Chemical Properties of 1-Butanamine (CAS 109-73-9)

InChI

InChI=1S/C4H11N/c1-2-3-4-5/h2-5H2,1H3

InChI Key

HQABUPZFAYXKJW-UHFFFAOYSA-N

Formula

C4H11N

SMILES

CCCCN

Molecular Weight¹

73.14

CAS

109-73-9

Other Names

• 1-Amino-butaan
• 1-Aminobutan
• 1-Butylamine
• 1-aminobutane
• Butanamine
• Mono-n-butylamine
• Monobutilamina
• N-Butylamin
• NSC 8029
• Norralamine
• Norvalamine
• UN 1125
• butylamine
• monobutylamine
• n-Butilamina
• n-C4H9NH2
• n-butylamine

• 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).
• ε_r : Dielectric Constant (Relative permittivity).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper 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).
• 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_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.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• 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_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• V_m : Molar Volume (m³/mol).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.3290; 0.3960]
ω	0.3960		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.3290		KDB
PAff	921.50	kJ/mol	NIST
Tig	[585.15; 585.37]	K
Tig	585.37	K	KDB
Tig	585.15	K	NCMS SOLV-DB
BasG	886.60	kJ/mol	NIST
ΔcH°liquid	[-3018.50; -2984.00]	kJ/mol
ΔcH°liquid	-3018.50 ± 1.10	kJ/mol	NIST
ΔcH°liquid	-2984.00	kJ/mol	NIST
ΔcH°solid	-3018.00	kJ/mol	NIST
μ	1.30	debye	KDB
η	[0.0004760; 0.0004930]	Pa×s
η	0.0004760	Pa×s	A volumetric and viscosity study for the binary mixtures of 1-hexyl-3-methylimidazolium tetrafluoroborate with some molecular solvents
η	0.0004930	Pa×s	Excess Molar Volumes and Viscosity Deviations of Binary Liquid Mixtures of 1,3-Dioxolane and 1,4-Dioxane with Butyl Acetate, Butyric Acid, Butylamine, and 2-Butanone at 298.15 K
εr	4.88		NCMS SOLV-DB
LFL	1.70	% in Air	KDB
UFL	9.80	% in Air	KDB
Tflash,cc	[261.15; 272.04]	K
Tflash,cc	272.04	K	KDB
Tflash,cc	261.15	K	NCMS SOLV-DB
Tflash,oc	260.93	K	KDB
ΔfG°	49.24	kJ/mol	KDB
ΔfH°gas	[-149.30; -92.11]	kJ/mol
ΔfH°gas	-92.11	kJ/mol	KDB
ΔfH°gas	-95.00 ± 2.00	kJ/mol	NIST
ΔfH°gas	-149.30	kJ/mol	NIST
ΔfH°liquid	[-182.00; -127.70]	kJ/mol
ΔfH°liquid	-127.70 ± 1.20	kJ/mol	NIST
ΔfH°liquid	-182.00	kJ/mol	NIST
ΔfusH°	11.31	kJ/mol	Joback Calculated Property
ΔvapH°	[27.20; 36.00]	kJ/mol
ΔvapH°	35.73	kJ/mol	NCMS SOLV-DB
ΔvapH°	35.84	kJ/mol	NIST
ΔvapH°	35.60	kJ/mol	NIST
ΔvapH°	36.00	kJ/mol	NIST
ΔvapH°	35.70 ± 0.20	kJ/mol	NIST
ΔvapH°	35.70 ± 0.10	kJ/mol	NIST
ΔvapH°	35.70 ± 0.10	kJ/mol	NIST
ΔvapH°	35.71 ± 0.06	kJ/mol	NIST
ΔvapH°	33.00 ± 1.00	kJ/mol	NIST
ΔvapH°	32.70	kJ/mol	NIST
ΔvapH°	Outlier 27.20	kJ/mol	NIST
IE	[8.70; 9.40]	eV
IE	8.73 ± 0.04	eV	NIST
IE	8.70	eV	NIST
IE	8.79	eV	NIST
IE	8.71 ± 0.03	eV	NIST
IE	9.40	eV	NIST
log10WS	-0.37		Relay (1.0) Calculated Property
logPoct/wat	0.970		NCMS SOLV-DB
McVol	77.200	ml/mol	McGowan Calculated Property
NFPA Fire	[%!d(float64=3); %!d(float64=3)]
NFPA Fire	3		KDB
NFPA Fire	3		NCMS SOLV-DB
NFPA Health	[%!d(float64=2); %!d(float64=2)]
NFPA Health	2		KDB
NFPA Health	2		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
Pc	[4154.32; 4250.00]	kPa
