Author
Listed:
- Roger A. Khalil
(SINTEF Energy Research, P.O. Box 4761 Torgarden, NO-7465 Trondheim, Norway)
- Sethulakshmy Jayakumari
(SINTEF Industry, P.O. Box 4760 Torgarden, NO-7465 Trondheim, Norway)
- Halvor Dalaker
(SINTEF Industry, P.O. Box 4760 Torgarden, NO-7465 Trondheim, Norway)
- Liang Wang
(SINTEF Energy Research, P.O. Box 4761 Torgarden, NO-7465 Trondheim, Norway)
- Pål Tetlie
(SINTEF Industry, P.O. Box 4760 Torgarden, NO-7465 Trondheim, Norway)
- Øyvind Skreiberg
(SINTEF Energy Research, P.O. Box 4761 Torgarden, NO-7465 Trondheim, Norway)
Abstract
To reach agreed-on climate goals, it is necessary to develop new energy carriers and industrial materials that are carbon-neutral. To combat global warming and keep Earth’s temperature from increasing by 1.5 °C, some of these solutions need to be carbon-negative. This study fulfills this criterion by producing clean hydrogen and biocarbon suitable for the metallurgic industry through the thermal decomposition of methane using biocarbon as a catalyst. Five different biomass samples were used to prepare biocarbons at a pyrolysis temperature of 1000 °C with a holding time of 90 min. When methane was cracked at 1100 °C with a holding time of 90 min, the highest hydrogen production was 105 mol/kg biocarbon, achieved using birch bark. The lowest hydrogen yield, of 68 mol/kg biocarbon, was achieved with steam-explosion pellets. All the biocarbons showed substantial carbon deposition from cracked methane on their surfaces, with the highest deposition on birch bark and spruce wood biocarbons of 42% relative to the biocarbon start weight. The carbon deposition increased with the decomposition temperature, the methane share in the purge gas and the holding time. The steam-explosion pellets, after deactivation, had a CO 2 reactivity that was comparable to coke, a reducing agent that is commonly used in manganese-producing industries. About 90% of the potassium and sodium were removed from the biocarbon during catalytic decomposition of methane performed at 1100 °C. The alkali removal was calculated relative to the biocarbon produced under the same conditions, but with 100% N 2 purge instead of CH 4 . After catalytic decomposition, the surface area of the biocarbon was reduced by 11–34%, depending on the biocarbon type.
Suggested Citation
Roger A. Khalil & Sethulakshmy Jayakumari & Halvor Dalaker & Liang Wang & Pål Tetlie & Øyvind Skreiberg, 2025.
"Catalytic Methane Decomposition for the Simultaneous Production of Hydrogen and Low-Reactivity Biocarbon for the Metallurgic Industry,"
Energies, MDPI, vol. 18(3), pages 1-26, January.
Handle:
RePEc:gam:jeners:v:18:y:2025:i:3:p:558-:d:1576676
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