Electrified methane steam reforming on a washcoated SiSiC foam for low‐carbon hydrogen production

Mo-based catalysts for CH4/H2S reforming to hydrogen production: effect of hydroxyl concentration of the support

High concentration of H₂S in acidic natural gas will lead to poisoning of catalysts for hydrogen production by methane steam reforming, thus limiting the further use of natural gas. Reforming CH₄ by H₂S can be considered as an alternative route to hydrogen production from methane. This process not only achieves the removal of H₂S but also obtains chemical raw material CS₂ and clean energy H₂. By impregnating the Mo source on SiO₂ treated with hydrogen peroxide and then using the catalyst in the CH₄/H₂S reforming reaction, we surprisingly found that the conversion rate of CH₄ and H₂S increased from 28 and 32% to 34% and 43%, respectively, after hydrogen peroxide treatment. The H₂ production rate and the yield of CS₂ increased from 20 mmolH₂/(g_Mo*min) and 52% to 30 mmolH₂/(g_Mo*min) and 65%, respectively. Combining with characterization methods such as X-ray diffraction (XRD), hydrogen temperature programmed reduction (H₂-TPR), ¹H-based solid-state nuclear magnetic resonance (¹H MAS NMR), X-ray photoelectron spectroscopy (XPS), Raman spectra (RS), and transmission electron microscopy (TEM), we found that the hydroxyl concentration of the support increased after hydrogen peroxide treatment, which led to the strengthening of the force between the metal and the support, which was easy to form low-level and small-size MoS₂, exposing more active sites, and further improving the catalytic activity. This method provides a new idea for hydrogen production by CH₄/H₂S reforming and the development of high-performance MoS₂-based catalysts.