Abstract
This study presents a first of its kind demonstration of successful enhancement of CO2 chemical absorption, under selected conditions, using a process intensification approach. A multifunctional device that integrates contact of phases and heat exchange has been developed, characterized, and tested. Heat transfer analysis has demonstrated the efficacy of the device as a heat exchanger, and mass transfer results have shown substantial improvement in the uptake of CO2 under a range of operating conditions.
Original language | English |
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Article number | e16285 |
Journal | AIChE Journal |
Volume | 66 |
Issue number | 8 |
DOIs | |
State | Published - Aug 1 2020 |
Funding
This manuscript has been authored by UT‐Battelle, LLC under Contract No. DE‐AC05‐00OR22725 with the U.S. Department of Energy. The United States Government retains and the publisher, by accepting the article for publication, acknowledges that the United States Government retains a non‐exclusive, paid‐up, irrevocable, world‐wide license to publish or reproduce the published form of this manuscript, or allow others to do so, for United States Government purposes. The Department of Energy will provide public access to these results of federally sponsored research in accordance with the DOE Public Access Plan ( http://energy.gov/downloads/doe-public-access-plan ). This research was funded by the Office of Fossil Energy of the U.S. Department of Energy. Technical help by Scott Palko, John Storey, and James Parks II of the Applied Catalysis & Emissions Research Group is gratefully acknowledged.
Keywords
- CO absorption
- heat exchanger reactor
- intensified column packing
- postcombustion CO capture
- process intensification