Journal
CHEMSUSCHEM
Volume 4, Issue 9, Pages 1301-1310Publisher
WILEY-BLACKWELL
DOI: 10.1002/cssc.201100220
Keywords
electrochemistry; hydrogen; carbon dioxide; formic acid; renewable resources
Funding
- Det Norske Veritas AS
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The engineering and economic feasibility of large-scale electrochemical reduction of carbon dioxide to formate salts and formic acid is the focus of this Full Paper. In our study we investigated the long-term performance of tin and other proprietary catalysts in the reduction of carbon dioxide to formate/formic acid at a gas/solid/ liquid interface, using a flow-through reactor. The overall economics and energy consumption of the process are evaluated through a value chain analysis. The sensitivity of the net present value of the process to various process parameters is examined.
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