Chemical Properties of 1-Propanol, 3-amino- (CAS 156-87-6)

InChI

InChI=1S/C3H9NO/c4-2-1-3-5/h5H,1-4H2

InChI Key

WUGQZFFCHPXWKQ-UHFFFAOYSA-N

Formula

C3H9NO

SMILES

NCCCO

Molecular Weight¹

75.11

CAS

156-87-6

Other Names

• 1,3-Propanolamine
• 1-Amino-3-hydroxypropane
• 1-Amino-3-propanol
• 3-Aminopropanol
• 3-Aminopropanol-(1)
• 3-Aminopropyl alcohol
• 3-Hydroxy-1-aminopropane
• 3-Hydroxy-1-propylamine
• 3-Hydroxypropylamine
• 3-Propanolamine
• 3-amino-1-propanol
• 3-aminopropan-1-ol
• NH2(CH2)3OH
• NSC 7766
• Propanolamine
• «beta»-Alaninol
• «gamma»-Aminopropanol

• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• Δ_fH°_gas : 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).
• IE : Ionization energy (eV).
• 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 : 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).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
PAff	[936.00; 962.50]	kJ/mol
PAff	962.50	kJ/mol	NIST
PAff	945.30	kJ/mol	NIST
PAff	936.00	kJ/mol	NIST
PAff	953.50 ± 1.60	kJ/mol	NIST
BasG	[903.80; 921.30]	kJ/mol
BasG	917.30	kJ/mol	NIST
BasG	912.50	kJ/mol	NIST
BasG	903.80	kJ/mol	NIST
BasG	921.30 ± 1.20	kJ/mol	NIST
ΔfH°gas	-240.65	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	12.81	kJ/mol	Joback Calculated Property
ΔvapH°	59.72	kJ/mol	Relay (1.0) Calculated Property
IE	[9.00; 9.77]	eV
IE	9.00	eV	NIST
IE	9.77 ± 0.20	eV	NIST
logPoct/wat	-0.672		Crippen Calculated Property
McVol	68.980	ml/mol	McGowan Calculated Property
Pc	5430.51	kPa	Joback Calculated Property
Inp	[740.00; 826.00]
Inp	773.00		NIST
Inp	770.00		NIST
Inp	740.00		NIST
Inp	785.00		NIST
Inp	826.00		NIST
Inp	773.00		NIST
Inp	785.00		NIST
Inp	826.00		NIST
I	[1534.00; 1577.00]
I	1534.00		NIST
I	1577.00		NIST
I	1570.00		NIST
I	1548.00		NIST
I	1548.00		NIST
I	1555.00		NIST
I	1555.00		NIST
I	1555.00		NIST
Tboil	[460.70; 461.00]	K
Tboil	460.70	K	NIST
Tboil	461.00	K	NIST
Tc	683.88	K	Relay (1.0) Calculated Property
Tfus	[284.70; 285.55]	K
Tfus	284.70 ± 0.35	K	NIST
Tfus	285.55 ± 0.20	K	NIST

