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dc.contributor.authorLi, K.
dc.contributor.authorYu, H.
dc.contributor.authorTade, Moses
dc.contributor.authorFeron, P.
dc.contributor.authorYu, J.
dc.contributor.authorWang, S.
dc.date.accessioned2017-01-30T13:34:24Z
dc.date.available2017-01-30T13:34:24Z
dc.date.created2015-04-16T05:48:09Z
dc.date.issued2014
dc.identifier.citationLi, K. and Yu, H. and Tade, M. and Feron, P. and Yu, J. and Wang, S. 2014. Process Modeling of an Advanced NH3 Abatement and Recycling Technology in the Ammonia-Based CO2 Capture Process. Environmental Science and Technology. 48 (12): pp. 7179-7186.
dc.identifier.urihttp://hdl.handle.net/20.500.11937/32996
dc.identifier.doi10.1021/es501175x
dc.description.abstract

An advanced NH3 abatement and recycling process that makes great use of the waste heat in flue gas was proposed to solve the problems of ammonia slip, NH3 makeup, and flue gas cooling in the ammonia-based CO2 capture process. The rigorous rate-based model, RateFrac in Aspen Plus, was thermodynamically and kinetically validated by experimental data from open literature and CSIRO pilot trials at Munmorah Power Station, Australia, respectively. After a thorough sensitivity analysis and process improvement, the NH3 recycling efficiency reached as high as 99.87%, and the NH3 exhaust concentration was only 15.4 ppmv. Most importantly, the energy consumption of the NH3 abatement and recycling system was only 59.34 kJ/kg CO2 of electricity. The evaluation of mass balance and temperature steady shows that this NH3 recovery process was technically effective and feasible. This process therefore is a promising prospect toward industrial application.

dc.publisherAmerican Chemical Society
dc.titleProcess Modeling of an Advanced NH3 Abatement and Recycling Technology in the Ammonia-Based CO2 Capture Process
dc.typeJournal Article
dcterms.source.volume48
dcterms.source.number12
dcterms.source.startPage7179
dcterms.source.endPage7186
dcterms.source.issn0013-936X
dcterms.source.titleEnvironmental Science and Technology
curtin.departmentDepartment of Chemical Engineering
curtin.accessStatusFulltext not available


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