A synopsis of the published literature on removal of CO 2 from a flue gas is given. A novel thermal swing chemisorption (TSC) process concept is proposed for removal and recovery of compressed CO 2 from a flue gas without precompression, predrying, or precooling. The process uses Na 2 O promoted alumina as a reversible CO 2 selective chemisorbent in conjunction with the principles of rapid thermal swing adsorption for direct production of compressed CO 2 from a flue gas. Several complementary process steps are used in the design to compress the product CO 2 and to achieve high CO 2 recovery and sorbent capacity utilization. Judicious steam purge steps are used for highly efficient sorbent regeneration and to minimize the steam requirement. The CO 2 chemisorption characteristics of the sorbent are reviewed and a model simulation of the TSC process performance is reported.
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Lee et al. (2008) studied this question.
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