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- 2012 AIChE Annual Meeting
- Sustainable Engineering Forum
- CO2 Capture, Control and Sequestration II
- (481a) Integration of Post-Combustion Capture with Compression and Liquefaction Process of CO2
In this study, a process simulation including both post-combustion capture of CO2 using MEA absorbent and multi-stage compression was performed using Aspen Plus®. Different physical property methods were selected for each process to allow more stable and accurate simulation. [1] It was assumed that the compressed (liquefied) CO2 will be transported via CO2 carrier, which requires appropriate specifications of CO2 for ship loading. [2] In addition, 4-stage compression system with intercooling was adopted where both cold and hot utilities are available from compression as well as isenthalpic expansion. A quantitative analysis of how these utilities can be used was carried out so that the energy required for capture as well as the overall process was reduced.
This research was supported by a grant from the LNG Plant R&D Center funded by the Ministry of Land, Transportation and Maritime Affairs (MLTM) of the Korean government.
References:
[1] Van Wagener, D.H., Rochelle, G.T., 2011. Stripper configurations for CO2capture by aqueous monoethanolamine, Chem. Eng. Res. Des. 89, 1639-1646.
[2] Aspelund A., Jordal, K., 2007. Gas Conditioning–The interface between CO2 capture and transport, Int. J. Greenhouse Gas Control, 1(3), 343-354.