Solubility of carbon dioxide in aqueous blends of 2-amino-2-methyl-1-propanol and piperazine
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Published version
Author(s)
Tong, D
Maitland, GC
Trusler, MJP
Fennell, PS
Type
Journal Article
Abstract
In this work, we report new solubility data for carbon dioxide in aqueous blends of 2-amino-2-methyl-1-propanol (AMP) and piperazine (PZ). A static-analytical apparatus, validated in previous work, was employed to obtain the results at temperatures of (313.2, 333.2, 373.2, 393.2) K, and at total pressures up to 460 kPa. Two different solvent blends were studied, both having a total amine mass fraction of 30%: (25 mass% AMP+5 mass% PZ) and (20 mass% AMP+10 mass% PZ). Comparisons between these PZ activated aqueous AMP systems and 30 mass% aqueous AMP have been made in terms of their cyclic capacities under typical scrubbing conditions of 313 K in the absorber and 393 K in the stripper. The Kent–Eisenberg model was used to correlate the experimental data.
Date Issued
2013-06-05
Date Acceptance
2013-05-17
Citation
Chemical Engineering Science, 2013, 101, pp.851-864
ISSN
0009-2509
Publisher
Elsevier
Start Page
851
End Page
864
Journal / Book Title
Chemical Engineering Science
Volume
101
Copyright Statement
© 2013 The Authors. Published by Elsevier Ltd. Open access under CC BY license (https://creativecommons.org/licenses/by/3.0/)
Identifier
http://gateway.webofknowledge.com/gateway/Gateway.cgi?GWVersion=2&SrcApp=PARTNER_APP&SrcAuth=LinksAMR&KeyUT=WOS:000323603700081&DestLinkType=FullRecord&DestApp=ALL_WOS&UsrCustomerID=1ba7043ffcc86c417c072aa74d649202
Subjects
Science & Technology
Technology
Engineering, Chemical
Engineering
ENGINEERING, CHEMICAL
Gas absorption
Vapour-liquid equilibria
Sterically-hindered amines
AMP
PZ
Kent-Eisenberg model
STERICALLY HINDERED AMINES
EQUILIBRIUM SOLUBILITY
POTASSIUM CARBONATE
CO2 ABSORPTION
MASS-TRANSFER
KINETICS
METHYLDIETHANOLAMINE
MONOETHANOLAMINE
MIXTURES
WATER
Chemical Engineering
0904 Chemical Engineering
0913 Mechanical Engineering
Publication Status
Published