Chemical Properties of 1-Propanol, 2-amino-2-methyl- (CAS 124-68-5)

InChI

InChI=1S/C4H11NO/c1-4(2,5)3-6/h6H,3,5H2,1-2H3

InChI Key

CBTVGIZVANVGBH-UHFFFAOYSA-N

Formula

C4H11NO

SMILES

CC(C)(N)CO

Molecular Weight¹

89.14

CAS

124-68-5

Other Names

• 1,1-Dimethyl-2-hydroxyethylamine
• 2,2-Dimethyl-ethanolamine
• 2-Amino-1-hydroxy-2-methylpropane
• 2-Amino-2,2-dimethylethanol
• 2-Amino-2-methyl-1-propanol
• 2-Amino-2-methylpropan-1-ol
• 2-Amino-2-methylpropanol
• 2-Aminodimethylethanol
• 2-Aminoisobutanol
• 2-Hydroxymethyl-2-propylamine
• 2-Methyl-2-aminopropanol
• 2-Methyl-2-aminopropanol-1
• AMP
• AMP (thinner)
• AMP 75
• AMP Regular
• AMP-95
• Amino-2,2-dimethylethanol
• Amino-2-methyl-1-propanol
• Aminoisobutanol
• Aminomethylpropanol
• Corrguard 75
• Hydroxy-tert-butylamine
• Hydroxymethyl-2-propylamine
• Isobutanol-2-amine
• KV 5088
• NSC 441
• «beta»-Aminoisobutanol
• «beta»-Aminoisobutanol

