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dc.contributor.authorLu, R.
dc.contributor.authorLi, K.
dc.contributor.authorChen, J.
dc.contributor.authorYu, H.
dc.contributor.authorTade, Moses
dc.date.accessioned2017-11-24T05:24:21Z
dc.date.available2017-11-24T05:24:21Z
dc.date.created2017-11-24T04:48:51Z
dc.date.issued2017
dc.identifier.citationLu, R. and Li, K. and Chen, J. and Yu, H. and Tade, M. 2017. CO<inf>2</inf>capture using piperazine-promoted, aqueous ammonia solution: Rate-based modelling and process simulation. International Journal of Greenhouse Gas Control. 65: pp. 65-75.
dc.identifier.urihttp://hdl.handle.net/20.500.11937/58180
dc.identifier.doi10.1016/j.ijggc.2017.08.018
dc.description.abstract

© 2017 Elsevier Ltd Due to the fast reaction rate of piperazine (PZ) with CO 2 , it has the potential to act as a promoter in aqueous ammonia (NH 3 )-based CO 2 capture processes. We have developed a rigorous, rate-based model for the NH 3 –PZ–CO 2 –H 2 O system using Aspen Plus ® , and validated the model against experimental results. Absorption and desorption processes were simulated under real flue gas conditions to gain a practical understanding of the behaviour and characteristics of interactions between PZ-promoted NH 3 solution and CO 2 . Adding PZ significantly increased the CO 2 absorption rate in the NH 3 -based CO 2 capture process via a fast reaction between PZ carbamate and CO 2 . The temperature along the column was higher than in the absence of PZ, and more free ammonia was released into the solution, which led to higher ammonia loss. Adding PZ also reduced the stripping heat, resulting in a smaller energy requirement for solvent regeneration.

dc.publisherElsevier
dc.titleCO<inf>2</inf>capture using piperazine-promoted, aqueous ammonia solution: Rate-based modelling and process simulation
dc.typeJournal Article
dcterms.source.volume65
dcterms.source.startPage65
dcterms.source.endPage75
dcterms.source.issn1750-5836
dcterms.source.titleInternational Journal of Greenhouse Gas Control
curtin.accessStatusFulltext not available
curtin.facultyFaculty of Science and Engineering


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