Pc	4200.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 9 Compiled value
Pc	4154.32	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4250.00	kPa	KDB
Pc	4200.00 ± 41.96	kPa	NIST
Pc	4154.33 ± 1.50	kPa	NIST
Inp	[608.00; 629.00]
Inp	609.40		NIST
Inp	609.40		NIST
Inp	610.00		NIST
Inp	629.00		NIST
Inp	629.00		NIST
Inp	621.00		NIST
Inp	619.00		NIST
Inp	617.00		NIST
Inp	614.00		NIST
Inp	608.00		NIST
Inp	626.00		NIST
Inp	626.00		NIST
Inp	628.00		NIST
Inp	628.00		NIST
Inp	628.00		NIST
Inp	627.00		NIST
Inp	609.40		NIST
Inp	621.00		NIST
Inp	608.00		NIST
Ip	[886.00; 918.00]
Ip	896.00		NIST
Ip	890.00		NIST
Ip	918.00		NIST
Ip	912.00		NIST
Ip	886.00		NIST
Ip	904.00		NIST
Ip	908.00		NIST
Ip	908.00		NIST
Ip	896.00		NIST
Ip	904.00		NIST
Tboil	[336.15; 351.20]	K
Tboil	350.00	K	Evolution of the Liquid Vapor Equilibrium Properties of Several Unsymmetrical Amines: Determination of Their Binary Isobaric Diagrams and Applications to the Distillation
Tboil	350.15	K	KDB
Tboil	350.22	K	NCMS SOLV-DB
Tboil	351.00	K	NIST
Tboil	350.00	K	NIST
Tboil	350.20	K	NIST
Tboil	351.00 ± 2.00	K	NIST
Tboil	350.12 ± 0.20	K	NIST
Tboil	350.55	K	NIST
Tboil	349.95 ± 0.50	K	NIST
Tboil	350.70 ± 0.30	K	NIST
Tboil	351.20 ± 0.30	K	NIST
Tboil	351.15 ± 0.80	K	NIST
Tboil	351.15 ± 1.50	K	NIST
Tboil	350.15 ± 1.00	K	NIST
Tboil	350.95 ± 1.00	K	NIST
Tboil	349.65 ± 3.00	K	NIST
Tboil	350.95 ± 0.50	K	NIST
Tboil	350.65 ± 0.60	K	NIST
Tboil	350.45 ± 0.20	K	NIST
Tboil	351.15 ± 1.00	K	NIST
Tboil	350.65 ± 2.00	K	NIST
Tboil	350.96 ± 0.20	K	NIST
Tboil	350.65 ± 4.00	K	NIST
Tboil	351.15 ± 2.00	K	NIST
Tboil	350.65 ± 1.00	K	NIST
Tboil	349.15 ± 2.00	K	NIST
Tboil	Outlier 336.15 ± 8.00	K	NIST
Tboil	349.65 ± 4.00	K	NIST
Tboil	349.65 ± 4.00	K	NIST
Tboil	Outlier 336.65 ± 7.00	K	NIST
Tc	[524.00; 531.90]	K
Tc	531.90	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 9 Compiled value
Tc	524.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	531.90	K	KDB
Tc	524.00	K	NIST
Tc	531.90 ± 0.53	K	NIST
Tc	524.15 ± 1.50	K	NIST
Tfus	[222.65; 224.15]	K
Tfus	224.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	224.05	K	KDB
Tfus	224.05	K	NCMS SOLV-DB
Tfus	224.00 ± 0.10	K	NIST
Tfus	224.05	K	NIST
Tfus	Outlier 222.65 ± 0.50	K	NIST
Vc	[0.277; 0.288]	m3/kmol
Vc	0.288	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.277	m3/kmol	KDB
Vm	9.99e-05	m3/mol	Thermodynamic study of (heptane + amine) mixtures. II. Excess and partial molar volumes at 298.15 K
Zc	0.2661960		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	188.00	J/mol×K	298.15	NIST
η	[0.0003600; 0.0005780]	Pa×s	[293.15; 323.15]
η	0.0005250	Pa×s	293.15	Relative Permittivity, Viscosity, and Speed of Sound for 2-Methoxyethanol + Butylamine Mixtures
η	0.0004960	Pa×s	298.15	Relative Permittivity, Viscosity, and Speed of Sound for 2-Methoxyethanol + Butylamine Mixtures
η	0.0005780	Pa×s	298.15	NCMS SOLV-DB
η	0.0004440	Pa×s	303.15	Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
η	0.0004670	Pa×s	303.15	Relative Permittivity, Viscosity, and Speed of Sound for 2-Methoxyethanol + Butylamine Mixtures
η	0.0004600	Pa×s	303.15	Density and Viscosity Measurement of n-Butylamine with Hexyl Alcohol Isomer Binary Systems
