Chemical Properties of 2-Propanamine (CAS 75-31-0)

InChI

InChI=1S/C3H9N/c1-3(2)4/h3H,4H2,1-2H3

InChI Key

JJWLVOIRVHMVIS-UHFFFAOYSA-N

Formula

C3H9N

SMILES

CC(C)N

Molecular Weight¹

59.11

CAS

75-31-0

Other Names

• 1-Methylethylamine
• 2-Amino-propaan
• 2-Amino-propano
• 2-Aminopropan
• 2-aminopropane
• 2-propylamine
• Isopropilamina
• Monoisopropylamine
• NSC 62775
• Propane, 2-amino-
• UN 1221
• iso-C3H7NH2
• iso-Propylamine gas
• isopropylamine
• sec-Propylamine

• 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).
• 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).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed 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_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_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• 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).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ : Gas thermal conductivity (W/m×K).
• λ : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• 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	[0.2759; 0.2910]
ω	0.2759		ChemSep v8.3 pure component data Compiled value
ω	0.2910		KDB
PAff	923.80	kJ/mol	NIST
Tig	675.37	K	KDB
BasG	889.00	kJ/mol	NIST
ΔcH°liquid	-2354.50 ± 0.50	kJ/mol	NIST
μ	1.50	debye	ChemSep v8.3 pure component data Compiled value
LFL	2.30	% in Air	KDB
UFL	12.00	% in Air	KDB
Tflash,cc	247.04	K	KDB
ΔfG°	31.92	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	[-83.82; -83.70]	kJ/mol
ΔfH°gas	-83.80	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-83.82	kJ/mol	KDB
ΔfH°gas	-83.70 ± 0.80	kJ/mol	NIST
ΔfH°gas	-83.76 ± 0.79	kJ/mol	NIST
ΔfH°liquid	-112.30 ± 0.67	kJ/mol	NIST
ΔfusH°	5.20	kJ/mol	Joback Calculated Property
ΔvapH°	[28.40; 28.71]	kJ/mol
ΔvapH°	28.71	kJ/mol	NIST
ΔvapH°	28.40	kJ/mol	NIST
ΔvapH°	28.50 ± 0.20	kJ/mol	NIST
ΔvapH°	28.50	kJ/mol	NIST
IE	[8.60; 9.31]	eV
IE	8.60 ± 0.10	eV	NIST
IE	8.86	eV	NIST
IE	8.72 ± 0.03	eV	NIST
IE	9.31	eV	NIST
log10WS	0.14		Relay (1.0) Calculated Property
logPoct/wat	0.353		Crippen Calculated Property
McVol	63.110	ml/mol	McGowan Calculated Property
NFPA Fire	4		KDB
NFPA Health	3		KDB
Pc	[4540.00; 4540.00]	kPa
Pc	4540.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	4540.00	kPa	KDB
Pc	4540.00 ± 50.66	kPa	NIST
Ptriple	7.73e-03	kPa	ChemSep v8.3 pure component data Compiled value
ρc	267.77 ± 0.01	kg/m3	NIST
Inp	[465.00; 477.00]
Inp	469.00		NIST
Inp	468.00		NIST
Inp	Outlier 477.00		NIST
Inp	469.00		NIST
Inp	465.00		NIST
Inp	465.00		NIST
Inp	465.00		NIST
Inp	469.00		NIST
I	[710.00; 743.00]
I	743.00		NIST
I	740.00		NIST
I	725.00		NIST
I	710.00		NIST
I	740.00		NIST
I	743.00		NIST
S°liquid	218.32	J/mol×K	NIST
Tboil	[304.65; 307.15]	K
Tboil	305.55	K	ChemSep v8.3 pure component data Compiled value
Tboil	304.91	K	KDB
Tboil	306.70	K	NIST
Tboil	305.60	K	NIST
Tboil	304.90	K	NIST
Tboil	305.01 ± 0.25	K	NIST
Tboil	305.55	K	NIST
Tboil	307.15 ± 1.50	K	NIST
Tboil	304.65 ± 1.00	K	NIST
Tboil	307.15 ± 1.00	K	NIST
Tboil	306.15 ± 0.30	K	NIST
Tboil	305.15 ± 2.00	K	NIST
Tc	[471.80; 472.50]	K
Tc	472.50	K	Gas-Liquid Critical Temperatures of Some Alkenes, Amines, and Cyclic Hydrocarbons
Tc	471.85	K	ChemSep v8.3 pure component data Compiled value
Tc	471.80	K	KDB
Tc	471.80	K	NIST
Tc	471.90 ± 0.50	K	NIST
Tfus	[171.95; 178.01]	K
Tfus	177.95	K	ChemSep v8.3 pure component data Compiled value
Tfus	178.01	K	KDB
Tfus	177.95	K	NIST
Tfus	171.95 ± 0.60	K	NIST
Ttriple	[177.95; 178.01]	K
Ttriple	177.95	K	ChemSep v8.3 pure component data Compiled value
Ttriple	178.01 ± 0.01	K	NIST
Ttriple	178.01 ± 0.01	K	NIST
UQi	2.62		ChemSep v8.3 pure component data Compiled value
URi	2.94		ChemSep v8.3 pure component data Compiled value
Vc	[0.221; 0.221]	m3/kmol
