Chemical Properties of Benzenamine, N,N-dimethyl- (CAS 121-69-7)

InChI

InChI=1S/C8H11N/c1-9(2)8-6-4-3-5-7-8/h3-7H,1-2H3

InChI Key

JLTDJTHDQAWBAV-UHFFFAOYSA-N

Formula

C8H11N

SMILES

CN(C)c1ccccc1

Molecular Weight¹

121.18

CAS

121-69-7

Other Names

• (Dimethylamino)benzene
• Aniline, N,N-dimethyl-
• Dimethylaniline
• Dimethylphenylamine
• Dwumetyloanilina
• N,N-(Dimethylamino)benzene
• N,N-Dimethylbenzeneamine
• N,N-dimethylanilin
• N,N-dimethylaniline
• N,N-dimethylbenzenamine
• N,N-dimethylphenylamine
• NCI-C56428
• NL 63-10P
• NSC 7195
• UN 2253
• Versneller NL 63/10

• 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).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• 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).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• 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.
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_boilr : Boiling point at reduced pressure (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.4049; 0.4110]
ω	0.4049		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.4110		KDB
PAff	941.10	kJ/mol	NIST
BasG	909.20	kJ/mol	NIST
ΔcH°liquid	[-4767.80; -4754.30]	kJ/mol
ΔcH°liquid	-4767.80 ± 3.20	kJ/mol	NIST
ΔcH°liquid	-4754.30	kJ/mol	NIST
μ	1.60	debye	KDB
ΔfG°	231.40	kJ/mol	KDB
ΔfH°gas	[84.10; 100.50]	kJ/mol
ΔfH°gas	84.15	kJ/mol	KDB
ΔfH°gas	100.50 ± 3.40	kJ/mol	NIST
ΔfH°gas	84.10	kJ/mol	NIST
ΔfH°liquid	[34.00; 47.70]	kJ/mol
ΔfH°liquid	47.70 ± 3.40	kJ/mol	NIST
ΔfH°liquid	34.00	kJ/mol	NIST
ΔfusH°	13.54	kJ/mol	Joback Calculated Property
ΔvapH°	[49.80; 52.83]	kJ/mol
ΔvapH°	52.83	kJ/mol	NIST
ΔvapH°	52.83 ± 0.03	kJ/mol	NIST
ΔvapH°	52.80	kJ/mol	NIST
ΔvapH°	52.80 ± 0.10	kJ/mol	NIST
ΔvapH°	49.80	kJ/mol	NIST
ΔvapH°	50.10	kJ/mol	NIST
IE	[7.10; 7.92]	eV
IE	7.12 ± 0.02	eV	NIST
IE	7.15	eV	NIST
IE	7.78	eV	NIST
IE	7.10 ± 0.02	eV	NIST
IE	7.42	eV	NIST
IE	7.11	eV	NIST
IE	7.13 ± 0.04	eV	NIST
IE	7.20	eV	NIST
IE	7.10 ± 0.05	eV	NIST
IE	7.31	eV	NIST
IE	7.20	eV	NIST
IE	7.14 ± 0.03	eV	NIST
IE	7.35	eV	NIST
IE	Outlier 7.92	eV	NIST
IE	7.60	eV	NIST
IE	7.37	eV	NIST
IE	7.51	eV	NIST
log10WS	[-1.92; -1.92]
log10WS	-1.92		Aq. Solubility Prediction
log10WS	-1.92		Estimated Solubility
logPoct/wat	1.753		Crippen Calculated Property
McVol	109.800	ml/mol	McGowan Calculated Property
NFPA Fire	2		KDB
NFPA Health	3		KDB
Pc	[3576.77; 3657.83]	kPa
Pc	3600.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 9 Compiled value
Pc	3627.43	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3630.00	kPa	KDB
Pc	3610.00 ± 91.19	kPa	NIST
Pc	3650.00 ± 91.19	kPa	NIST
Pc	3597.04 ± 151.99	kPa	NIST
Pc	3627.44 ± 151.99	kPa	NIST
Pc	3657.83 ± 151.99	kPa	NIST
Pc	3637.57 ± 151.99	kPa	NIST
Pc	3576.77 ± 151.99	kPa	NIST
Inp	[1061.00; 1104.00]
Inp	1065.40		NIST
Inp	1100.00		NIST
Inp	1083.90		NIST
Inp	1094.50		NIST
Inp	1074.00		NIST
Inp	1087.00		NIST
Inp	1100.00		NIST
Inp	1103.00		NIST
Inp	1065.40		NIST
Inp	1062.37		NIST
Inp	1062.07		NIST
Inp	1063.00		NIST
Inp	1062.71		NIST
Inp	1100.00		NIST
Inp	1104.00		NIST
Inp	1086.00		NIST
Inp	1073.00		NIST
Inp	1062.00		NIST
Inp	1067.00		NIST
Inp	1086.10		NIST
Inp	1073.00		NIST
Inp	1061.00		NIST
Inp	1068.00		NIST
Inp	1080.00		NIST
Inp	1083.90		NIST
Inp	1104.00		NIST
Inp	1068.00		NIST
Ip	[1569.90; 1605.00]
Ip	1569.90		NIST
Ip	1602.00		NIST
Ip	1599.00		NIST
Ip	1603.00		NIST
Ip	1605.00		NIST
Ip	1604.80		NIST
Ip	1603.40		NIST
Ip	1574.00		NIST
Ip	1574.00		NIST
Ip	1569.90		NIST
Ip	1604.80		NIST
Tboil	[462.70; 467.30]	K
Tboil	467.30	K	KDB
Tboil	467.20	K	NIST
Tboil	466.55 ± 0.40	K	NIST
Tboil	467.15 ± 1.50	K	NIST
Tboil	467.20 ± 0.30	K	NIST
Tboil	465.40 ± 0.50	K	NIST
Tboil	467.20 ± 0.30	K	NIST
Tboil	467.20 ± 0.50	K	NIST
Tboil	Outlier 462.70 ± 1.00	K	NIST
Tboil	466.90 ± 1.00	K	NIST
Tboil	466.15 ± 0.50	K	NIST
Tc	[687.00; 688.00]	K
Tc	688.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 9 Compiled value
Tc	687.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	687.00	K	KDB
Tc	687.70 ± 2.00	K	NIST
Tc	687.20 ± 2.00	K	NIST
Tc	687.75 ± 1.00	K	NIST
Tc	687.35 ± 1.50	K	NIST
Tc	687.25 ± 1.50	K	NIST
Tc	687.95 ± 1.00	K	NIST
Tfus	[272.00; 275.75]	K
Tfus	275.40	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	275.60	K	KDB