η	0.0003930	Pa×s	313.15	Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
η	0.0004000	Pa×s	313.15	Density and Viscosity Measurement of n-Butylamine with Hexyl Alcohol Isomer Binary Systems
η	0.0003600	Pa×s	323.15	Density and Viscosity Measurement of n-Butylamine with Hexyl Alcohol Isomer Binary Systems
ΔvapH	[31.10; 35.50]	kJ/mol	[313.00; 358.00]
ΔvapH	34.70 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	35.20	kJ/mol	320.50	NIST
ΔvapH	35.50	kJ/mol	322.50	NIST
ΔvapH	33.50 ± 0.10	kJ/mol	323.00	NIST
ΔvapH	34.70	kJ/mol	331.50	NIST
ΔvapH	32.40 ± 0.10	kJ/mol	343.00	NIST
ΔvapH	32.09	kJ/mol	350.10	KDB
ΔvapH	31.81	kJ/mol	350.20	NIST
ΔvapH	31.10 ± 0.10	kJ/mol	358.00	NIST
Pvap	[12.23; 101.33]	kPa	[298.15; 350.00]
Pvap	12.23	kPa	298.15	NCMS SOLV-DB
Pvap	19.99	kPa	308.30	Evolution of the Liquid Vapor Equilibrium Properties of Several Unsymmetrical Amines: Determination of Their Binary Isobaric Diagrams and Applications to the Distillation
Pvap	26.66	kPa	314.70	Evolution of the Liquid Vapor Equilibrium Properties of Several Unsymmetrical Amines: Determination of Their Binary Isobaric Diagrams and Applications to the Distillation
Pvap	33.33	kPa	319.90	Evolution of the Liquid Vapor Equilibrium Properties of Several Unsymmetrical Amines: Determination of Their Binary Isobaric Diagrams and Applications to the Distillation
Pvap	46.66	kPa	328.20	Evolution of the Liquid Vapor Equilibrium Properties of Several Unsymmetrical Amines: Determination of Their Binary Isobaric Diagrams and Applications to the Distillation
Pvap	59.99	kPa	334.80	Evolution of the Liquid Vapor Equilibrium Properties of Several Unsymmetrical Amines: Determination of Their Binary Isobaric Diagrams and Applications to the Distillation
Pvap	66.66	kPa	337.90	Evolution of the Liquid Vapor Equilibrium Properties of Several Unsymmetrical Amines: Determination of Their Binary Isobaric Diagrams and Applications to the Distillation
Pvap	86.66	kPa	345.10	Evolution of the Liquid Vapor Equilibrium Properties of Several Unsymmetrical Amines: Determination of Their Binary Isobaric Diagrams and Applications to the Distillation
Pvap	101.33	kPa	350.00	Evolution of the Liquid Vapor Equilibrium Properties of Several Unsymmetrical Amines: Determination of Their Binary Isobaric Diagrams and Applications to the Distillation
n0	1.39900		298.15	NCMS SOLV-DB
ρl	[709.21; 741.72]	kg/m3	[288.15; 323.15]
ρl	741.72	kg/m3	288.15	Volumetric behaviour of binary mixtures of (trichloromethane + amines) at temperatures between T = (288.15 and 303.15) K at p = 0.1 MPa
ρl	739.00	kg/m3	293.00	KDB
ρl	737.12	kg/m3	293.15	Volumetric properties of binary mixtures of (acetonitrile + amines) at several temperatures with application of the ERAS model
ρl	736.95	kg/m3	293.15	Volumetric behaviour of binary mixtures of (trichloromethane + amines) at temperatures between T = (288.15 and 303.15) K at p = 0.1 MPa
ρl	737.05	kg/m3	293.15	Thermodynamics of amide + amine mixtures. 1. Volumetric, speed of sound, and refractive index data for N,Ndimethylformamide + N-propylpropan-1-amine, + N-butylbutan-1-amine, + butan-1-amine, or + hexan-1-amine systems at several temperatures
