Solar methane pyrolysis in a liquid metal bubble column reactor: Effect of medium type and gas injection configuration

Solar methane pyrolysis in different molten media and reactor configurations was experimented to improve hydrogen production. Pure Sn, Ni 0.18 Sn 0.82 , Cu 0.45 Bi 0.55 , and KCl melts were compared at three different temperatures (1030–1130–1230 °C), and no significant difference was observed except for KCl and only at 1230 °C (X CH4 = 72 % vs. 57 % for pure Sn). This enhanced performance was attributed to possible carbon dispersion in the salt, which probably modified the physical properties and enhanced hydrodynamics. A porous quartz sparger (downward injection) did not significantly enhance the bubbles hydrodynamics, mainly because bubbles were trapped and coalesced below the sintered disc. A custom-made sparger (lateral bubbling) did not either improve conversion due to non-uniform pores. A sparger with an upward injection should be preferred to generate small bubbles with longer residence time. When a solid bed of tungsten carbide particles was placed around the injector, overlaid by molten tin, the conversion was improved even at a relatively low temperature (X CH4 = 17 % at 1030 °C). The immersed bed likely behaved as a porous device and increased the gas-solid surface contact. Combining particle bed and liquid bubbling system is very promising for further optimization of methane pyrolysis in molten media. The carbon collected above molten metals showed mostly a sheet-like structure with significant metal contamination. In case of KCl, most carbon was entrained with the gas, while the remaining was mixed with KCl in the reactor. The density of KCl is close to that of carbon, which prevented a good separation. • Solar methane pyrolysis in molten media was studied using a bubble column reactor. • The molten medium type (Sn, NiSn, CuBi, KCl) only slightly influenced CH 4 conversion. • Carbon was separated at the surface of molten metals, whereas dispersed in KCl salt. • Downward or lateral gas injection through porous spargers induced bubbles coalescence. • A bed of dense WC particles immersed in liquid tin improved CH 4 pyrolysis performance.

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Publication Details

Journal
Journal of Analytical and Applied Pyrolysis
Published
2024-09-12
DOI
https://doi.org/10.1016/j.jaap.2024.106756
Citations
10
Primary Topic
Catalytic Processes in Materials Science
Type
article
Field-Weighted Citation Impact
1.17

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article

Solar methane pyrolysis in a liquid metal bubble column reactor: Effect of medium type and gas injection configuration

Malek Msheik, Sylvain Rodat, Stéphane Abanades
10 citations
Journal of Analytical and Applied Pyrolysis
Catalytic Processes in Materials Science
1.17
article

Solar methane pyrolysis in a liquid metal bubble column reactor: Effect of medium type and gas injection configuration

Malek Msheik, Sylvain Rodat, Stéphane Abanades
article en
10 citations

Abstract

Solar methane pyrolysis in different molten media and reactor configurations was experimented to improve hydrogen production. Pure Sn, Ni 0.18 Sn 0.82 , Cu 0.45 Bi 0.55 , and KCl melts were compared at three different temperatures (1030–1130–1230 °C), and no significant difference was observed except for KCl and only at 1230 °C (X CH4 = 72 % vs. 57 % for pure Sn). This enhanced performance was attributed to possible carbon dispersion in the salt, which probably modified the physical properties and enhanced hydrodynamics. A porous quartz sparger (downward injection) did not significantly enhance the bubbles hydrodynamics, mainly because bubbles were trapped and coalesced below the sintered disc. A custom-made sparger (lateral bubbling) did not either improve conversion due to non-uniform pores. A sparger with an upward injection should be preferred to generate small bubbles with longer residence time. When a solid bed of tungsten carbide particles was placed around the injector, overlaid by molten tin, the conversion was improved even at a relatively low temperature (X CH4 = 17 % at 1030 °C). The immersed bed likely behaved as a porous device and increased the gas-solid surface contact. Combining particle bed and liquid bubbling system is very promising for further optimization of methane pyrolysis in molten media. The carbon collected above molten metals showed mostly a sheet-like structure with significant metal contamination. In case of KCl, most carbon was entrained with the gas, while the remaining was mixed with KCl in the reactor. The density of KCl is close to that of carbon, which prevented a good separation. • Solar methane pyrolysis in molten media was studied using a bubble column reactor. • The molten medium type (Sn, NiSn, CuBi, KCl) only slightly influenced CH 4 conversion. • Carbon was separated at the surface of molten metals, whereas dispersed in KCl salt. • Downward or lateral gas injection through porous spargers induced bubbles coalescence. • A bed of dense WC particles immersed in liquid tin improved CH 4 pyrolysis performance.

Journal of Analytical and Applied PyrolysisVol. 183
Centre National de la Recherche Scientifique (FR), Laboratoire Procédés, Matériaux et Energie Solaire (FR)
Centre National de la Recherche Scientifique, CHIST-ERA
Affordable and clean energy
Openalex Percentile: Top 18%
Catalytic Processes in Materials Science
1.17
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