Effect of absorption enthalpy on temperature-swing CO2 separation process performance
Elsevier BV, 2011
Online
academicJournal
Zugriff:
We model a CO2 absorption process to elucidate the rationale for the search for a solvent with an enthalpy of absorption (ΔH) of low magnitude. We explore the relationship between ΔH and the system’s performance. While in general a lower magnitude appears to provide better system performance because it permits the stripper temperature to be decreased, as the magnitude drops below its value for monoethanolamine amine (MEA), 80 kJ/mol, the required solvent mass flow rate must increase precipitously and/or the flue gas must be cooled significantly. We argue that the associated parasitic pumping and cooling loads, as well as the increased capital cost, may set a practical lower limit on the magnitude of the enthalpy of absorption that is not very different from that of MEA.
Engineering and Applied Sciences
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Effect of absorption enthalpy on temperature-swing CO2 separation process performance
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Autor/in / Beteiligte Person: | van Nierop, Ernst A. ; Hormoz, Sahand ; House, Kurt Z. ; Aziz, Michael J. |
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Veröffentlichung: | Elsevier BV, 2011 |
Medientyp: | academicJournal |
ISSN: | 1876-6102 (print) |
DOI: | 10.1016/j.egypro.2011.02.054 |
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