ρl	732.15	kg/m3	298.15	Volumetric behaviour of binary mixtures of (trichloromethane + amines) at temperatures between T = (288.15 and 303.15) K at p = 0.1 MPa
ρl	733.30	kg/m3	298.15	Volumetric, acoustic, viscometric, and spectroscopic properties for binary properties for binary mixtures of alkoxypropanol with mono, di-, and tri- alkylamines at a temperature of 298.15K
ρl	732.18	kg/m3	298.15	Thermodynamics of amide + amine mixtures. 5. Excess molar enthalpies of N,N-dimethylformamide or N,N-dimethylacetamide + N-propylpropan-1-amine, + N-butylbutan-1-amine, + butan-1-amine, or + hexan-1-amine systems at 298.15 K. Application of the ERAS model
ρl	732.33	kg/m3	298.15	Volumetric properties of binary mixtures of (acetonitrile + amines) at several temperatures with application of the ERAS model
ρl	733.33	kg/m3	298.15	Excess Molar Properties for Binary Systems of CnMIM-BF4 Ionic Liquids with Alkylamines in the Temperature Range (298.15 to 318.15) K. Experimental Results and Theoretical Model Calculations
ρl	732.23	kg/m3	298.15	Thermodynamics of amide + amine mixtures. 1. Volumetric, speed of sound, and refractive index data for N,Ndimethylformamide + N-propylpropan-1-amine, + N-butylbutan-1-amine, + butan-1-amine, or + hexan-1-amine systems at several temperatures
ρl	733.33	kg/m3	298.15	Binary mixtures of ([C4mim][NTf2] + molecular organic solvents): Thermophysical, acoustic and transport properties at various compositions and temperatures
ρl	734.65	kg/m3	298.15	Volumetric properties for binary and ternary systems consist of 1-chlorobutane, n-butylamine and isobutanol at 298.15 K with application of the Prigogine-Flory-Patterson theory and ERAS-Model
ρl	728.65	kg/m3	303.15	Studies of viscosities of dilute solutions of alkylamines in non-electrolyte solvents III. Alkylamines in butanols 303.15K
ρl	727.51	kg/m3	303.15	Volumetric properties of binary mixtures of (acetonitrile + amines) at several temperatures with application of the ERAS model
ρl	727.34	kg/m3	303.15	Volumetric behaviour of binary mixtures of (trichloromethane + amines) at temperatures between T = (288.15 and 303.15) K at p = 0.1 MPa
ρl	728.65	kg/m3	303.15	Studies of partial molar volumes of alkylamine in non-electrolyte solvents I. Alkylamines in hydrocarbons at 303.15 and 313.15K
ρl	727.45	kg/m3	303.15	Thermodynamics of amide + amine mixtures. 1. Volumetric, speed of sound, and refractive index data for N,Ndimethylformamide + N-propylpropan-1-amine, + N-butylbutan-1-amine, + butan-1-amine, or + hexan-1-amine systems at several temperatures
ρl	728.50	kg/m3	303.15	Binary mixtures of ([C4mim][NTf2] + molecular organic solvents): Thermophysical, acoustic and transport properties at various compositions and temperatures
ρl	723.67	kg/m3	308.15	Binary mixtures of ([C4mim][NTf2] + molecular organic solvents): Thermophysical, acoustic and transport properties at various compositions and temperatures
ρl	722.66	kg/m3	308.15	Volumetric properties of binary mixtures of (acetonitrile + amines) at several temperatures with application of the ERAS model
ρl	723.67	kg/m3	308.15	Excess Molar Properties for Binary Systems of CnMIM-BF4 Ionic Liquids with Alkylamines in the Temperature Range (298.15 to 318.15) K. Experimental Results and Theoretical Model Calculations
