Lars Erik Øi
Department of and Process, Energy and Environmental Technology, University College of Southeast Norway
Erik Sundbø
Department of and Process, Energy and Environmental Technology, University College of Southeast Norway
Hassan Ali
Department of and Process, Energy and Environmental Technology, University College of Southeast Norway
Ladda ner artikelhttp://dx.doi.org/10.3384/ecp17138298Ingår i: Proceedings of the 58th Conference on Simulation and Modelling (SIMS 58) Reykjavik, Iceland, September 25th – 27th, 2017
Linköping Electronic Conference Proceedings 138:40, s. 298-303
Publicerad: 2017-09-27
ISBN: 978-91-7685-417-4
ISSN: 1650-3686 (tryckt), 1650-3740 (online)
A standard method for CO2 capture is by absorption in
an amine based solvent followed by desorption. Such
plants are traditionally designed for removal of 85-90 %
CO2 from the exhaust gas as a reasonable trade-off
between high removal efficiency and low investment.
The major challenge is the high energy demand for CO2
desorption. In many industrial cases, a limited amount
of cheap waste heat is available and this makes partial
CO2 capture an interesting option. It is not obvious
whether a high removal efficiency from a part of the
exhaust or a low removal efficiency from the total
exhaust is the optimum solution. In this work,
simulations of traditional and vapor recompression
processes are performed, and it is found that vapour
recompression treating the total exhaust is energy
optimum. A traditional process with a low absorption
column treating the total exhaust gives the lowest cost
per ton CO2 captured.
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