Tfus	275.53	K	Aq. Solubility Prediction
Tfus	275.65 ± 0.30	K	NIST
Tfus	Outlier 272.00 ± 1.00	K	NIST
Tfus	275.60 ± 0.30	K	NIST
Tfus	275.36 ± 0.25	K	NIST
Tfus	275.75 ± 0.20	K	NIST
Tfus	275.35 ± 0.40	K	NIST
Tfus	274.60 ± 0.14	K	NIST
Tfus	274.15 ± 0.30	K	NIST
Vc	0.400	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[209.60; 214.60]	J/mol×K	[283.00; 302.40]
Cp,liquid	212.10	J/mol×K	283.00	NIST
Cp,liquid	209.60	J/mol×K	289.00	NIST
Cp,liquid	212.10	J/mol×K	298.00	NIST
Cp,liquid	214.60	J/mol×K	302.30	NIST
Cp,liquid	214.60	J/mol×K	302.40	NIST
η	[0.0008259; 0.0016960]	Pa×s	[283.15; 343.15]
η	0.0016960	Pa×s	283.15	Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η	0.0014390	Pa×s	293.15	Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η	0.0011743	Pa×s	303.15	Densities and Viscosities of Binary Mixtures of Propanoic Acid with N,N-Dimethylaniline and N,N-Diethylaniline at T = (303.15, 313.15, and 323.15) K
η	0.0011700	Pa×s	303.15	Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η	0.0009823	Pa×s	313.15	Densities and Viscosities of Binary Mixtures of Propanoic Acid with N,N-Dimethylaniline and N,N-Diethylaniline at T = (303.15, 313.15, and 323.15) K
η	0.0009810	Pa×s	313.15	Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η	0.0008259	Pa×s	323.15	Densities and Viscosities of Binary Mixtures of Propanoic Acid with N,N-Dimethylaniline and N,N-Diethylaniline at T = (303.15, 313.15, and 323.15) K
η	0.0009280	Pa×s	323.15	Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η	0.0009110	Pa×s	333.15	Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η	0.0008410	Pa×s	343.15	Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
ΔfusH	[11.56; 11.56]	kJ/mol	[275.60; 275.60]
ΔfusH	11.56	kJ/mol	275.60	NIST
ΔfusH	11.56	kJ/mol	275.60	NIST
ΔvapH	[44.35; 53.70]	kJ/mol	[303.50; 465.70]
ΔvapH	53.70 ± 0.50	kJ/mol	303.50	NIST
ΔvapH	47.60	kJ/mol	384.50	NIST
ΔvapH	49.20	kJ/mol	390.50	NIST
ΔvapH	44.35	kJ/mol	465.70	NIST
Pvap	[5.16; 8.04]	kPa	[373.70; 384.96]
Pvap	5.16	kPa	373.70	Vapor-Liquid Equilibrium for the Binary System of N,N-Dimethylaniline with 2-Amino-3-methylpyridine
Pvap	8.04	kPa	384.96	Vapor-Liquid Equilibrium for the Binary System of N,N-Dimethylaniline with 2-Amino-3-methylpyridine
ρl	[923.50; 960.60]	kg/m3	[288.15; 333.15]
ρl	960.60	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	956.00	kg/m3	293.00	KDB
ρl	956.50	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	952.05	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	952.30	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	947.70	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	948.18	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	948.20	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	943.50	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	944.10	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	943.55	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	939.78	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	939.40	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	940.00	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	935.30	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	935.90	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	931.45	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	931.80	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	927.70	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	923.50	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
csound,fluid	[1393.00; 1468.00]	m/s	[303.15; 323.15]
csound,fluid	1468.00	m/s	303.15	Thermodynamic and acoustic properties of binary mixtures of ethers. IV. Diisopropyl ether or oxolane with N,N-dimethylaniline or N,Ndiethylaniline at 303.15, 313.15 and 323.15 K
csound,fluid	1431.00	m/s	313.15	Thermodynamic and acoustic properties of binary mixtures of ethers. IV. Diisopropyl ether or oxolane with N,N-dimethylaniline or N,Ndiethylaniline at 303.15, 313.15 and 323.15 K
csound,fluid	1393.00	m/s	323.15	Thermodynamic and acoustic properties of binary mixtures of ethers. IV. Diisopropyl ether or oxolane with N,N-dimethylaniline or N,Ndiethylaniline at 303.15, 313.15 and 323.15 K