Vc	0.221	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.221	m3/kmol	KDB
Vm	8.67e-05	m3/mol	Thermodynamic study of (heptane + amine) mixtures. II. Excess and partial molar volumes at 298.15 K
Zc	[0.2557720; 0.2560000]
Zc	0.2560000		ChemSep v8.3 pure component data Compiled value
Zc	0.2557720		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[163.85; 165.30]	J/mol×K	[298.15; 313.00]
Cp,liquid	163.85	J/mol×K	298.15	NIST
Cp,liquid	164.00	J/mol×K	298.15	NIST
Cp,liquid	165.30	J/mol×K	298.15	NIST
Cp,liquid	164.00	J/mol×K	313.00	NIST
ΔfusH	[7.32; 7.33]	kJ/mol	[177.99; 178.00]
ΔfusH	7.32	kJ/mol	177.99	NIST
ΔfusH	7.32	kJ/mol	177.99	NIST
ΔfusH	7.33	kJ/mol	178.00	NIST
ΔfusH	7.33	kJ/mol	178.00	NIST
ΔvapH	[27.20; 29.70]	kJ/mol	[304.90; 313.00]
ΔvapH	27.83	kJ/mol	304.90	NIST
ΔvapH	29.70	kJ/mol	305.50	NIST
ΔvapH	27.20	kJ/mol	313.00	NIST
ρl	[683.94; 688.00]	kg/m3	[293.00; 298.15]
ρl	688.00	kg/m3	293.00	KDB
ρl	683.94	kg/m3	298.15	Excess enthalpies of binary mixtures of some propylamines + some propanols at 298.15K
ΔfusS	[41.15; 41.15]	J/mol×K	[177.99; 177.99]
ΔfusS	41.15	J/mol×K	177.99	NIST
ΔfusS	41.15	J/mol×K	177.99	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[83.66; 244.08]	J/mol×K	[255.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			5.02425e+01
Coefficient B			-5.40067e+02
Coefficient C			5.62708e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			ChemSep eq 16, IdealGasHeatCapacityCp
Temperature range, min.			255.00
Temperature range, max.			1500.00
Cp,gas	83.66	J/mol×K	255.00	Calculated Property
Cp,gas	120.63	J/mol×K	393.33	Calculated Property
Cp,gas	150.86	J/mol×K	531.67	Calculated Property
Cp,gas	174.33	J/mol×K	670.00	Calculated Property
Cp,gas	192.69	J/mol×K	808.33	Calculated Property
Cp,gas	207.30	J/mol×K	946.67	Calculated Property
Cp,gas	219.15	J/mol×K	1085.00	Calculated Property
Cp,gas	228.93	J/mol×K	1223.33	Calculated Property
Cp,gas	237.12	J/mol×K	1361.67	Calculated Property
Cp,gas	244.08	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[146.21; 166.71]	J/mol×K	[177.95; 320.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K
Coefficient A			-3.24690e+01
Coefficient B			1.97710e+00
Coefficient C			-7.01450e-03
Coefficient D			8.69130e-06
Coefficient E			0.00000e+00
Comment			ChemSep eq 100, LiquidHeatCapacityCp
Temperature range, min.			177.95
Temperature range, max.			320.00
Cp,liquid	146.21	J/mol×K	177.95	Calculated Property
Cp,liquid	150.49	J/mol×K	193.73	Calculated Property
Cp,liquid	153.78	J/mol×K	209.52	Calculated Property
Cp,liquid	156.31	J/mol×K	225.30	Calculated Property
Cp,liquid	158.27	J/mol×K	241.08	Calculated Property
Cp,liquid	159.86	J/mol×K	256.87	Calculated Property
Cp,liquid	161.30	J/mol×K	272.65	Calculated Property
Cp,liquid	162.78	J/mol×K	288.43	Calculated Property
Cp,liquid	164.52	J/mol×K	304.22	Calculated Property
Cp,liquid	166.71	J/mol×K	320.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0006737; 0.0001214]	Pa×s	[250.00; 453.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-3.11570e+01
Coefficient B			1.92600e+03
Coefficient C			2.92500e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			ChemSep eq 101, LiquidViscosity
Temperature range, min.			250.00
Temperature range, max.			453.15
η	0.0006737	Pa×s	250.00	Calculated Property
η	0.0004584	Pa×s	272.57	Calculated Property
η	0.0003370	Pa×s	295.14	Calculated Property
η	0.0002629	Pa×s	317.72	Calculated Property
η	0.0002150	Pa×s	340.29	Calculated Property
η	0.0001824	Pa×s	362.86	Calculated Property
η	0.0001595	Pa×s	385.43	Calculated Property
η	0.0001429	Pa×s	408.01	Calculated Property
η	0.0001306	Pa×s	430.58	Calculated Property