Cheméo can also estimate Critical Volume, Standard Gibbs free energy of formation, Acentric Factor, Log10 of Water solubility in mol/l for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[204.00; 217.00]	J/mol×K	[303.15; 353.15]
Cp,liquid	204.00	J/mol×K	303.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	207.00	J/mol×K	308.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	208.00	J/mol×K	313.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	208.00	J/mol×K	318.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	209.00	J/mol×K	323.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	210.00	J/mol×K	328.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	211.00	J/mol×K	333.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	213.00	J/mol×K	338.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	214.00	J/mol×K	343.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	216.00	J/mol×K	348.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
Cp,liquid	217.00	J/mol×K	353.15	Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
η	[0.0022500; 0.0404200]	Pa×s	[293.15; 373.15]
η	0.0404200	Pa×s	293.15	Experimental excess molar properties of binary mixtures of (3-amino-1-propanol + isobutanol, 2-propanol) at T = (293.15 to 333.15) K and modelling the excess molar volume by Prigogine-Flory-Patterson theory
η	0.0392895	Pa×s	293.15	Measurement and modeling the excess molar properties of binary mixtures of {[C6mim][BF4] + 3-amino-1-propanol} and {[C6mim][BF4] + isobutanol}: Application of Prigogine-Flory-Patterson theory
η	0.0304336	Pa×s	298.15	Measurement and modeling the excess molar properties of binary mixtures of {[C6mim][BF4] + 3-amino-1-propanol} and {[C6mim][BF4] + isobutanol}: Application of Prigogine-Flory-Patterson theory
η	0.0304300	Pa×s	298.15	Viscosity Measurement and Correlation of Unloaded and CO2-Loaded 3-Amino-1-propanol Solution
η	0.0238679	Pa×s	303.15	Measurement and modeling the excess molar properties of binary mixtures of {[C6mim][BF4] + 3-amino-1-propanol} and {[C6mim][BF4] + isobutanol}: Application of Prigogine-Flory-Patterson theory
η	0.0238700	Pa×s	303.15	Viscosity Measurement and Correlation of Unloaded and CO2-Loaded 3-Amino-1-propanol Solution
η	0.0238680	Pa×s	303.15	Experimental excess molar properties of binary mixtures of (3-amino-1-propanol + isobutanol, 2-propanol) at T = (293.15 to 333.15) K and modelling the excess molar volume by Prigogine-Flory-Patterson theory
η	0.0190712	Pa×s	308.15	Measurement and modeling the excess molar properties of binary mixtures of {[C6mim][BF4] + 3-amino-1-propanol} and {[C6mim][BF4] + isobutanol}: Application of Prigogine-Flory-Patterson theory
η	0.0190700	Pa×s	308.15	Viscosity Measurement and Correlation of Unloaded and CO2-Loaded 3-Amino-1-propanol Solution
η	0.0152660	Pa×s	313.15	Experimental excess molar properties of binary mixtures of (3-amino-1-propanol + isobutanol, 2-propanol) at T = (293.15 to 333.15) K and modelling the excess molar volume by Prigogine-Flory-Patterson theory
η	0.0152700	Pa×s	313.15	Viscosity Measurement and Correlation of Unloaded and CO2-Loaded 3-Amino-1-propanol Solution
η	0.0152664	Pa×s	313.15	Measurement and modeling the excess molar properties of binary mixtures of {[C6mim][BF4] + 3-amino-1-propanol} and {[C6mim][BF4] + isobutanol}: Application of Prigogine-Flory-Patterson theory
η	0.0123600	Pa×s	318.15	Viscosity Measurement and Correlation of Unloaded and CO2-Loaded 3-Amino-1-propanol Solution
η	0.0123545	Pa×s	318.15	Measurement and modeling the excess molar properties of binary mixtures of {[C6mim][BF4] + 3-amino-1-propanol} and {[C6mim][BF4] + isobutanol}: Application of Prigogine-Flory-Patterson theory
η	0.0102200	Pa×s	323.15	Viscosity Measurement and Correlation of Unloaded and CO2-Loaded 3-Amino-1-propanol Solution
η	0.0102191	Pa×s	323.15	Measurement and modeling the excess molar properties of binary mixtures of {[C6mim][BF4] + 3-amino-1-propanol} and {[C6mim][BF4] + isobutanol}: Application of Prigogine-Flory-Patterson theory
η	0.0102190	Pa×s	323.15	Experimental excess molar properties of binary mixtures of (3-amino-1-propanol + isobutanol, 2-propanol) at T = (293.15 to 333.15) K and modelling the excess molar volume by Prigogine-Flory-Patterson theory
η	0.0085400	Pa×s	328.15	Viscosity Measurement and Correlation of Unloaded and CO2-Loaded 3-Amino-1-propanol Solution
η	0.0085347	Pa×s	328.15	Measurement and modeling the excess molar properties of binary mixtures of {[C6mim][BF4] + 3-amino-1-propanol} and {[C6mim][BF4] + isobutanol}: Application of Prigogine-Flory-Patterson theory
η	0.0071230	Pa×s	333.15	Experimental excess molar properties of binary mixtures of (3-amino-1-propanol + isobutanol, 2-propanol) at T = (293.15 to 333.15) K and modelling the excess molar volume by Prigogine-Flory-Patterson theory
