Chemical Properties of sec-Butylamine (CAS 13952-84-6)

InChI

InChI=1S/C4H11N/c1-3-4(2)5/h4H,3,5H2,1-2H3

InChI Key

BHRZNVHARXXAHW-UHFFFAOYSA-N

Formula

C4H11N

SMILES

CCC(C)N

Molecular Weight¹

73.14

CAS

13952-84-6

Other Names

• (.+/-.)-sec-Butylamine
• (RS)-2-aminobutane
• (RS)-sec-butylamine
• 1-Methylpropanamine
• 1-Methylpropylamine
• 1-methyl-1-propanamine
• 2-AB
• 2-Aminobutane base
• 2-Butanamine, (.+/-.)-
• 2-Butylamine
• 2-aminobutane
• 2-butanamine
• Butafume
• Deccotane
• Frucote
• NSC 8030
• Propylamine, 1-Methyl-
• Secondary butylamine
• Tutane
• sec-Butanamine
• sec-C4H9NH2

• 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).
• 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).
• 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.
• 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	0.2998		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
PAff	929.70	kJ/mol	NIST
BasG	895.70	kJ/mol	NIST
ΔcH°liquid	[-3008.60; -2979.00]	kJ/mol
ΔcH°liquid	-3008.60 ± 0.92	kJ/mol	NIST
ΔcH°liquid	-2979.00	kJ/mol	NIST
ΔfG°	46.81	kJ/mol	Joback Calculated Property
ΔfH°gas	[-155.50; -106.00]	kJ/mol
ΔfH°gas	-106.00 ± 2.00	kJ/mol	NIST
ΔfH°gas	-155.50	kJ/mol	NIST
ΔfH°liquid	[-187.00; -137.50]	kJ/mol
ΔfH°liquid	-137.50 ± 1.00	kJ/mol	NIST
ΔfH°liquid	-187.00	kJ/mol	NIST
ΔfusH°	7.79	kJ/mol	Joback Calculated Property
ΔvapH°	[31.00; 32.70]	kJ/mol
ΔvapH°	32.70 ± 0.10	kJ/mol	NIST
ΔvapH°	32.60 ± 0.10	kJ/mol	NIST
ΔvapH°	32.64 ± 0.06	kJ/mol	NIST
ΔvapH°	31.00 ± 1.00	kJ/mol	NIST
ΔvapH°	31.50	kJ/mol	NIST
IE	[8.50; 8.70]	eV
IE	8.50 ± 0.10	eV	NIST
IE	8.70	eV	NIST
log10WS	-0.41		Relay (1.0) Calculated Property
logPoct/wat	0.744		Crippen Calculated Property
McVol	77.200	ml/mol	McGowan Calculated Property
Pc	[3969.99; 5000.00]	kPa
Pc	5000.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 9 Compiled value
Pc	3969.99	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4200.00	kPa	KDB
Pc	5000.00 ± 499.79	kPa	NIST
Inp	[471.00; 527.00]
Inp	471.00		NIST
Inp	527.00		NIST
Inp	517.00		NIST
Inp	515.00		NIST
Inp	471.00		NIST
Inp	471.00		NIST
Inp	471.00		NIST
Ip	[815.00; 864.00]
Ip	826.00		NIST
Ip	821.00		NIST
Ip	825.00		NIST
Ip	815.00		NIST
Ip	816.00		NIST
Ip	Outlier 864.00		NIST
Tboil	[335.88; 336.70]	K
Tboil	335.88	K	KDB
Tboil	Outlier 336.70	K	NIST
Tboil	336.00	K	NIST
Tboil	336.15 ± 1.50	K	NIST
Tboil	336.15 ± 2.00	K	NIST
Tboil	336.15 ± 2.00	K	NIST
Tc	[511.00; 514.30]	K
Tc	514.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 9 Compiled value
Tc	511.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	514.30	K	KDB
Tc	514.30 ± 0.51	K	NIST
Tfus	[168.60; 169.15]	K
Tfus	169.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	168.60	K	KDB
Tfus	168.65 ± 0.60	K	NIST
Vc	[0.278; 0.282]	m3/kmol
Vc	0.282	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.278	m3/kmol	KDB
Vm	1.02e-04	m3/mol	Thermodynamic study of (heptane + amine) mixtures. II. Excess and partial molar volumes at 298.15 K
Zc	0.2730490		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[29.40; 34.10]	kJ/mol	[313.00; 343.00]
ΔvapH	31.60 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	34.10	kJ/mol	317.50	NIST
ΔvapH	32.40	kJ/mol	317.50	NIST
ΔvapH	30.50 ± 0.10	kJ/mol	328.00	NIST
ΔvapH	29.40 ± 0.10	kJ/mol	343.00	NIST
Pvap	[6.80; 232.69]	kPa	[274.06; 363.15]
Pvap	6.81	kPa	274.06	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	6.80	kPa	274.09	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	11.46	kPa	283.91	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	18.43	kPa	293.15	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	19.21	kPa	293.88	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	19.21	kPa	293.88	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	29.11	kPa	303.15	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	30.03	kPa	303.84	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	30.04	kPa	303.84	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	44.25	kPa	313.15	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	45.47	kPa	313.81	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	45.38	kPa	313.81	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	65.05	kPa	323.15	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	66.77	kPa	323.92	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	92.82	kPa	333.15	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	95.10	kPa	333.91	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	95.08	kPa	333.91	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	95.07	kPa	333.91	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	128.99	kPa	343.15	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	132.05	kPa	343.86	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	132.05	kPa	343.86	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	132.08	kPa	343.86	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	175.09	kPa	353.15	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	179.16	kPa	353.90	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	178.99	kPa	353.90	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
Pvap	232.69	kPa	363.15	Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
ρl	[712.73; 727.87]	kg/m3	[288.15; 303.15]
ρl	727.87	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	722.86	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	717.81	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	712.73	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