η	0.0001214	Pa×s	453.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[35.87; 0.00]	kJ/mol	[177.95; 471.85]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			4.40410e+01
Coefficient B			4.33250e-01
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			4.71850e+02
Comment			ChemSep eq 106, HeatOfVaporization
Temperature range, min.			177.95
Temperature range, max.			471.85
ΔvapH	35.87	kJ/mol	177.95	Calculated Property
ΔvapH	34.09	kJ/mol	210.61	Calculated Property
ΔvapH	32.17	kJ/mol	243.26	Calculated Property
ΔvapH	30.09	kJ/mol	275.92	Calculated Property
ΔvapH	27.81	kJ/mol	308.57	Calculated Property
ΔvapH	25.25	kJ/mol	341.23	Calculated Property
ΔvapH	22.29	kJ/mol	373.88	Calculated Property
ΔvapH	18.70	kJ/mol	406.54	Calculated Property
ΔvapH	13.85	kJ/mol	439.19	Calculated Property
ΔvapH	0.00	kJ/mol	471.85	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 4308.91]	kPa	[225.49; 471.85]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42286e+01
Coefficient B			-2.49064e+03
Coefficient C			-4.68340e+01
Temperature range, min.			225.49
Temperature range, max.			471.85
Pvap	1.33	kPa	225.49	Calculated Property
Pvap	8.50	kPa	252.86	Calculated Property
Pvap	35.08	kPa	280.24	Calculated Property
Pvap	107.52	kPa	307.61	Calculated Property
Pvap	266.39	kPa	334.98	Calculated Property
Pvap	563.89	kPa	362.36	Calculated Property
Pvap	1058.92	kPa	389.73	Calculated Property
Pvap	1811.64	kPa	417.10	Calculated Property
Pvap	2878.53	kPa	444.48	Calculated Property
Pvap	4308.91	kPa	471.85	Calculated Property
Pvap	[7.73e-03; 4540.44]	kPa	[177.95; 471.85]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			1.29752e+02
Coefficient B			-7.20150e+03
Coefficient C			-1.89340e+01
Coefficient D			2.22550e-02
Coefficient E			1.00000e+00
Comment			ChemSep eq 101, VaporPressure
Temperature range, min.			177.95
Temperature range, max.			471.85
Pvap	7.73e-03	kPa	177.95	Calculated Property
Pvap	0.35	kPa	210.61	Calculated Property
Pvap	4.65	kPa	243.26	Calculated Property
Pvap	29.42	kPa	275.92	Calculated Property
Pvap	115.88	kPa	308.57	Calculated Property
Pvap	332.98	kPa	341.23	Calculated Property
Pvap	771.02	kPa	373.88	Calculated Property
Pvap	1534.85	kPa	406.54	Calculated Property
Pvap	2743.95	kPa	439.19	Calculated Property
Pvap	4540.44	kPa	471.85	Calculated Property
Pvap	[7.94e-03; 4548.17]	kPa	[177.95; 471.85]	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			9.27941e+01
Coefficient B			-6.47623e+03
Coefficient C			-1.18881e+01
Coefficient D			1.14303e-05
Coefficient E			0.00000e+00
Temperature range, min.			177.95
Temperature range, max.			471.85
Pvap	7.94e-03	kPa	177.95	Calculated Property
Pvap	0.35	kPa	210.61	Calculated Property
Pvap	4.63	kPa	243.26	Calculated Property
Pvap	29.37	kPa	275.92	Calculated Property
Pvap	115.86	kPa	308.57	Calculated Property
Pvap	332.81	kPa	341.23	Calculated Property
Pvap	769.45	kPa	373.88	Calculated Property
Pvap	1529.78	kPa	406.54	Calculated Property
Pvap	2736.71	kPa	439.19	Calculated Property
Pvap	4548.17	kPa	471.85	Calculated Property
Pvap	[31.16; 270.12]	kPa	[277.07; 334.13]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.38502e+01
Coefficient B			-2.26954e+03
Coefficient C			-5.90790e+01
Reference			Osborn and Douslin, 1968
Temperature range, min.			277.07
Temperature range, max.			334.13
Pvap	31.16	kPa	277.07	Calculated Property
Pvap	41.82	kPa	283.41	Calculated Property
Pvap	55.22	kPa	289.75	Calculated Property
Pvap	71.85	kPa	296.09	Calculated Property
Pvap	92.20	kPa	302.43	Calculated Property
Pvap	116.84	kPa	308.77	Calculated Property
Pvap	146.33	kPa	315.11	Calculated Property
Pvap	181.29	kPa	321.45	Calculated Property
Pvap	222.33	kPa	327.79	Calculated Property
Pvap	270.12	kPa	334.13	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[801.59; 267.56]	kg/m3	[177.95; 471.85]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			7.56671e+01