• ω : Acentric Factor.
• 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_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : 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).
• 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 : Polar retention indices.
• c_sound,fluid : Speed of sound in fluid (m/s).
• 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).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.6190		Relay (1.0) Calculated Property
ΔfG°	-84.73	kJ/mol	Joback Calculated Property
ΔfH°gas	-268.30	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	7.99	kJ/mol	Joback Calculated Property
ΔvapH°	54.91	kJ/mol	Relay (1.0) Calculated Property
IE	9.25	eV	Relay (1.0) Calculated Property
log10WS	0.08		Relay (1.0) Calculated Property
logPoct/wat	-0.284		Crippen Calculated Property
McVol	83.070	ml/mol	McGowan Calculated Property
Pc	4862.97	kPa	Joback Calculated Property
I	[1380.00; 1468.00]
I	1468.00		NIST
I	1460.00		NIST
I	1380.00		NIST
I	1384.00		NIST
I	1452.00		NIST
I	1468.00		NIST
Tboil	[436.85; 438.70]	K
Tboil	436.85	K	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Tboil	438.70	K	NIST
Tboil	438.00	K	NIST
Tc	609.77	K	Relay (1.0) Calculated Property
Tfus	303.50 ± 0.50	K	NIST
Ttriple	295.75	K	Solid Solubility in the Aqueous 2-Amino-2-methyl-propanol (AMP) Plus Piperazine (PZ) System
Vc	0.303	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[182.53; 227.82]	J/mol×K	[452.40; 639.25]
Cp,gas	182.53	J/mol×K	452.40	Joback Calculated Property
Cp,gas	191.22	J/mol×K	483.54	Joback Calculated Property
Cp,gas	199.43	J/mol×K	514.68	Joback Calculated Property
Cp,gas	207.16	J/mol×K	545.82	Joback Calculated Property
Cp,gas	214.46	J/mol×K	576.96	Joback Calculated Property
Cp,gas	221.34	J/mol×K	608.11	Joback Calculated Property
Cp,gas	227.82	J/mol×K	639.25	Joback Calculated Property
Cp,liquid	229.50	J/mol×K	298.15	NIST
η	[0.0089100; 0.0478000]	Pa×s	[313.15; 343.15]
η	0.0478000	Pa×s	313.15	Volumetric Properties and Viscosities for Aqueous AMP Solutions from 25 0C to 70 0C
η	0.0251000	Pa×s	323.15	Volumetric Properties and Viscosities for Aqueous AMP Solutions from 25 0C to 70 0C
η	0.0144000	Pa×s	333.15	Volumetric Properties and Viscosities for Aqueous AMP Solutions from 25 0C to 70 0C
η	0.0089100	Pa×s	343.15	Volumetric Properties and Viscosities for Aqueous AMP Solutions from 25 0C to 70 0C
Pvap	[0.04; 160.00]	kPa	[293.29; 452.00]
Pvap	0.04	kPa	293.29	Investigation of the isothermal (vapour + liquid) equilibria of aqueous 2-amino-2-methyl-1-propanol (AMP), N-benzylethanolamine, or 3-dimethylamino-1-propanol solutions at several temperatures
Pvap	0.10	kPa	303.35	Investigation of the isothermal (vapour + liquid) equilibria of aqueous 2-amino-2-methyl-1-propanol (AMP), N-benzylethanolamine, or 3-dimethylamino-1-propanol solutions at several temperatures
Pvap	0.22	kPa	313.24	Investigation of the isothermal (vapour + liquid) equilibria of aqueous 2-amino-2-methyl-1-propanol (AMP), N-benzylethanolamine, or 3-dimethylamino-1-propanol solutions at several temperatures
Pvap	0.46	kPa	323.25	Investigation of the isothermal (vapour + liquid) equilibria of aqueous 2-amino-2-methyl-1-propanol (AMP), N-benzylethanolamine, or 3-dimethylamino-1-propanol solutions at several temperatures
Pvap	0.87	kPa	332.57	Investigation of the isothermal (vapour + liquid) equilibria of aqueous 2-amino-2-methyl-1-propanol (AMP), N-benzylethanolamine, or 3-dimethylamino-1-propanol solutions at several temperatures
Pvap	1.66	kPa	343.18	Investigation of the isothermal (vapour + liquid) equilibria of aqueous 2-amino-2-methyl-1-propanol (AMP), N-benzylethanolamine, or 3-dimethylamino-1-propanol solutions at several temperatures
Pvap	1.94	kPa	347.50	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	2.93	kPa	353.17	Investigation of the isothermal (vapour + liquid) equilibria of aqueous 2-amino-2-methyl-1-propanol (AMP), N-benzylethanolamine, or 3-dimethylamino-1-propanol solutions at several temperatures
Pvap	2.94	kPa	354.30	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	4.99	kPa	363.10	Investigation of the isothermal (vapour + liquid) equilibria of aqueous 2-amino-2-methyl-1-propanol (AMP), N-benzylethanolamine, or 3-dimethylamino-1-propanol solutions at several temperatures