η	0.0071234	Pa×s	333.15	Measurement and modeling the excess molar properties of binary mixtures of {[C6mim][BF4] + 3-amino-1-propanol} and {[C6mim][BF4] + isobutanol}: Application of Prigogine-Flory-Patterson theory
η	0.0071200	Pa×s	333.15	Viscosity Measurement and Correlation of Unloaded and CO2-Loaded 3-Amino-1-propanol Solution
η	0.0060452	Pa×s	338.15	Measurement and modeling the excess molar properties of binary mixtures of {[C6mim][BF4] + 3-amino-1-propanol} and {[C6mim][BF4] + isobutanol}: Application of Prigogine-Flory-Patterson theory
η	0.0060500	Pa×s	338.15	Viscosity Measurement and Correlation of Unloaded and CO2-Loaded 3-Amino-1-propanol Solution
η	0.0048400	Pa×s	343.15	Viscosity Measurement and Correlation of Unloaded and CO2-Loaded 3-Amino-1-propanol Solution
η	0.0041700	Pa×s	348.15	Viscosity Measurement and Correlation of Unloaded and CO2-Loaded 3-Amino-1-propanol Solution
η	0.0036300	Pa×s	353.15	Viscosity Measurement and Correlation of Unloaded and CO2-Loaded 3-Amino-1-propanol Solution
η	0.0031900	Pa×s	358.15	Viscosity Measurement and Correlation of Unloaded and CO2-Loaded 3-Amino-1-propanol Solution
η	0.0027300	Pa×s	363.15	Viscosity Measurement and Correlation of Unloaded and CO2-Loaded 3-Amino-1-propanol Solution
η	0.0025200	Pa×s	368.15	Viscosity Measurement and Correlation of Unloaded and CO2-Loaded 3-Amino-1-propanol Solution
η	0.0022500	Pa×s	373.15	Viscosity Measurement and Correlation of Unloaded and CO2-Loaded 3-Amino-1-propanol Solution
ΔfusH	16.90	kJ/mol	284.10	NIST
ρl	[939.30; 987.80]	kg/m3	[293.15; 353.15]
ρl	987.65	kg/m3	293.15	Density and Viscosity Measurements of Binary Alkanol Mixtures from (293.15 to 333.15) K at Atmospheric Pressure
ρl	987.50	kg/m3	293.15	Density Measurements of Unloaded and CO2-Loaded 3-Amino-1-propanol Solutions at Temperatures (293.15 to 353.15) K
ρl	987.80	kg/m3	293.15	Density and Viscosity of 2-Butanol + (1-Propanol, 2-Propanol, or 3-Amino-1-propanol) Mixtures at Temperatures of (293.15 to 323.15) K: Application of the ERAS Model
ρl	987.50	kg/m3	293.15	Volumetric and Viscometric Properties of Alcohol Amines + Ethanol Binary Mixtures
ρl	983.59	kg/m3	298.15	Density, Speed of Sound, Viscosity and Surface Tension of 3-Dimethylamino-1-propylamine + Water, 3-Amino-1-propanol + 3-Dimethylamino-1-propanol, and (3-Amino-1-propanol + 3-Dimethylamino-1-propanol) + Water from T = (293.15 to 323.15) K
ρl	983.60	kg/m3	298.15	Density Measurements of Unloaded and CO2-Loaded 3-Amino-1-propanol Solutions at Temperatures (293.15 to 353.15) K
ρl	984.30	kg/m3	298.15	Density and Viscosity of 2-Butanol + (1-Propanol, 2-Propanol, or 3-Amino-1-propanol) Mixtures at Temperatures of (293.15 to 323.15) K: Application of the ERAS Model
ρl	979.60	kg/m3	303.15	Density Measurements of Unloaded and CO2-Loaded 3-Amino-1-propanol Solutions at Temperatures (293.15 to 353.15) K
ρl	979.65	kg/m3	303.15	Density and Viscosity Measurements of Binary Alkanol Mixtures from (293.15 to 333.15) K at Atmospheric Pressure
ρl	980.30	kg/m3	303.15	Density and Viscosity of 2-Butanol + (1-Propanol, 2-Propanol, or 3-Amino-1-propanol) Mixtures at Temperatures of (293.15 to 323.15) K: Application of the ERAS Model
ρl	979.45	kg/m3	303.15	Volumetric and Viscometric Properties of Alcohol Amines + Ethanol Binary Mixtures
ρl	976.20	kg/m3	308.15	Density and Viscosity of 2-Butanol + (1-Propanol, 2-Propanol, or 3-Amino-1-propanol) Mixtures at Temperatures of (293.15 to 323.15) K: Application of the ERAS Model
ρl	975.50	kg/m3	308.15	Density Measurements of Unloaded and CO2-Loaded 3-Amino-1-propanol Solutions at Temperatures (293.15 to 353.15) K
ρl	971.61	kg/m3	313.15	Density and Viscosity Measurements of Binary Alkanol Mixtures from (293.15 to 333.15) K at Atmospheric Pressure
ρl	971.50	kg/m3	313.15	Density Measurements of Unloaded and CO2-Loaded 3-Amino-1-propanol Solutions at Temperatures (293.15 to 353.15) K
ρl	971.67	kg/m3	313.15	Volumetric and Viscometric Properties of Alcohol Amines + Ethanol Binary Mixtures
ρl	972.30	kg/m3	313.15	Density and Viscosity of 2-Butanol + (1-Propanol, 2-Propanol, or 3-Amino-1-propanol) Mixtures at Temperatures of (293.15 to 323.15) K: Application of the ERAS Model
ρl	967.50	kg/m3	318.15	Density Measurements of Unloaded and CO2-Loaded 3-Amino-1-propanol Solutions at Temperatures (293.15 to 353.15) K
ρl	968.50	kg/m3	318.15	Density and Viscosity of 2-Butanol + (1-Propanol, 2-Propanol, or 3-Amino-1-propanol) Mixtures at Temperatures of (293.15 to 323.15) K: Application of the ERAS Model
ρl	963.40	kg/m3	323.15	Density Measurements of Unloaded and CO2-Loaded 3-Amino-1-propanol Solutions at Temperatures (293.15 to 353.15) K
