Heat-Stable Salts and Methods for Their Removal from Alkanolamine Carbon Dioxide Absorbents (Review)


Cite item

Full Text

Open Access Open Access
Restricted Access Access granted
Restricted Access Subscription Access

Abstract

Absorption using aqueous solutions of alkanolamines is the most widely used procedure for removal of carbon dioxide from natural gas, flue gases from power-generating facilities, and other mixtures. Its main drawback is degradation/deactivation of alkanolamine under the process conditions (high temperatures, presence of oxygen and other impurities) with the formation of heat-stable salts consisting of alkanolammonium cation and anions of organic and inorganic acids. The main operation problems caused by heat-stable salts are considered in the review. Three main methods for removal of heat-stable salts from alkanolamine adsorbents are described in detail: distillation, ion exchange, and electrodialysis. The main characteristics of these methods and their advantages and drawbacks are described, and a comparative analysis is made. The history and state-of-the art of studies within the framework of each method are presented.

About the authors

S. D. Bazhenov

Topchiev Institute of Petrochemical Synthesis

Author for correspondence.
Email: sbazhenov@ips.ac.ru
Russian Federation, Moscow, 119991

E. G. Novitskii

Topchiev Institute of Petrochemical Synthesis

Email: sbazhenov@ips.ac.ru
Russian Federation, Moscow, 119991

V. P. Vasilevskii

Topchiev Institute of Petrochemical Synthesis

Email: sbazhenov@ips.ac.ru
Russian Federation, Moscow, 119991

E. A. Grushevenko

Topchiev Institute of Petrochemical Synthesis

Email: sbazhenov@ips.ac.ru
Russian Federation, Moscow, 119991

A. A. Bienko

PAO VNIPIgasdobycha

Email: sbazhenov@ips.ac.ru
Russian Federation, Moscow, 119415

A. V. Volkov

Topchiev Institute of Petrochemical Synthesis

Email: sbazhenov@ips.ac.ru
Russian Federation, Moscow, 119991

Supplementary files

Supplementary Files
Action
1. JATS XML

Copyright (c) 2019 Pleiades Publishing, Ltd.