Pvap	4.94	kPa	363.60	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	5.00	kPa	364.11	Ternary Isobaric Vapor-Liquid Equilibria of Methanol + N-Methyldiethanolamine + Water and Methanol + 2-Amino-2-methyl-1-propanol + Water Systems
Pvap	7.44	kPa	371.40	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	8.14	kPa	373.00	Investigation of the isothermal (vapour + liquid) equilibria of aqueous 2-amino-2-methyl-1-propanol (AMP), N-benzylethanolamine, or 3-dimethylamino-1-propanol solutions at several temperatures
Pvap	8.00	kPa	373.25	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	9.94	kPa	377.20	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	10.00	kPa	377.39	Ternary Isobaric Vapor-Liquid Equilibria of Methanol + N-Methyldiethanolamine + Water and Methanol + 2-Amino-2-methyl-1-propanol + Water Systems
Pvap	12.00	kPa	381.35	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	16.00	kPa	388.05	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	19.90	kPa	392.30	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	20.00	kPa	392.71	Ternary Isobaric Vapor-Liquid Equilibria of Methanol + N-Methyldiethanolamine + Water and Methanol + 2-Amino-2-methyl-1-propanol + Water Systems
Pvap	20.00	kPa	393.05	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	24.00	kPa	397.25	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	28.00	kPa	401.05	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	29.90	kPa	402.10	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	30.00	kPa	402.56	Ternary Isobaric Vapor-Liquid Equilibria of Methanol + N-Methyldiethanolamine + Water and Methanol + 2-Amino-2-methyl-1-propanol + Water Systems
Pvap	32.00	kPa	404.45	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	36.00	kPa	407.75	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	39.90	kPa	409.50	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	40.00	kPa	410.35	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	44.00	kPa	412.95	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	48.00	kPa	415.15	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	49.90	kPa	415.60	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	50.00	kPa	415.99	Ternary Isobaric Vapor-Liquid Equilibria of Methanol + N-Methyldiethanolamine + Water and Methanol + 2-Amino-2-methyl-1-propanol + Water Systems
Pvap	50.70	kPa	416.65	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	53.30	kPa	418.15	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	57.30	kPa	419.95	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	61.30	kPa	421.85	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	65.00	kPa	423.00	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	65.30	kPa	423.65	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	66.70	kPa	424.45	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	70.00	kPa	425.48	Ternary Isobaric Vapor-Liquid Equilibria of Methanol + N-Methyldiethanolamine + Water and Methanol + 2-Amino-2-methyl-1-propanol + Water Systems
Pvap	69.30	kPa	425.55	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	73.30	kPa	427.15	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	80.00	kPa	429.20	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	80.00	kPa	429.65	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	80.00	kPa	429.75	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	85.30	kPa	431.85	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	90.70	kPa	433.65	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	96.00	kPa	435.35	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	100.00	kPa	436.20	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	101.30	kPa	436.85	Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
Pvap	120.00	kPa	442.10	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	140.00	kPa	447.30	Vapor Pressures of Several Commercially Used Alkanolamines
Pvap	160.00	kPa	452.00	Vapor Pressures of Several Commercially Used Alkanolamines
ρl	[900.70; 930.52]	kg/m3	[298.15; 333.15]
ρl	930.52	kg/m3	298.15	Densities and Viscosities of Aqueous Ternary Mixtures of 2-(Methylamino)ethanol and 2-(Ethylamino)ethanol with Diethanolamine, Triethanolamine, N-Methyldiethanolamine, or 2-Amino-1-methyl-1-propanol from 298.15 to 323.15 K
