A5888
2-氨基-2-甲基-1-丙醇 盐酸盐
别名:
β-氨基异丁醇 盐酸盐, AMP
方案
≥98% (titration)
表单
crystalline
有效pH范围
9.0-10.5
pKa (25 °C)
9.7
溶解性
water: 0.5 g/mL, clear, colorless
SMILES字符串
Cl.CC(C)(N)CO
InChI
1S/C4H11NO.ClH/c1-4(2,5)3-6;/h6H,3,5H2,1-2H3;1H
InChI key
PMZIUAOBHNJYQT-UHFFFAOYSA-N
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储存分类代码
13 - Non Combustible Solids
WGK
WGK 3
闪点(°F)
Not applicable
闪点(°C)
Not applicable
个人防护装备
Eyeshields, Gloves, type N95 (US)
法规信息
新产品
此项目有
Su-Hsia Lin et al.
Chemosphere, 75(10), 1410-1416 (2009-03-18)
The influence of hydrophobicity in flat-plate porous poly(vinylidene fluoride) (PVDF) and expended polytetrafluoroethylene (PTFE) membranes on CO(2) recovery using aqueous solutions of piperazine (PZ) and alkanolamine is examined. Experiments were conducted at various gas flow rates, liquid flow rates, and
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.
Pei Zhang et al.
Journal of environmental sciences (China), 20(1), 39-44 (2008-06-25)
To improve the efficiency of the carbon dioxide cycling process and to reduce the regeneration energy consumption, a sterically hindered amine of 2-amino-2-methyl-1-propranol (AMP) was investigated to determine its regeneration behavior as a CO2 absorbent. The CO2 absorption and amine
Graeme Puxty et al.
Environmental science & technology, 45(6), 2398-2405 (2011-02-19)
The most common method of carbon dioxide (CO(2)) capture is the absorption of CO(2) into a falling thin film of an aqueous amine solution. Modeling of mass transfer during CO(2) absorption is an important way to gain insight and understanding
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
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