ρl	963.36	kg/m3	323.15	Volumetric and Viscometric Properties of Alcohol Amines + Ethanol Binary Mixtures
ρl	964.90	kg/m3	323.15	Density and Viscosity of 2-Butanol + (1-Propanol, 2-Propanol, or 3-Amino-1-propanol) Mixtures at Temperatures of (293.15 to 323.15) K: Application of the ERAS Model
ρl	963.52	kg/m3	323.15	Density and Viscosity Measurements of Binary Alkanol Mixtures from (293.15 to 333.15) K at Atmospheric Pressure
ρl	959.30	kg/m3	328.15	Density Measurements of Unloaded and CO2-Loaded 3-Amino-1-propanol Solutions at Temperatures (293.15 to 353.15) K
ρl	955.80	kg/m3	333.15	Density Measurements of Unloaded and CO2-Loaded 3-Amino-1-propanol Solutions at Temperatures (293.15 to 353.15) K
ρl	955.38	kg/m3	333.15	Density and Viscosity Measurements of Binary Alkanol Mixtures from (293.15 to 333.15) K at Atmospheric Pressure
ρl	951.70	kg/m3	338.15	Density Measurements of Unloaded and CO2-Loaded 3-Amino-1-propanol Solutions at Temperatures (293.15 to 353.15) K
ρl	947.60	kg/m3	343.15	Density Measurements of Unloaded and CO2-Loaded 3-Amino-1-propanol Solutions at Temperatures (293.15 to 353.15) K
ρl	943.50	kg/m3	348.15	Density Measurements of Unloaded and CO2-Loaded 3-Amino-1-propanol Solutions at Temperatures (293.15 to 353.15) K
ρl	939.30	kg/m3	353.15	Density Measurements of Unloaded and CO2-Loaded 3-Amino-1-propanol Solutions at Temperatures (293.15 to 353.15) K
csound,fluid	[1632.43; 1727.44]	m/s	[293.15; 323.15]
csound,fluid	1727.44	m/s	293.15	Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of Binary Mixtures of 1-Amino-2-propanol or 3-Amino-1-propanol with 2-Amino-2-methyl-1-propanol, Diethanolamine, or Triethanolamine from (293.15 to 323.15) K
csound,fluid	1712.25	m/s	298.15	Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of Binary Mixtures of 1-Amino-2-propanol or 3-Amino-1-propanol with 2-Amino-2-methyl-1-propanol, Diethanolamine, or Triethanolamine from (293.15 to 323.15) K
csound,fluid	1696.24	m/s	303.15	Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of Binary Mixtures of 1-Amino-2-propanol or 3-Amino-1-propanol with 2-Amino-2-methyl-1-propanol, Diethanolamine, or Triethanolamine from (293.15 to 323.15) K
csound,fluid	1680.79	m/s	308.15	Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of Binary Mixtures of 1-Amino-2-propanol or 3-Amino-1-propanol with 2-Amino-2-methyl-1-propanol, Diethanolamine, or Triethanolamine from (293.15 to 323.15) K
csound,fluid	1664.67	m/s	313.15	Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of Binary Mixtures of 1-Amino-2-propanol or 3-Amino-1-propanol with 2-Amino-2-methyl-1-propanol, Diethanolamine, or Triethanolamine from (293.15 to 323.15) K
csound,fluid	1648.51	m/s	318.15	Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of Binary Mixtures of 1-Amino-2-propanol or 3-Amino-1-propanol with 2-Amino-2-methyl-1-propanol, Diethanolamine, or Triethanolamine from (293.15 to 323.15) K
csound,fluid	1632.43	m/s	323.15	Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of Binary Mixtures of 1-Amino-2-propanol or 3-Amino-1-propanol with 2-Amino-2-methyl-1-propanol, Diethanolamine, or Triethanolamine from (293.15 to 323.15) K
γ	[0.04; 0.04]	N/m	[298.15; 323.15]
γ	0.04	N/m	298.15	Surface Tension of aqueous vinary mixtures of 1-amino-2-propanol and 3-amino-1-propanol, and aqueous ternary mixtures of these amines with diethanolamine, triethanolamine, and 2-amino-2-methyl-1-propanol from (298.15 to 323.15) K
γ	0.04	N/m	303.15	Surface Tension of aqueous vinary mixtures of 1-amino-2-propanol and 3-amino-1-propanol, and aqueous ternary mixtures of these amines with diethanolamine, triethanolamine, and 2-amino-2-methyl-1-propanol from (298.15 to 323.15) K
γ	0.04	N/m	308.15	Surface Tension of aqueous vinary mixtures of 1-amino-2-propanol and 3-amino-1-propanol, and aqueous ternary mixtures of these amines with diethanolamine, triethanolamine, and 2-amino-2-methyl-1-propanol from (298.15 to 323.15) K
γ	0.04	N/m	313.15	Surface Tension of aqueous vinary mixtures of 1-amino-2-propanol and 3-amino-1-propanol, and aqueous ternary mixtures of these amines with diethanolamine, triethanolamine, and 2-amino-2-methyl-1-propanol from (298.15 to 323.15) K
γ	0.04	N/m	318.15	Surface Tension of aqueous vinary mixtures of 1-amino-2-propanol and 3-amino-1-propanol, and aqueous ternary mixtures of these amines with diethanolamine, triethanolamine, and 2-amino-2-methyl-1-propanol from (298.15 to 323.15) K
γ	0.04	N/m	323.15	Surface Tension of aqueous vinary mixtures of 1-amino-2-propanol and 3-amino-1-propanol, and aqueous ternary mixtures of these amines with diethanolamine, triethanolamine, and 2-amino-2-methyl-1-propanol from (298.15 to 323.15) K