ρl	926.40	kg/m3	303.15	Densities and Viscosities of Aqueous Ternary Mixtures of 2-(Methylamino)ethanol and 2-(Ethylamino)ethanol with Diethanolamine, Triethanolamine, N-Methyldiethanolamine, or 2-Amino-1-methyl-1-propanol from 298.15 to 323.15 K
ρl	922.26	kg/m3	308.15	Densities and Viscosities of Aqueous Ternary Mixtures of 2-(Methylamino)ethanol and 2-(Ethylamino)ethanol with Diethanolamine, Triethanolamine, N-Methyldiethanolamine, or 2-Amino-1-methyl-1-propanol from 298.15 to 323.15 K
ρl	917.20	kg/m3	313.15	Density and Viscosity of Aqueous Blends of Three Alkanolamines: N-Methyldiethanolamine, Diethanolamine, and 2-Amino-2-methyl-1-propanol in the Range of (303 to 343) K
ρl	918.08	kg/m3	313.15	Densities and Viscosities of Aqueous Ternary Mixtures of 2-(Methylamino)ethanol and 2-(Ethylamino)ethanol with Diethanolamine, Triethanolamine, N-Methyldiethanolamine, or 2-Amino-1-methyl-1-propanol from 298.15 to 323.15 K
ρl	913.87	kg/m3	318.15	Densities and Viscosities of Aqueous Ternary Mixtures of 2-(Methylamino)ethanol and 2-(Ethylamino)ethanol with Diethanolamine, Triethanolamine, N-Methyldiethanolamine, or 2-Amino-1-methyl-1-propanol from 298.15 to 323.15 K
ρl	909.20	kg/m3	323.15	Density and Viscosity of Aqueous Blends of Three Alkanolamines: N-Methyldiethanolamine, Diethanolamine, and 2-Amino-2-methyl-1-propanol in the Range of (303 to 343) K
ρl	909.62	kg/m3	323.15	Densities and Viscosities of Aqueous Ternary Mixtures of 2-(Methylamino)ethanol and 2-(Ethylamino)ethanol with Diethanolamine, Triethanolamine, N-Methyldiethanolamine, or 2-Amino-1-methyl-1-propanol from 298.15 to 323.15 K
ρl	900.70	kg/m3	333.15	Density and Viscosity of Aqueous Blends of Three Alkanolamines: N-Methyldiethanolamine, Diethanolamine, and 2-Amino-2-methyl-1-propanol in the Range of (303 to 343) K
csound,fluid	[1386.93; 1501.44]	m/s	[293.15; 323.15]
csound,fluid	1501.44	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	1501.44	m/s	293.15	Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of (Monoethanolamine + 2-Amino-2-methyl-1-propanol), (Monoethanolamine + Triethanolamine), and (Monoethanolamine + N-Methyldiethanolamine) at Temperatures from (293.15 to 323.15) K
csound,fluid	1483.44	m/s	298.15	Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of (Monoethanolamine + 2-Amino-2-methyl-1-propanol), (Monoethanolamine + Triethanolamine), and (Monoethanolamine + N-Methyldiethanolamine) at Temperatures from (293.15 to 323.15) K
csound,fluid	1483.44	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	1461.22	m/s	303.15	Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of (Monoethanolamine + 2-Amino-2-methyl-1-propanol), (Monoethanolamine + Triethanolamine), and (Monoethanolamine + N-Methyldiethanolamine) at Temperatures from (293.15 to 323.15) K
csound,fluid	1461.22	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	1442.40	m/s	308.15	Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of (Monoethanolamine + 2-Amino-2-methyl-1-propanol), (Monoethanolamine + Triethanolamine), and (Monoethanolamine + N-Methyldiethanolamine) at Temperatures from (293.15 to 323.15) K
csound,fluid	1442.40	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	1423.80	m/s	313.15	Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of (Monoethanolamine + 2-Amino-2-methyl-1-propanol), (Monoethanolamine + Triethanolamine), and (Monoethanolamine + N-Methyldiethanolamine) at Temperatures from (293.15 to 323.15) K
csound,fluid	1423.80	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	1405.28	m/s	318.15	Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of (Monoethanolamine + 2-Amino-2-methyl-1-propanol), (Monoethanolamine + Triethanolamine), and (Monoethanolamine + N-Methyldiethanolamine) at Temperatures from (293.15 to 323.15) K
csound,fluid	1405.28	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	1386.93	m/s	323.15	Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of (Monoethanolamine + 2-Amino-2-methyl-1-propanol), (Monoethanolamine + Triethanolamine), and (Monoethanolamine + N-Methyldiethanolamine) at Temperatures from (293.15 to 323.15) K
csound,fluid	1386.93	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