ρl	718.66	kg/m3	313.15	Binary mixtures of ([C4mim][NTf2] + molecular organic solvents): Thermophysical, acoustic and transport properties at various compositions and temperatures
ρl	719.17	kg/m3	313.15	Studies of partial molar volumes of alkylamine in non-electrolyte solvents I. Alkylamines in hydrocarbons at 303.15 and 313.15K
ρl	714.10	kg/m3	318.15	Binary mixtures of ([C4mim][NTf2] + molecular organic solvents): Thermophysical, acoustic and transport properties at various compositions and temperatures
ρl	714.00	kg/m3	318.15	Excess Molar Properties for Binary Systems of CnMIM-BF4 Ionic Liquids with Alkylamines in the Temperature Range (298.15 to 318.15) K. Experimental Results and Theoretical Model Calculations
ρl	709.21	kg/m3	323.15	Binary mixtures of ([C4mim][NTf2] + molecular organic solvents): Thermophysical, acoustic and transport properties at various compositions and temperatures
csound,fluid	[1205.72; 1296.08]	m/s	[288.15; 308.15]
csound,fluid	1296.08	m/s	288.15	Volumetric and Acoustic Properties for Binary Mixtures of Dipropylene Glycol Monopropyl Ether with Alkylamines at Temperatures Between 288.15 K and 308.15 K
csound,fluid	1296.08	m/s	288.15	Densities, Excess Molar Volumes, Speeds of Sound, and Isothermal Compressibilities for 2-(2-Hexyloxyethoxy)ethanol + n-Alkylamine at Temperatures Between 288.15 K and 308.15 K
csound,fluid	1273.56	m/s	293.15	Volumetric and Acoustic Properties for Binary Mixtures of Dipropylene Glycol Monopropyl Ether with Alkylamines at Temperatures Between 288.15 K and 308.15 K
csound,fluid	1273.56	m/s	293.15	Densities, Excess Molar Volumes, Speeds of Sound, and Isothermal Compressibilities for 2-(2-Hexyloxyethoxy)ethanol + n-Alkylamine at Temperatures Between 288.15 K and 308.15 K
csound,fluid	1249.96	m/s	298.15	Volumetric and Acoustic Properties for Binary Mixtures of Dipropylene Glycol Monopropyl Ether with Alkylamines at Temperatures Between 288.15 K and 308.15 K
csound,fluid	1249.96	m/s	298.15	Densities, Excess Molar Volumes, Speeds of Sound, and Isothermal Compressibilities for 2-(2-Hexyloxyethoxy)ethanol + n-Alkylamine at Temperatures Between 288.15 K and 308.15 K
csound,fluid	1228.92	m/s	303.15	Volumetric and Acoustic Properties for Binary Mixtures of Dipropylene Glycol Monopropyl Ether with Alkylamines at Temperatures Between 288.15 K and 308.15 K
csound,fluid	1228.92	m/s	303.15	Densities, Excess Molar Volumes, Speeds of Sound, and Isothermal Compressibilities for 2-(2-Hexyloxyethoxy)ethanol + n-Alkylamine at Temperatures Between 288.15 K and 308.15 K
csound,fluid	1205.72	m/s	308.15	Volumetric and Acoustic Properties for Binary Mixtures of Dipropylene Glycol Monopropyl Ether with Alkylamines at Temperatures Between 288.15 K and 308.15 K
csound,fluid	1205.72	m/s	308.15	Densities, Excess Molar Volumes, Speeds of Sound, and Isothermal Compressibilities for 2-(2-Hexyloxyethoxy)ethanol + n-Alkylamine at Temperatures Between 288.15 K and 308.15 K
γ	[0.02; 0.02]	N/m	[293.20; 298.15]
γ	0.02	N/m	293.20	KDB
γ	0.02	N/m	298.15	NCMS SOLV-DB