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[102.00; 228.74]	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			1.19430e+01
Coefficient B			3.84700e-01
Coefficient C			-2.13200e-04
Coefficient D			4.53000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	102.00	J/mol×K	273.00	Calculated Property
Cp,gas	123.36	J/mol×K	353.78	Calculated Property
Cp,gas	142.57	J/mol×K	434.56	Calculated Property
Cp,gas	159.77	J/mol×K	515.33	Calculated Property
Cp,gas	175.10	J/mol×K	596.11	Calculated Property
Cp,gas	188.71	J/mol×K	676.89	Calculated Property
Cp,gas	200.73	J/mol×K	757.67	Calculated Property
Cp,gas	211.32	J/mol×K	838.44	Calculated Property
Cp,gas	220.61	J/mol×K	919.22	Calculated Property
Cp,gas	228.74	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[360.86; 483.82]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.65620e+01
Coefficient B			-4.48126e+03
Coefficient C			-8.55000e+01
Temperature range, min.			360.86
Temperature range, max.			483.82
Pvap	1.33	kPa	360.86	Calculated Property
Pvap	2.88	kPa	374.52	Calculated Property
Pvap	5.79	kPa	388.18	Calculated Property
Pvap	10.98	kPa	401.85	Calculated Property
Pvap	19.74	kPa	415.51	Calculated Property
Pvap	33.87	kPa	429.17	Calculated Property
Pvap	55.77	kPa	442.83	Calculated Property
Pvap	88.50	kPa	456.50	Calculated Property
Pvap	135.91	kPa	470.16	Calculated Property
Pvap	202.67	kPa	483.82	Calculated Property