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	340.50	K	1.30	NIST

Datasets

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
313.06	1000.00	931.4
313.06	2000.00	931.9
313.06	3000.00	932.4
313.06	4000.00	932.9
313.06	5000.00	933.5
313.06	6000.00	933.9
313.06	7000.00	934.5
313.06	8000.00	935.0
313.06	9007.00	935.5
313.06	10003.00	936.0
313.06	11000.00	936.6
313.06	12000.00	937.0
313.06	13000.00	937.6
313.06	14000.00	938.1
313.06	15002.00	938.6
313.06	16000.00	939.1
313.06	17001.00	939.7
313.06	18002.00	940.2
313.06	19000.00	940.6
313.06	20029.00	941.1
313.06	21004.00	941.7
313.06	22004.00	942.1
313.06	24004.00	943.1
322.98	500.00	922.7
322.98	1000.00	922.8
322.98	2000.00	923.4
322.98	3000.00	924.0
322.98	4000.00	924.5
322.98	5000.00	925.1
322.98	6000.00	925.7
322.98	7000.00	926.2
322.98	8000.00	926.8
322.98	9007.00	927.4
322.98	10002.00	927.8
322.98	11000.00	928.4
322.98	12000.00	928.9
322.98	13000.00	929.5
322.98	14000.00	930.1
322.98	15003.00	930.6
322.98	16006.00	931.1
322.98	17001.00	931.6
322.98	18002.00	932.1
322.98	19000.00	932.6
322.98	20030.00	933.2
322.98	21005.00	933.7
322.98	22004.00	934.1
322.98	24004.00	935.2
332.91	500.00	914.0
332.91	1000.00	914.4
332.91	2000.00	915.0
332.91	3000.00	915.6
332.91	4000.00	916.1
332.91	5000.00	916.7
332.91	6000.00	917.3
332.91	7000.00	918.0
332.91	8000.00	918.5
332.91	9009.00	919.1
332.91	10003.00	919.7
332.91	11002.00	920.2
332.91	12001.00	920.8
332.91	13000.00	921.3
332.91	14000.00	921.9
332.91	15002.00	922.4
332.91	16001.00	923.0
332.91	17001.00	923.5
332.91	18002.00	924.1
332.91	19000.00	924.6
332.91	20030.00	925.2
332.91	21002.00	925.6
332.91	22004.00	926.2
332.91	23000.00	926.7
332.91	24004.00	927.3
342.84	500.00	905.4
342.84	1000.00	905.7
342.84	2000.00	906.4
342.84	3000.00	907.0
342.84	4000.00	907.6
342.84	5000.00	908.3
342.84	6000.00	908.9
342.84	7000.00	909.5
342.84	8001.00	910.1
342.84	9009.00	910.7
342.84	10003.00	911.3
342.84	11001.00	911.9
342.84	12000.00	912.5
342.84	13000.00	913.1
342.84	14000.00	913.6
342.84	15003.00	914.3
342.84	16001.00	914.8
342.84	17001.00	915.3
342.84	18002.00	915.9
342.84	19000.00	916.5
342.84	20030.00	917.1
342.84	21005.00	917.6
342.84	22004.00	918.1
342.84	23000.00	918.7
342.84	24004.00	919.2
352.79	500.00	896.8
352.79	1000.00	897.2
352.79	2000.00	897.9
352.79	3000.00	898.5
352.79	4001.00	899.2
352.79	5000.00	899.9
352.79	6000.00	900.5
352.79	7001.00	901.2
352.79	8000.00	901.8
352.79	9009.00	902.4
352.79	10003.00	903.1
352.79	11001.00	903.7
352.79	12000.00	904.3
352.79	13001.00	904.9
352.79	14000.00	905.5
352.79	15002.00	906.1
352.79	16001.00	906.7
352.79	17001.00	907.4
352.79	18002.00	907.9
352.79	18997.00	908.5
352.79	20030.00	909.1
352.79	21001.00	909.7
352.79	22004.00	910.3
352.79	23000.00	910.9
352.79	24004.00	911.4
362.65	504.00	888.0
362.65	1002.00	888.4
362.65	2000.00	889.0
362.65	3000.00	889.7
362.65	4000.00	890.5
362.65	5000.00	891.2
362.65	6000.00	891.8
362.65	7000.00	892.5
362.65	8001.00	893.2
362.65	9010.00	893.9
362.65	10003.00	894.6
362.65	11001.00	895.2
362.65	12000.00	895.8
362.65	13001.00	896.5
362.65	14000.00	897.1
362.65	15003.00	897.8
362.65	16001.00	898.4
362.65	17000.00	899.1
362.65	18002.00	899.7
362.65	19000.00	900.3
362.65	20030.00	901.0
362.65	21004.00	901.6
362.65	22004.00	902.2
362.65	23000.00	902.8
362.65	24003.00	903.3
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[335.92; 462.54]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.61365e+01
Coefficient B			-4.32398e+03
Coefficient C			-6.30950e+01
Temperature range, min.			335.92
Temperature range, max.			462.54
Pvap	1.33	kPa	335.92	Calculated Property
Pvap	2.90	kPa	349.99	Calculated Property
Pvap	5.87	kPa	364.06	Calculated Property
Pvap	11.14	kPa	378.13	Calculated Property
Pvap	20.04	kPa	392.20	Calculated Property
Pvap	34.34	kPa	406.26	Calculated Property
Pvap	56.41	kPa	420.33	Calculated Property
Pvap	89.23	kPa	434.40	Calculated Property
Pvap	136.50	kPa	448.47	Calculated Property
Pvap	202.66	kPa	462.54	Calculated Property