Datasets

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.15	101.33	0.0004
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[110.71; 261.66]	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			5.74300e+00
Coefficient B			4.45720e-01
Coefficient C			-2.37200e-04
Coefficient D			4.74000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	110.71	J/mol×K	273.00	Calculated Property
Cp,gas	135.84	J/mol×K	353.78	Calculated Property
Cp,gas	158.53	J/mol×K	434.56	Calculated Property
Cp,gas	178.93	J/mol×K	515.33	Calculated Property
Cp,gas	197.19	J/mol×K	596.11	Calculated Property
Cp,gas	213.47	J/mol×K	676.89	Calculated Property
Cp,gas	227.90	J/mol×K	757.67	Calculated Property
Cp,gas	240.64	J/mol×K	838.44	Calculated Property
Cp,gas	251.85	J/mol×K	919.22	Calculated Property
Cp,gas	261.66	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[258.47; 373.87]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.45389e+01
Coefficient B			-3.02088e+03
Coefficient C			-4.64950e+01
Temperature range, min.			258.47
Temperature range, max.			373.87
Pvap	1.33	kPa	258.47	Calculated Property
Pvap	3.01	kPa	271.29	Calculated Property
Pvap	6.21	kPa	284.11	Calculated Property
Pvap	11.90	kPa	296.94	Calculated Property
Pvap	21.42	kPa	309.76	Calculated Property
Pvap	36.49	kPa	322.58	Calculated Property
Pvap	59.31	kPa	335.40	Calculated Property
Pvap	92.49	kPa	348.23	Calculated Property
Pvap	139.10	kPa	361.05	Calculated Property
Pvap	202.63	kPa	373.87	Calculated Property
Pvap	[0.08; 4205.44]	kPa	[224.05; 531.90]	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			5.84534e+01
Coefficient B			-6.04187e+03
Coefficient C			-6.30480e+00
Coefficient D			2.90389e-06
Coefficient E			0.00000e+00
Temperature range, min.			224.05
Temperature range, max.			531.90
Pvap	0.08	kPa	224.05	Calculated Property
Pvap	1.27	kPa	258.26	Calculated Property
Pvap	9.42	kPa	292.46	Calculated Property
Pvap	43.36	kPa	326.67	Calculated Property
Pvap	143.05	kPa	360.87	Calculated Property
Pvap	371.25	kPa	395.08	Calculated Property
Pvap	807.37	kPa	429.28	Calculated Property
Pvap	1537.32	kPa	463.49	Calculated Property
Pvap	2644.55	kPa	497.69	Calculated Property
Pvap	4205.44	kPa	531.90	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.02]	N/m	[223.15; 350.15]	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			5.68874e-02
Coefficient B			-1.12200e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			223.15
Temperature range, max.			350.15
γ	0.03	N/m	223.15	Calculated Property
γ	0.03	N/m	237.26	Calculated Property
γ	0.03	N/m	251.37	Calculated Property
γ	0.03	N/m	265.48	Calculated Property
γ	0.03	N/m	279.59	Calculated Property
γ	0.02	N/m	293.71	Calculated Property
γ	0.02	N/m	307.82	Calculated Property
γ	0.02	N/m	321.93	Calculated Property
γ	0.02	N/m	336.04	Calculated Property
γ	0.02	N/m	350.15	Calculated Property

Similar Compounds

Find more compounds similar to 1-Butanamine.

Mixtures

• 1-Butanamine + 1,4-Dioxane
• 1-Butanamine + Tetrahydrofuran
• 1-Butanamine + Heptane
• 1-Butanamine + Water
• Trichloromethane + 1-Butanamine
• 1-Butanamine + Carbon Tetrachloride
• 1-Butanamine + Formamide, N,N-dimethyl-
• 1-Butanamine + N,N-Dimethylacetamide
• 1-Butanamine + Butane, 1-chloro-
• 1-Butanamine + 1-Propanol, 2-methyl-
• 1-Butanamine + Butane, 1-chloro- + 1-Propanol, 2-methyl-
• 1-Butanamine + Methyl Alcohol
• 1-Butanamine + Acetonitrile
• 1-Butanamine + 1-Butanol
• 1-Butanamine + Cyclohexane
• Benzene + 1-Butanamine
• 1-Butanamine + 1-(1-methyl-2-propoxyethoxy)-2-propanol
• 1-Butanamine + 2-Hexanol
• 3-Hexanol + 1-Butanamine
• 1-Butanamine + 1-Pentanol, 2-methyl-

Find more mixtures with 1-Butanamine.