Coefficient B			2.82800e-01
Coefficient C			4.71850e+02
Coefficient D			2.97200e-01
Comment			ChemSep eq 105, LiquidDensity
Temperature range, min.			177.95
Temperature range, max.			471.85
ρl	801.59	kg/m3	177.95	Calculated Property
ρl	771.90	kg/m3	210.61	Calculated Property
ρl	740.73	kg/m3	243.26	Calculated Property
ρl	707.71	kg/m3	275.92	Calculated Property
ρl	672.32	kg/m3	308.57	Calculated Property
ρl	633.72	kg/m3	341.23	Calculated Property
ρl	590.49	kg/m3	373.88	Calculated Property
ρl	539.74	kg/m3	406.54	Calculated Property
ρl	473.64	kg/m3	439.19	Calculated Property
ρl	267.56	kg/m3	471.85	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.00]	N/m	[177.95; 471.85]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is γ in N/m, T in K
Coefficient A			5.81300e-02
Coefficient B			1.20700e+00
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			4.71850e+02
Comment			ChemSep eq 106, SurfaceTension
Temperature range, min.			177.95
Temperature range, max.			471.85
γ	0.03	N/m	177.95	Calculated Property
γ	0.03	N/m	210.61	Calculated Property
γ	0.02	N/m	243.26	Calculated Property
γ	0.02	N/m	275.92	Calculated Property
γ	0.02	N/m	308.57	Calculated Property
γ	0.01	N/m	341.23	Calculated Property
γ	0.01	N/m	373.88	Calculated Property
γ	0.01	N/m	406.54	Calculated Property
γ	0.00	N/m	439.19	Calculated Property
γ	0.00	N/m	471.85	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.02; 0.10]	W/m×K	[304.92; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λ in W/m×K, T in K
Coefficient A			2.81830e-04
Coefficient B			9.20940e-01
Coefficient C			6.19170e+02
Coefficient D			0.00000e+00
Comment			ChemSep eq 102, VaporThermalConductivity
Temperature range, min.			304.92
Temperature range, max.			1000.00
λ	0.02	W/m×K	304.92	Calculated Property
λ	0.03	W/m×K	382.15	Calculated Property
λ	0.03	W/m×K	459.38	Calculated Property
λ	0.04	W/m×K	536.61	Calculated Property
λ	0.05	W/m×K	613.84	Calculated Property
λ	0.06	W/m×K	691.08	Calculated Property
λ	0.07	W/m×K	768.31	Calculated Property
λ	0.08	W/m×K	845.54	Calculated Property
λ	0.09	W/m×K	922.77	Calculated Property
λ	0.10	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.18; 0.14]	W/m×K	[177.95; 305.55]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λ in W/m×K, T in K
Coefficient A			2.37000e-01
Coefficient B			-3.32000e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			ChemSep eq 100, LiquidThermalConductivity
Temperature range, min.			177.95
Temperature range, max.			305.55
λ	0.18	W/m×K	177.95	Calculated Property
λ	0.17	W/m×K	192.13	Calculated Property
λ	0.17	W/m×K	206.31	Calculated Property
λ	0.16	W/m×K	220.48	Calculated Property
λ	0.16	W/m×K	234.66	Calculated Property
λ	0.15	W/m×K	248.84	Calculated Property
λ	0.15	W/m×K	263.02	Calculated Property
λ	0.14	W/m×K	277.19	Calculated Property
λ	0.14	W/m×K	291.37	Calculated Property
λ	0.14	W/m×K	305.55	Calculated Property

Similar Compounds

Find more compounds similar to 2-Propanamine.

Mixtures

• 2-Propanamine + Heptane
• Propylene Glycol + 2-Propanamine
• 1,3-Propanediol + 2-Propanamine

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Crippen Method
• Crippen Method
• Thermodynamic study of heptane + amine mixtures. V. Excess and solvation Gibbs energies
• Thermodynamic study of (heptane + amine) mixtures. II. Excess and partial molar volumes at 298.15 K
• Excess enthalpies of binary mixtures of some propylamines + some propanols at 298.15K
• Gas-Liquid Critical Temperatures of Some Alkenes, Amines, and Cyclic Hydrocarbons
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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