Similar Compounds

Find more compounds similar to 1-Propanol, 2-amino-2-methyl-.

Mixtures

• Water + 1-Propanol, 2-amino-2-methyl-
• 1,6-Hexanediamine + Water + 1-Propanol, 2-amino-2-methyl-
• Piperazine + Water + 1-Propanol, 2-amino-2-methyl-
• 2-Propanol, 1-amino- + Water + 1-Propanol, 2-amino-2-methyl-
• 1-Propanol, 3-amino- + Water + 1-Propanol, 2-amino-2-methyl-
• Ethanol, 2-(methylamino)- + Water + 1-Propanol, 2-amino-2-methyl-
• Ethanol, 2-(ethylamino)- + Water + 1-Propanol, 2-amino-2-methyl-
• Methyl Alcohol + 1-Propanol, 2-amino-2-methyl-
• Methyl Alcohol + Water + 1-Propanol, 2-amino-2-methyl-
• Monoethanolamine + 1-Propanol, 2-amino-2-methyl-
• 2-Propanol, 1-amino-, (R)- + 1-Propanol, 2-amino-2-methyl-
• 1-Propanol, 3-amino- + 1-Propanol, 2-amino-2-methyl-
• Methyldiethanolamine + Water + 1-Propanol, 2-amino-2-methyl-
• Piperazine + 1-Propanol, 2-amino-2-methyl-
• Carbon dioxide + Water + 1-Propanol, 2-amino-2-methyl-
• Monoethanolamine + Water + 1-Propanol, 2-amino-2-methyl-
• Diethanolamine + Water + 1-Propanol, 2-amino-2-methyl-
• Nitrous oxide + Water + 1-Propanol, 2-amino-2-methyl-
• Nitrous oxide + Diethanolamine + 1-Propanol, 2-amino-2-methyl-