Pressure Dependent Properties

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[133.44; 351.56]	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			-4.89800e+01
Coefficient B			8.08840e-01
Coefficient C			-5.55200e-04
Coefficient D			1.46900e-07
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	133.44	J/mol×K	273.00	Calculated Property
Cp,gas	174.19	J/mol×K	353.78	Calculated Property
Cp,gas	209.72	J/mol×K	434.56	Calculated Property
Cp,gas	240.50	J/mol×K	515.33	Calculated Property
Cp,gas	267.01	J/mol×K	596.11	Calculated Property
Cp,gas	289.69	J/mol×K	676.89	Calculated Property
Cp,gas	309.03	J/mol×K	757.67	Calculated Property
Cp,gas	325.47	J/mol×K	838.44	Calculated Property
Cp,gas	339.50	J/mol×K	919.22	Calculated Property
Cp,gas	351.56	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[342.92; 495.81]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.50960e+01
Coefficient B			-4.40969e+03
Coefficient C			-4.51330e+01
Temperature range, min.			342.92
Temperature range, max.			495.81
Pvap	1.33	kPa	342.92	Calculated Property
Pvap	2.97	kPa	359.91	Calculated Property
Pvap	6.08	kPa	376.90	Calculated Property
Pvap	11.61	kPa	393.88	Calculated Property
Pvap	20.88	kPa	410.87	Calculated Property
Pvap	35.67	kPa	427.86	Calculated Property
Pvap	58.20	kPa	444.85	Calculated Property
Pvap	91.25	kPa	461.83	Calculated Property
Pvap	138.12	kPa	478.82	Calculated Property
Pvap	202.63	kPa	495.81	Calculated Property
Pvap	[0.02; 3612.43]	kPa	[275.60; 687.15]	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			4.20032e+01
Coefficient B			-7.05985e+03
Coefficient C			-3.63909e+00
Coefficient D			4.98882e-07
Coefficient E			0.00000e+00
Temperature range, min.			275.60
Temperature range, max.			687.15
Pvap	0.02	kPa	275.60	Calculated Property
Pvap	0.40	kPa	321.33	Calculated Property
Pvap	3.84	kPa	367.06	Calculated Property
Pvap	21.48	kPa	412.78	Calculated Property
Pvap	82.31	kPa	458.51	Calculated Property
Pvap	240.53	kPa	504.24	Calculated Property
Pvap	575.43	kPa	549.97	Calculated Property
Pvap	1183.22	kPa	595.69	Calculated Property
Pvap	2164.57	kPa	641.42	Calculated Property
Pvap	3612.43	kPa	687.15	Calculated Property
Pvap	[0.14; 100.88]	kPa	[302.70; 466.30]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.57267e+01
Coefficient B			-4.87512e+03
Coefficient C			-2.76060e+01
Reference			Stull, 1947
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			302.70
Temperature range, max.			466.30
Pvap	0.14	kPa	302.70	Calculated Property
Pvap	0.41	kPa	320.88	Calculated Property
Pvap	1.08	kPa	339.06	Calculated Property
Pvap	2.55	kPa	357.23	Calculated Property
Pvap	5.53	kPa	375.41	Calculated Property
Pvap	11.09	kPa	393.59	Calculated Property
Pvap	20.83	kPa	411.77	Calculated Property
Pvap	36.96	kPa	429.94	Calculated Property
Pvap	62.40	kPa	448.12	Calculated Property
Pvap	100.88	kPa	466.30	Calculated Property
Pvap	[1.39; 110.22]	kPa	[344.17; 469.93]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.57662e+01
Coefficient B			-4.91026e+03
Coefficient C			-2.61160e+01
Reference			Nelson and Wales, 1925
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			344.17
Temperature range, max.			469.93
Pvap	1.39	kPa	344.17	Calculated Property
Pvap	2.66	kPa	358.14	Calculated Property
Pvap	4.83	kPa	372.12	Calculated Property
Pvap	8.38	kPa	386.09	Calculated Property
Pvap	13.95	kPa	400.06	Calculated Property
Pvap	22.38	kPa	414.04	Calculated Property
Pvap	34.76	kPa	428.01	Calculated Property
Pvap	52.40	kPa	441.98	Calculated Property
Pvap	76.92	kPa	455.96	Calculated Property
Pvap	110.22	kPa	469.93	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.02]	N/m	[275.65; 467.15]	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			6.67934e-02
Coefficient B			-1.04900e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			275.65
Temperature range, max.			467.15
γ	0.04	N/m	275.65	Calculated Property
γ	0.04	N/m	296.93	Calculated Property
γ	0.03	N/m	318.21	Calculated Property
γ	0.03	N/m	339.48	Calculated Property
γ	0.03	N/m	360.76	Calculated Property
γ	0.03	N/m	382.04	Calculated Property
γ	0.02	N/m	403.32	Calculated Property
γ	0.02	N/m	424.59	Calculated Property
γ	0.02	N/m	445.87	Calculated Property
γ	0.02	N/m	467.15	Calculated Property