Similar Compounds

Find more compounds similar to 1-Propanol, 3-amino-.

Mixtures

• 1-Propanol, 3-amino- + Water
• 1-Propanol, 2-methyl- + 1-Propanol, 3-amino-
• 2-Propanol + 1-Propanol, 3-amino-
• 1-Propanol + 1-Propanol, 3-amino-
• 1-Propanol, 3-(dimethylamino)- + 1-Propanol, 3-amino- + Water
• 1-Propanol, 3-(dimethylamino)- + 1-Propanol, 3-amino-
• Ethanol + 1-Propanol, 3-amino-
• 1-Propanol, 3-amino- + 1-Propanol, 2-amino-2-methyl-
• ETHANOL, 2,2'-IMINOBIS- + 1-Propanol, 3-amino-
• Triethanolamine + 1-Propanol, 3-amino-
• ETHANOL, 2,2'-IMINOBIS- + 1-Propanol, 3-amino- + Water
• Triethanolamine + 1-Propanol, 3-amino- + Water
• 1-Propanol, 3-amino- + Water + 1-Propanol, 2-amino-2-methyl-
• Carbon dioxide + 1-Propanol, 3-amino- + Water

Sources

• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Equilibrium solubility of carbon dioxide in aqueous solutions of 3-amino-1-propanol, 4-amino-1-butanol and 5-amino-1-pentanol at low partial pressures
• Solubility of CO2 in 3-amino-1-propanol and in N-methyldiethanolamine aqueous solutions: Experimental investigation and correlation using the CPA equation of state
• Molar excess enthalpy (HEm) for various {alkanolamine (1) + water (2)} systems at T = (298.15, 313.15, and 323.15) K
• Measurement and modeling the excess molar properties of binary mixtures of {[C6mim][BF4] + 3-amino-1-propanol} and {[C6mim][BF4] + isobutanol}: Application of Prigogine-Flory-Patterson theory
• Experimental excess molar properties of binary mixtures of (3-amino-1-propanol + isobutanol, 2-propanol) at T = (293.15 to 333.15) K and modelling the excess molar volume by Prigogine-Flory-Patterson theory
• Low-temperature thermal properties of the aqueous solutions of simple aminoalcohols: Finding of peculiarities in 1-amino-2-propanol solutions
• Density Measurements of Unloaded and CO2-Loaded 3-Amino-1-propanol Solutions at Temperatures (293.15 to 353.15) K
• Density, Speed of Sound, Viscosity and Surface Tension of 3-Dimethylamino-1-propylamine + Water, 3-Amino-1-propanol + 3-Dimethylamino-1-propanol, and (3-Amino-1-propanol + 3-Dimethylamino-1-propanol) + Water from T = (293.15 to 323.15) K
• Volumetric and Viscometric Properties of Alcohol Amines + Ethanol Binary Mixtures
• Viscosity Measurement and Correlation of Unloaded and CO2-Loaded 3-Amino-1-propanol Solution
• Density and Viscosity of 2-Butanol + (1-Propanol, 2-Propanol, or 3-Amino-1-propanol) Mixtures at Temperatures of (293.15 to 323.15) K: Application of the ERAS Model
• Surface Tension of aqueous vinary mixtures of 1-amino-2-propanol and 3-amino-1-propanol, and aqueous ternary mixtures of these amines with diethanolamine, triethanolamine, and 2-amino-2-methyl-1-propanol from (298.15 to 323.15) K
• Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K
• Density and Viscosity Measurements of Binary Alkanol Mixtures from (293.15 to 333.15) K at Atmospheric Pressure
• Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of Binary Mixtures of 1-Amino-2-propanol or 3-Amino-1-propanol with 2-Amino-2-methyl-1-propanol, Diethanolamine, or Triethanolamine from (293.15 to 323.15) K
• Joback Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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