Dimethylbenzene (k)} at T = 308.15 K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook

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