Similar Compounds

Find more compounds similar to Benzenamine, N,N-dimethyl-.

Mixtures

• Diisopropyl ether + Benzenamine, N,N-dimethyl-
• Benzenamine, N,N-dimethyl- + Tetrahydrofuran
• Benzyl alcohol + Benzenamine, N,N-dimethyl-
• Benzenamine, N,N-dimethyl- + Dimethyl Sulfoxide
• n-Hexane + Benzenamine, N,N-dimethyl- + Acetophenone
• n-Hexane + Benzenamine, N,N-dimethyl- + Ethanone, 1-(4-chlorophenyl)-
• n-Hexane + Benzenamine, N,N-dimethyl- + Ethanone, 1-(4-methylphenyl)-
• Benzenamine, N,N-dimethyl- + Thiophene, tetrahydro-, 1,1-dioxide
• Benzenamine, N,N-dimethyl- + Water
• Benzenamine, N,N-dimethyl- + Propanoic acid
• Benzenamine, N,N-dimethyl- + 1-Hexanol
• Benzenamine, N,N-dimethyl- + 1,4-Dioxane
• Benzenamine, N,N-dimethyl- + 1-Hexanol + 1,4-Dioxane
• 2-Pyridinamine, 3-methyl- + Benzenamine, N,N-dimethyl-

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
• Spectroscopic and ultrasonic studies on the molecular interaction of certain aromatic amines with p-chloranil
• 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
• 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
• 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 acoustic properties of binary mixtures of ethers. IV. Diisopropyl ether or oxolane with N,N-dimethylaniline or N,Ndiethylaniline at 303.15, 313.15 and 323.15 K
• THERMODYNAMIC PROPERTIES OF DONOR ACCEPTOR COMPLEXES OF TERTIARY AMINE WITH ARYL KETONES IN HEXANE MEDIUM
• Vapor-Liquid Equilibrium for the Binary System of N,N-Dimethylaniline with 2-Amino-3-methylpyridine
• Densities and Viscosities of Binary Mixtures of Propanoic Acid with N,N-Dimethylaniline and N,N-Diethylaniline at T = (303.15, 313.15, and 323.15) K
• Solute Partitioning Between 1-n-Butyl-3-methylimidazolium Trifluoromethanesulfonate Ionic Liquid and Supercritical CO2
• 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
• Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) 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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