Sources

• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Measurement and thermodynamic modeling of the phase equilibrium of aqueous 2-amino-2-methyl-1-propanol solutions
• The solubility measurement and modeling of CO2 in aqueous solution of N-methyldiethanolaminen + 2-amino-2-methyl-1- propanol + piperazine at high pressures
• Experimental investigation of the density and viscosity of CO2-loaded aqueous alkanolamine solutions
• Experimental measurement and Kent-Eisenberg modelling of CO2 solubility in aqueous mixture of 2-amino-2-methyl-1-propanol and hexamethylenediamine
• Liquid heat capacity of the solvent system (piperazine + 2-amino-2-methyl-lpropanol + water)
• Investigation of the isothermal (vapour + liquid) equilibria of aqueous 2-amino-2-methyl-1-propanol (AMP), N-benzylethanolamine, or 3-dimethylamino-1-propanol solutions at several temperatures
• (Vapour + liquid) equilibria (VLE) of CO2 in aqueous solutions of 2-amino-2-methyl-1-propanol: New data and modelling using eNRTL-equation
• Experimental analysis and modeling of CO2 solubility in AMP (2-amino-2-methyl-1-propanol) at low CO2 partial pressure using the models of Deshmukh-Mather and the artificial neural network
• Experimental and theoretical investigation of solubility of carbon dioxide in concentrated aqueous solution of 2-amino-2-methyl-1-propanol and piperazine
• Experiments and model for the viscosity of carbonated 2-amino-2-methyl-1-propanol and piperazine aqueous solution
• Solubility and thermodynamic modeling of hydrogen sulfide in aqueous (diisopropanolamine + 2-amino-2-methyl-1-propanol + piperazine) solution at high pressure
• Solid Solubility in the Aqueous 2-Amino-2-methyl-propanol (AMP) Plus Piperazine (PZ) System
• 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
• Volumetric Properties and Viscosities for Aqueous AMP Solutions from 25 0C to 70 0C
• Vapor-Liquid Equilibrium of CO2 in Aqueous Solutions of 2-Amino-2-methyl-1-propanol
• Density and Viscosity of Aqueous Solutions of (N-Methyldiethanolamine + Monoethanolamine), (N-Methyldiethanolamine + Diethanolamine), (2-Amino-2-methyl-1-propanol + Monoethanolamine) and (2-Amino-2-methyl-1-propanol + Diethanolamine
• Physical Solubility and Diffusivity of N2O and CO2 into Aqueous Solutions of (2-Amino-2-methyl-1-propanol + Diethanolamine) and (N-Methyldiethanolamine + Diethanolamine)
• Mutual Diffusion Coefficients of Some Aqueous Alkanolamines Solutions
• Density and Viscosity of Aqueous Solutions of Piperazine and (2-Amino-2-methyl-1-propanol + Piperazine) from 298 to 333 K
• Density and Viscosity of Aqueous Blends of Three Alkanolamines: N-Methyldiethanolamine, Diethanolamine, and 2-Amino-2-methyl-1-propanol in the Range of (303 to 343) K
• Densities and Viscosities of Aqueous Ternary Mixtures of 2-(Methylamino)ethanol and 2-(Ethylamino)ethanol with Diethanolamine, Triethanolamine, N-Methyldiethanolamine, or 2-Amino-1-methyl-1-propanol from 298.15 to 323.15 K
• Density and Viscosity of Aqueous Solutions of (N-Methyldiethanolamine + Piperazine) and (2-Amino-2-methyl-1-propanol + Piperazine) from (288 to 333) K
• Density and Viscosity of Aqueous Solutions of (2-Piperidineethanol + Piperazine) from (288 to 333) K and Surface Tension of Aqueous Solutions of (N-Methyldiethanolamine + Piperazine), (2-Amino-2-methyl-1-propanol + Piperazine), and (2-Piperidineethanol + Piperazine) from (293 to 323) K
• Ternary Isobaric Vapor-Liquid Equilibria of Methanol + N-Methyldiethanolamine + Water and Methanol + 2-Amino-2-methyl-1-propanol + Water Systems
• Density and Surface Tension of Aqueous Solutions of (2-(Methylamino)-ethanol +2-Amino-2-methyl-1-propanol) and (2-(Methylamino)-ethanol + N-Methyl-diethanolamine) from (298.15 to 323.15) K
• Physical Properties of Aqueous Solutions of Piperazine and (2-Amino-2-methyl-1-propanol + Piperazine) from (298.15 to 333.15) K
• Vapor Pressures of Several Commercially Used Alkanolamines
• Aqueous Solubility of Piperazine and 2-Amino-2-methyl-1-propanol plus Their Mixtures Using an Improved Freezing-Point Depression Method
• Densities and Derived Thermodynamic Properties of 2-Amino-2-methyl-1-propanol + Water Mixtures at Temperatures from (313 to 363) K and Pressures up to 24 MPa
• Density, Speed of Sound, Isentropic Compressibility, and Excess Volume of (Monoethanolamine + 2-Amino-2-methyl-1-propanol), (Monoethanolamine + Triethanolamine), and (Monoethanolamine + N-Methyldiethanolamine) at Temperatures from (293.15 to 323.15) K
• 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

Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.