Datasets

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	725.3
293.15	10000.00	733.6
293.15	20000.00	741.2
293.15	30000.00	748.1
293.15	40000.00	754.5
293.15	50000.00	760.4
293.15	60000.00	766.1
293.15	70000.00	771.3
293.15	80000.00	776.3
293.15	90000.00	781.1
293.15	100000.00	785.5
293.15	110000.00	789.7
293.15	120000.00	793.9
293.15	130000.00	797.8
293.15	140000.00	801.5
303.15	100.00	715.1
303.15	10000.00	724.3
303.15	20000.00	732.4
303.15	30000.00	739.7
303.15	40000.00	746.3
303.15	50000.00	752.5
303.15	60000.00	758.3
303.15	70000.00	763.7
303.15	80000.00	768.9
303.15	90000.00	773.8
303.15	100000.00	778.4
303.15	110000.00	782.9
303.15	120000.00	787.2
303.15	130000.00	791.2
303.15	140000.00	795.2
313.15	100.00	705.0
313.15	10000.00	714.8
313.15	20000.00	723.4
313.15	30000.00	731.1
313.15	40000.00	738.2
313.15	50000.00	744.7
313.15	60000.00	750.8
313.15	70000.00	756.5
313.15	80000.00	761.9
313.15	90000.00	767.0
313.15	100000.00	771.8
313.15	110000.00	776.4
313.15	120000.00	780.8
313.15	130000.00	785.1
313.15	140000.00	789.1
323.15	100.00	694.7
323.15	10000.00	705.4
323.15	20000.00	714.5
323.15	30000.00	722.8
323.15	40000.00	730.4
323.15	50000.00	737.2
323.15	60000.00	743.6
323.15	70000.00	749.5
323.15	80000.00	755.2
323.15	90000.00	760.4
323.15	100000.00	765.4
323.15	110000.00	770.2
323.15	120000.00	774.7
323.15	130000.00	779.0
323.15	140000.00	783.2
333.15	10000.00	695.4
333.15	20000.00	705.2
333.15	30000.00	714.0
333.15	40000.00	722.0
333.15	50000.00	729.2
333.15	60000.00	735.8
333.15	70000.00	742.1
333.15	80000.00	748.0
333.15	90000.00	753.4
333.15	100000.00	758.6
333.15	110000.00	763.5
333.15	120000.00	768.1
333.15	130000.00	772.5
333.15	140000.00	776.9
343.15	10000.00	685.9
343.15	20000.00	696.6
343.15	30000.00	706.0
343.15	40000.00	714.3
343.15	50000.00	721.9
343.15	60000.00	728.8
343.15	70000.00	735.3
343.15	80000.00	741.3
343.15	90000.00	747.1
343.15	100000.00	752.4
343.15	110000.00	757.4
343.15	120000.00	762.3
343.15	130000.00	767.0
343.15	140000.00	771.3
353.15	10000.00	675.8
353.15	20000.00	687.1
353.15	30000.00	697.2
353.15	40000.00	705.8
353.15	50000.00	714.0
353.15	60000.00	721.2
353.15	70000.00	728.0
353.15	80000.00	734.2
353.15	90000.00	740.1
353.15	100000.00	745.7
353.15	110000.00	751.0
353.15	120000.00	756.0
353.15	130000.00	760.7
353.15	140000.00	765.3
363.15	10000.00	665.7
363.15	20000.00	678.0
363.15	30000.00	688.5
363.15	40000.00	697.8
363.15	50000.00	706.2
363.15	60000.00	713.9
363.15	70000.00	721.0
363.15	80000.00	727.5
363.15	90000.00	733.6
363.15	100000.00	739.4
363.15	110000.00	744.8
363.15	120000.00	749.9
363.15	130000.00	754.8
363.15	140000.00	759.5
373.15	10000.00	655.5
373.15	20000.00	668.9
373.15	30000.00	680.1
373.15	40000.00	690.0
373.15	50000.00	698.2
373.15	60000.00	707.0
373.15	70000.00	714.0
373.15	80000.00	720.9
373.15	90000.00	727.2
373.15	100000.00	733.2
373.15	110000.00	738.7
373.15	120000.00	744.0
373.15	130000.00	749.1
373.15	140000.00	753.9
383.15	10000.00	645.5
383.15	20000.00	659.9
383.15	30000.00	671.9
383.15	40000.00	682.3
383.15	50000.00	691.4
383.15	60000.00	699.6
383.15	70000.00	707.3
383.15	80000.00	714.4
383.15	90000.00	720.8
383.15	100000.00	726.9
383.15	110000.00	732.7
383.15	120000.00	738.2
383.15	130000.00	743.3
383.15	140000.00	748.2
393.15	10000.00	634.9
393.15	20000.00	650.5
393.15	30000.00	663.1
393.15	40000.00	674.3
393.15	50000.00	684.3
393.15	60000.00	693.0
393.15	70000.00	700.9
393.15	80000.00	708.2
393.15	90000.00	714.9
393.15	100000.00	721.2
393.15	110000.00	727.2
393.15	120000.00	732.8
393.15	130000.00	738.1
393.15	140000.00	742.9
403.15	10000.00	623.9
403.15	20000.00	640.6
403.15	30000.00	654.5
403.15	40000.00	666.1
403.15	50000.00	676.3
403.15	60000.00	685.3
403.15	70000.00	693.6
