1. Syngas and H2 production from natural gas using CaFe2O4 – Looping: Experimental and thermodynamic integrated process assessment.
- Author
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Riley, Jarrett, Bobek, Michael, Atallah, Chris, Siriwardane, Ranjani, and Bayham, Samuel
- Subjects
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NATURAL gas production , *FERRIC oxide , *SYNTHESIS gas , *STEAM reforming , *FIXED bed reactors , *OXYGEN carriers - Abstract
Experimental methods and thermodynamic simulations were employed in this study to assess the H 2 production potential of a CaFe 2 O 4 based blue H 2 production process from natural gas (NG, >90 vol%CH 4). Fixed bed reactor testing was used to verify the product outcomes. Syngas production from methane using CaFe 2 O 4 was demonstrated. Stable H 2 production with high steam conversion was demonstrated with the CaFe 2 O 4 when reduced with methane. The thermodynamic integrated process simulation enabled simulation of the process in two and three reactor configurations to understand the feasibility of a heat integrated system. The 2-reactor process used the generation of syngas as the prevailing mode for H 2 generation while the 3-reactor system utilized steam water splitting in a dedicated reactor as the prevailing mode to generate H 2. Simulation of the 2-reactor process's FR showed syngas generation similar to the products from fixed bed demonstrations, establishing a connection between thermodynamic simulation and experimental data. The H 2 yield potentials of the various configurations were determined and compared to steam methane reforming with capture (SMR-CCS) and a Fe 2 O 3 based system from the literature. The 2-reactor process has the potential to generate 1.6–2.1 mol of H 2 /mole of NG fed to the system. Three reactor configurations showed the highest potential for H 2 yield with a range of 2.2–2.56 mol of H 2 /mole NG but with the need for additional CCS at the highest yield. A thermal management approach was introduced that combined the chemistries of CaFe 2 O 4 and CuFeAlO 4 which enabled increasing the potential yield to 2.66 mol H 2 /mol NG and enabling a system without the need for addition carbon capture to meet 90% threshold targets. The three reactor cases showed the most competitive performance in comparison to SMR-CCS with up to a 14.6% improvement in H 2 yield. [Display omitted] • Bench scale fixed bed reactor demonstrations for H 2 productions with CaFe 2 O 4. • Thermally integrated H 2 production process screening analysis of 2 and 3 reactor concepts. • 2 reactor concept H 2 yield range: 1.6–1.9 mol H 2 /mol CH 4. • 3 reactor concept H 2 yield range: 2.51–2.66 mol H 2 /mol CH 4. • Novel thermal management strategy using exothermic oxygen carrier (CuFeAlO 4) co-mixing with CaFe 2 O 4. [ABSTRACT FROM AUTHOR]
- Published
- 2023
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