Frimpong, Reynolds A.
; Nikolic, Heather
; Liu, Kunlei
; ... - International journal of energy for a clean environment
The size of columns in traditional absorption-based processes for CO
2 capture contributes significantly to the overall capital cost. A demonstrated method to reduce the cost of point source CO
2 capture, focusing on reducing the absorber height by increasing the liquid-to-gas reaction contact area and decreasing the CO
2 diffusion resistance without increasing gas-side pressure drop is presented along with techno-economic analysis results. Bench-scale tests on the unique Compact Absorber showed overall CO
2 mass transfer enhancement of varying degrees compared to a traditional packed column for similar process conditions, demonstrating that a 60+% reduction in size of a typical post-combustion absorber with
more » a packing height of 70-100 ft and total height of 150-180 ft can be achieved. The techno-economic analysis showed significant cost reductions when the Compact Absorber is combined with other transformative aspects of the University of Kentucky Institute for Decarbonization and Energy Advancement point source CO2 capture process compared to the U.S. Department of Energy National Energy Technology Laboratory pertinent reference case for pulverized coal plants with CO2 capture. Here, a levelized cost of electricity excluding CO2 transportation and storage of $$\$$95.6$/MWh was estimated, which is a 9% reduction, with a total capital cost contribution of $45/MWh, which is a 12% reduction. Additionally, a breakeven CO2 sales price also referred to as the cost of CO2 capture, of $36.70/tonne was estimated when the UK hindered primary amine solvent is used, which is a 20% reduction compared to the reference case.« less