403.15	80000.00	701.1
403.15	90000.00	708.2
403.15	100000.00	714.9
403.15	110000.00	721.1
403.15	120000.00	726.9
403.15	130000.00	732.3
403.15	140000.00	737.4
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[110.40; 262.20]	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			4.06100e+00
Coefficient B			4.51640e-01
Coefficient C			-2.40400e-04
Coefficient D			4.69000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	110.40	J/mol×K	273.00	Calculated Property
Cp,gas	135.83	J/mol×K	353.78	Calculated Property
Cp,gas	158.78	J/mol×K	434.56	Calculated Property
Cp,gas	179.38	J/mol×K	515.33	Calculated Property
Cp,gas	197.80	J/mol×K	596.11	Calculated Property
Cp,gas	214.17	J/mol×K	676.89	Calculated Property
Cp,gas	228.65	J/mol×K	757.67	Calculated Property
Cp,gas	241.38	J/mol×K	838.44	Calculated Property
Cp,gas	252.52	J/mol×K	919.22	Calculated Property
Cp,gas	262.20	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[250.70; 357.25]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.55051e+01
Coefficient B			-3.28970e+03
Coefficient C			-3.45250e+01
Temperature range, min.			250.70
Temperature range, max.			357.25
Pvap	1.33	kPa	250.70	Calculated Property
Pvap	2.94	kPa	262.54	Calculated Property
Pvap	5.99	kPa	274.38	Calculated Property
Pvap	11.41	kPa	286.22	Calculated Property
Pvap	20.53	kPa	298.06	Calculated Property
Pvap	35.11	kPa	309.89	Calculated Property
Pvap	57.46	kPa	321.73	Calculated Property
Pvap	90.42	kPa	333.57	Calculated Property
Pvap	137.47	kPa	345.41	Calculated Property
Pvap	202.66	kPa	357.25	Calculated Property
Pvap	[4.04e-04; 3922.51]	kPa	[168.65; 514.30]	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			5.75882e+01
Coefficient B			-5.56943e+03
Coefficient C			-6.33708e+00
Coefficient D			4.07040e-06
Coefficient E			0.00000e+00
Temperature range, min.			168.65
Temperature range, max.			514.30
Pvap	4.04e-04	kPa	168.65	Calculated Property
Pvap	0.05	kPa	207.06	Calculated Property
Pvap	1.31	kPa	245.46	Calculated Property
Pvap	12.20	kPa	283.87	Calculated Property
Pvap	62.18	kPa	322.27	Calculated Property
Pvap	213.47	kPa	360.68	Calculated Property
Pvap	559.50	kPa	399.08	Calculated Property
Pvap	1212.77	kPa	437.49	Calculated Property
Pvap	2292.93	kPa	475.89	Calculated Property
Pvap	3922.51	kPa	514.30	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.02]	N/m	[169.15; 336.15]	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			5.26220e-02
Coefficient B			-1.05700e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			169.15
Temperature range, max.			336.15
γ	0.03	N/m	169.15	Calculated Property
γ	0.03	N/m	187.71	Calculated Property
γ	0.03	N/m	206.26	Calculated Property
γ	0.03	N/m	224.82	Calculated Property
γ	0.03	N/m	243.37	Calculated Property
γ	0.02	N/m	261.93	Calculated Property
γ	0.02	N/m	280.48	Calculated Property
γ	0.02	N/m	299.04	Calculated Property
γ	0.02	N/m	317.59	Calculated Property
γ	0.02	N/m	336.15	Calculated Property

Similar Compounds

Find more compounds similar to sec-Butylamine.

Mixtures

• sec-Butylamine + Heptane
• Trichloromethane + sec-Butylamine
• sec-Butylamine + Methyl Alcohol
• Benzene + sec-Butylamine
• sec-Butylamine + Water

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
• Crippen Method
• Thermodynamic study of heptane + amine mixtures. V. Excess and solvation Gibbs energies
• 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
• Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
• 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
• Volumetric Properties of 2-Alkylamines (2-Aminobutane and 2-Aminooctane) at Pressures up to 140 MPa and Temperatures between (293.15 and 403.15) K
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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