Abstract
A process capable of large-scale formic acid (FA) production via CO2 hydrogenation is presented. This study provides the key strategies for use in developing a viable process for continuous operation. Based on the proposed strategies, a pilot-scale process with a capacity of 10 kg/day was constructed. The continuous operability of the process is demonstrated via pilot plant operation for >100 h, achieving a CO2 conversion rate of 82% and producing FA with a high purity of >92 wt %. Techno-economic analysis and life cycle assessment results of the validated simulation model indicate that the proposed process significantly reduces the level of global warming impact by 42% while cutting the production cost by 37%, compared with the conventional process for producing FA. The contents of this study provide a comprehensive manual for developing a viable CO2 utilization solution, showing economic profitability as well as environmental impact reduction.
Original language | English |
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Pages (from-to) | 693-713 |
Number of pages | 21 |
Journal | Joule |
Volume | 8 |
Issue number | 3 |
DOIs | |
Publication status | Published - 2024 Mar 20 |
Bibliographical note
Publisher Copyright:© 2024 The Authors
Keywords
- CO utilization
- formic acid
- heterogeneous catalysis
- hydrogen storage
- life cycle assessment
- liquid organic hydrogen carrier
- pilot plant
- reactive CO capture and conversion
- single atom catalysis
- techno-economic analysis
ASJC Scopus subject areas
- General Energy