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.
• Cheméo Relay (1.0)
• Crippen Method
• Volumetric and Acoustic Properties for Binary Mixtures of Dipropylene Glycol Monopropyl Ether with Alkylamines at Temperatures Between 288.15 K and 308.15 K
• Establishing benchmarks for the Second Industrial Fluids Simulation Challenge
• Thermodynamic study of heptane + amine mixtures. V. Excess and solvation Gibbs energies
• Thermodynamics of amide + amine mixtures. 5. Excess molar enthalpies of N,N-dimethylformamide or N,N-dimethylacetamide + N-propylpropan-1-amine, + N-butylbutan-1-amine, + butan-1-amine, or + hexan-1-amine systems at 298.15 K. Application of the ERAS model
• Volumetric, acoustic, viscometric, and spectroscopic properties for binary properties for binary mixtures of alkoxypropanol with mono, di-, and tri- alkylamines at a temperature of 298.15K
• Volumetric behaviour of binary mixtures of (trichloromethane + amines) at temperatures between T = (288.15 and 303.15) K at p = 0.1 MPa
• Thermodynamic study of (heptane + amine) mixtures. II. Excess and partial molar volumes at 298.15 K
• A volumetric and viscosity study for the binary mixtures of 1-hexyl-3-methylimidazolium tetrafluoroborate with some molecular solvents
• Volumetric properties of binary mixtures of (acetonitrile + amines) at several temperatures with application of the ERAS model
• Binary mixtures of ([C4mim][NTf2] + molecular organic solvents): Thermophysical, acoustic and transport properties at various compositions and temperatures
• Thermodynamics of amide + amine mixtures. 4. Relative permittivities of N,N-dimethylacetamide + N-propylpropan-1-amine, + N-butylbutan-1-amine, + butan-1-amine, or + hexan-1-amine systems and of N,N-dimethylformamide + aniline mixture at several temperatures. Characterization of amine + amide systems using ERAS
• Improving the method of solution calorimetry for evaluation of the enthalpies of phase transitions and condensed state enthalpies of formation
• Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
• Studies of partial molar volumes of alkylamine in non-electrolyte solvents I. Alkylamines in hydrocarbons at 303.15 and 313.15K
• Studies of viscosities of dilute solutions of alkylamines in non-electrolyte solvents III. Alkylamines in butanols 303.15K
• Studies of viscosities of dilute solutions of alkylamines in non-electrolyte solvents: IV. Alkylamines in 1,4-dioxane and oxolane at 303.15K
• Volumetric properties for binary and ternary systems consist of 1-chlorobutane, n-butylamine and isobutanol at 298.15 K with application of the Prigogine-Flory-Patterson theory and ERAS-Model
• Thermodynamic functions of hydrogen bonding of amines in methanol: head space analysis and solution calorimetry
• Enthalpies of solution and enthalpies of solvation of organic solutes in ethylene glycol at 298.15 K: Prediction and analysis of intermolecular interaction contributions
• Thermodynamics of amide + amine mixtures. 1. Volumetric, speed of sound, and refractive index data for N,Ndimethylformamide + N-propylpropan-1-amine, + N-butylbutan-1-amine, + butan-1-amine, or + hexan-1-amine systems at several temperatures
• Relative Permittivity, Viscosity, and Speed of Sound for 2-Methoxyethanol + Butylamine Mixtures
• Density and Viscosity Measurement of n-Butylamine with Hexyl Alcohol Isomer Binary Systems
• Excess Molar Volumes and Viscosity Deviations of Binary Liquid Mixtures of 1,3-Dioxolane and 1,4-Dioxane with Butyl Acetate, Butyric Acid, Butylamine, and 2-Butanone at 298.15 K
• Thermodynamic Parameters of Anionic Surfactant-Additive Systems at the Cloud Point
• Evolution of the Liquid Vapor Equilibrium Properties of Several Unsymmetrical Amines: Determination of Their Binary Isobaric Diagrams and Applications to the Distillation
• Excess Molar Properties for Binary Systems of CnMIM-BF4 Ionic Liquids with Alkylamines in the Temperature Range (298.15 to 318.15) K. Experimental Results and Theoretical Model Calculations
• Densities, Excess Molar Volumes, Speeds of Sound, and Isothermal Compressibilities for 2-(2-Hexyloxyethoxy)ethanol + n-Alkylamine at Temperatures Between 288.15 K and 308.15 K
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

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