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CO2 capture into aqueous solutions of piperazine activated 2-amino-2-methyl-1-propanol
被引:117
|作者:
Bruder, Peter
[1
]
Grimstvedt, Andreas
[2
]
Mejdell, Thor
[2
]
Svendsen, Hallvard F.
[1
]
机构:
[1] Norwegian Univ Sci & Technol NTNU, Dept Chem Engn, NO-7491 Trondheim, Norway
[2] SINTEF Mat & Chem, NO-7465 Trondheim, Norway
关键词:
Piperazine (PZ);
2-amino-2-methyl-1-propanol (AMP);
Absorption;
Thermodynamics process;
Mathematical modeling;
Phase equilibria;
CARBON-DIOXIDE;
METHYLDIETHANOLAMINE SOLUTIONS;
LIQUID-EQUILIBRIUM;
ABSORPTION;
SOLUBILITY;
MONOETHANOLAMINE;
MIXTURES;
KINETICS;
DIETHANOLAMINE;
SELECTION;
D O I:
10.1016/j.ces.2011.08.051
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
In this work, experimental data and a simplified vapor-liquid equilibrium (VLE) model for the absorption of CO2 into aqueous solutions of piperazine (PZ) activated 2-amino-2-methyl-1-propanol (AMP) are reported. The purpose of the work was to find the AMP/PZ system with the highest concentration and cyclic capacity, which could be used in the industry without forming solid precipitations at operational temperatures. The effect of the AMP/PZ ratio and the total concentration level of amine was studied. The highest possible ratio of AMP/PZ, which does not form solid precipitates during the absorption of CO2 at 40 degrees C (40 wt% amine), was identified. Considering the maximum loading found in the screening tests for AMP/PZ (3+1.5 M) and for 30 wt% MEA systems, the AMP/PZ system has about 128% higher specific cyclic capacity if operating between 40 and 80 degrees C, and almost twice the CO2 partial pressure at 120 degrees C compared to MEA. (C) 2011 Elsevier Ltd. All rights reserved.
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页码:6193 / 6198
页数:6
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