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01-3780

Sigma-Aldrich

2-Amino-2-methyl-1-propanol

SAJ first grade, ≥98.0%

Synonym(s):

β-Aminoisobutyl alcohol, AMP

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About This Item

Linear Formula:
(CH3)2C(NH2)CH2OH
CAS Number:
124-68-5
Molecular Weight:
89.14
Beilstein:
505979
EC Number:
204-709-8
MDL number:
MFCD00008051
UNSPSC Code:
12352104
PubChem Substance ID:
329747260
grade:
SAJ first grade
Assay:
≥98.0%
bp:
165 °C (lit.)
vapor pressure:
<1 mmHg ( 25 °C)
Pricing and availability is not currently available.

grade

SAJ first grade

vapor density

3 (vs air)

vapor pressure

<1 mmHg ( 25 °C)

Assay

≥98.0%

availability

available only in Japan

refractive index

n20/D 1.4455 (lit.)

useful pH range

9.0-10.5

pKa (25 °C)

9.7

bp

165 °C (lit.)

mp

24-28 °C (lit.)

density

0.934 g/mL at 25 °C (lit.)

SMILES string

CC(C)(N)CO

InChI

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

InChI key

CBTVGIZVANVGBH-UHFFFAOYSA-N

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Pictograms

Corrosion
GHS05

Signal Word

Danger

Hazard Statements

H315,H318,H412

Hazard Classifications

Aquatic Chronic 3 - Eye Dam. 1 - Skin Irrit. 2

Storage Class Code

11 - Combustible Solids

WGK

WGK 1

Flash Point(F)

179.8 °F - closed cup

Flash Point(C)

82.1 °C - closed cup

Personal Protective Equipment

dust mask type N95 (US), Eyeshields, Gloves

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Certificates of Analysis (COA)

Lot/Batch Number
G7441
G5443
G4435
G6362
G3337

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Sontaya Limmatvapirat et al.
European journal of pharmaceutics and biopharmaceutics : official journal of Arbeitsgemeinschaft fur Pharmazeutische Verfahrenstechnik e.V, 67(3), 690-698 (2007-06-20)
The objective of this study was to improve the properties of shellac by composite salts formation. The shellac samples were prepared in various salt forms by dissolving them with 2-amino-2-methyl-1-propanol (AMP) and ammonium hydroxide (AMN) at various ratios of AMP:AMN.
Shia-Chung Chen et al.
Journal of environmental management, 92(4), 1083-1090 (2011-01-05)
In this study, the absorption of carbon dioxide using an absorbent composed of 2-amino-2-methyl-L-propanol (AMP) + monoethanolamine (MEA) + piperazine (PZ) in asymmetric and symmetric polytetrafluoroethylene (PTFE) membrane contactors was investigated. Experiments were conducted using various gas flow rates, liquid
Muhammad Hasib-ur-Rahman et al.
Environmental science & technology, 46(20), 11443-11450 (2012-09-12)
One of the major drawbacks of aqueous alkanolamine based CO(2) capture processes is the requirement of significantly higher energy of regeneration. This weakness can be overcome by separating the CO(2)-captured product to regenerate the corresponding amine, thus avoiding the consumption
Vishal Govind Rao et al.
The journal of physical chemistry. B, 115(14), 3828-3837 (2011-03-23)
In this work we have shown a comparative study of changes in physicochemical properties of an aqueous solution of a common cationic surfactant cetyltrimethylammonium bromide (CTAB) upon addition of two protic ionic liquids N,N-dimethylethanolammonium [corrected] hexanoate (DAH) and N,N-dimethylethanolammonium [corrected]
Chia-Chang Lin et al.
Journal of hazardous materials, 175(1-3), 344-351 (2009-11-17)
The removal of CO(2) from a 10 vol% CO(2) gas by chemical absorption with 30 wt% alkanolamine solutions containing monoethanolamine (MEA), piperazine (PZ), and 2-amino-2-methyl-1-propanol (AMP) in the cross-flow rotating packed bed (RPB) was investigated. The CO(2) removal efficiency increased
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