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Characteristics of Methanol Steam Reforming Catalyzed by Cu⁃Mn⁃Al Ternary Spinel
Changhe LÜ, Dianqing WU, Kaiwen ZHANG, Dongbei YU, Caishun ZHANG, Jiao HAN, Zhixian GAO
Abstract15)   HTML1)    PDF (1808KB)(4)      

Cu0.7Mn0.3Al2.5 ternary solid solution spinel catalysts were prepared by ball milling method using copper nitrate as the copper source, proposed thin alumina as the aluminium source, citric acid as the additive, and manganese acetate as the third component to partially replace copper. With the help of characterisation techniques such as XRD, BET, H2?TPR and XPS, the crystalline phase structure, weaving properties, reducing properties and surface cation states and distributions of Cu0.7Mn0.3Al2.5 were investigated. The catalytic performance of Cu0.7Mn0.3Al2.5 in methanol steam reforming (MSR) for hydrogen production with a sustained release feature was scrutinized, and a comparison was made with CuAl2.5 binary spinel and Cu0.7Zn0.3Al2.5 ternary spinel catalysts. The results showed that compared with CuAl2.5 and Cu0.7Zn0.3Al2.5, the Cu0.7Mn0.3Al2.5 exhibited the maximum contraction of the unit cell, resulting in a smaller unit cell constant. The catalyst had smaller crystalline size and higher specific surface area. The catalyst showed an aluminium?rich state, but with a higher percentage of Cu in the surface spinel phase, which made the reduction under H2 atmosphere more difficult, and exhibited a better slow?release catalytic performance in MSR hydrogen production. Under the conditions of a reaction temperature of 265 °C, n(H2O)/n(CH3OH) =2, and mass flow rate of 2.25 h-1, a stable conversion rate of 84% was achieved for 40 hours. The study provided valuable data reference for the development of efficient copper?based sustained?release catalysts.

2024, 37 (2): 50-57. DOI: 10.12422/j.issn.1006-396X.2024.02.007
Effects of Hydrothermal Reaction Time on the Performance of CuO/CeO 2 Catalyst for Hydrogen Production from Steam Reforming Methanol
Xinyu Yang, Shu Sun, Yan Shi, Xu Feng, Jiao Han, Caishun Zhang, Lei Zhang, Zhixian Gao
Abstract234)   HTML8)    PDF (1384KB)(218)      

CeO2?X (X is the hydrothermal synthesis time, X=3, 6, 12, 24 h) carriers were prepared by varying the hydrothermal synthesis time using Ce(NO3)3·6H2O and urea as raw materials, and CuO/CeO2?X catalysts were obtained by isovolumetric impregnation with active component Cu, which were applied to methanol steam reforming (MSR) reaction. The effects of hydrothermal synthesis time on the structure and physicochemical properties of the prepared CeO2?X carriers and CuO/CeO2?X catalysts were explored by XRD, BET, H2?TPR.The performances of the CuO/CeO2?X catalyst samples were evaluated in methanol steam reforming(MSR) reaction.The results show that the CuO/CeO2?6 has good catalytic activity. At the reaction temperature of 280 °C, when the molar ratio of water to methanol was 1.2, and the space velocity of methanol vapor (GHSV) was 800 h-1, the methanol conversion rate could reach 92.8%.

2023, 36 (2): 63-69. DOI: 10.12422/j.issn.1006-396X.2023.02.008