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U.S. Department of Energy
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Advancing Post-Combustion CO2 Capture through Increased Mass Transfer and Lower Degradation

Technical Report ·
DOI:https://doi.org/10.2172/1906480· OSTI ID:1906480
 [1];  [2];  [2];  [2];  [2];  [2]
  1. Univ. of Kentucky, Lexington, KY (United States); University of Kentucky
  2. Univ. of Kentucky, Lexington, KY (United States)
The over-arching goal of the proposed project is to develop three techniques to enable aqueous post-combustion CO2 capture technologies to meet the DOE performance and cost targets of 90% CO2 capture, 95% purity, at a cost of less than $30/tonne CO2 captured. This will be accomplished by the development of materials and processes to increase mass transfer in the absorber and reduce the environmental impacts. While constantly working to reduce the cost of CO2 capture via solvent development and process & heat integration, increasing CO2 mass transfer through development of custom dynamic packing materials and tuning solvent physical properties may offer a route to increased solvent capacity, lower energy consumption and reduced aerosol formation. The environmental concerns that have been identified in amine-based CO2 capture systems, nitrosamines specifically, are another critical element that will be addressed in this project. The specific objectives of the project were to: 1) conduct detailed studies to understand how solvent physical properties and aerosol formation are impacted by additives; 2) quantify the CO2 mass transfer improvement from the dynamic polarity packing in the absorber and the additive-modified solvent using the existing UK bench-scale CO2 capture unit; 3) quantify the energy consumption savings associated with enhanced mass transfer; 4) quantify the benefits of the UK’s electrochemical cell to decompose nitrosamines; and 5) collect the necessary information/data to conduct a high-level TEA assessment of the proposed technologies. The project involved the fabrication and installation of customized dynamic polarity packing and an investigation into the understanding of the impact of chemical additives on solvent properties to increase CO2 mass transfer in the absorber column, and lastly the design of an electrochemical cell to decompose nitrosamines in a water wash. After both systems were fabricated, they were tested at UK facilities, including on the bench-scale CO2 capture unit under parametric and long-term operation.
Research Organization:
Univ. of Kentucky, Lexington, KY (United States)
Sponsoring Organization:
USDOE Office of Fossil Energy (FE)
DOE Contract Number:
FE0031661
OSTI ID:
1906480
Report Number(s):
DOE-UK-31661
Country of Publication:
United States
Language:
English