Abstract
A preliminary study based on a conceptual process design methodology that includes a technical evaluation and an economic study has been carried out for the use of the metal-organic framework NH2-MIL-53(Al) as adsorbent for the separation of carbon dioxide from methane. Among the alternatives considered, a vacuum pressure swing adsorption was chosen in the detailed design phase. The combination of a design with columns in parallel and the possibility of recirculating some of the streams ensures a high degree of separation and a final product with high quality without compromising the operation costs. A comparison with the state-of-the-art technology, amine scrubbing, and with a process based on membranes demonstrates that the proposed process is competitive as a result of its low operation costs and the energy demand.
Original language | English (US) |
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Pages (from-to) | 1183-1194 |
Number of pages | 12 |
Journal | Chemical Engineering and Technology |
Volume | 38 |
Issue number | 7 |
DOIs | |
State | Published - Jul 1 2015 |
Externally published | Yes |
Bibliographical note
Publisher Copyright:© 2015 WILEY-VCH Verlag GmbH & Co. KGaA, Weinheim.
Keywords
- CO/CH separation
- Gas separation
- Metal-organic framework
- Natural gas upgrading
- Pressure swing adsorption
ASJC Scopus subject areas
- General Chemistry
- General Chemical Engineering
- Industrial and Manufacturing Engineering