Glycerol steam reforming to syngas over Ni-based catalysts on commercial Linde-type 5A zeolite modified by metal oxides
Autor: | Chenghua Xu, Jun Chen, Yong-Xiang Zhang, Jue Meng, Hui-Wen Xiao, Zun-Yu Huang, Chang-Fu Zheng |
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Rok vydání: | 2014 |
Předmět: |
Materials science
Process Chemistry and Technology Inorganic chemistry Pollution Water-gas shift reaction law.invention Catalysis Steam reforming Metal Chemical engineering law Methanation visual_art visual_art.visual_art_medium Chemical Engineering (miscellaneous) Calcination Zeolite Waste Management and Disposal Syngas |
Zdroj: | Journal of Environmental Chemical Engineering. 2:598-604 |
ISSN: | 2213-3437 |
DOI: | 10.1016/j.jece.2013.10.015 |
Popis: | Metal oxides-modified Ni-based catalysts for glycerol steam reforming (GSR) to syngas were prepared by impregnation using commercial Ca-containing Linde-type 5A zeolite (LTA) as support, and characterized by XRD, N2-adsorption, CO2-TPD, H2-TPR, and TPO. The XRD and CO2-TPD results indicated that the introduction of alkali and rare earth metals could modify the basic property of Ni/LTA catalysts. H2-TPR results indicated that the simultaneous presence of Mo–La oxides and nonskeletal CaO in Ni/LTA weakened the strong interaction between Ni active metal species and support (SIMS). The catalytic test showed that increase on basic property of Ni/LTA catalysts was helpful to improving glycerol conversion to syngas and inhibiting water–gas shift reaction and methanation during GSR. The Ni/MoLaCa-LTA with a weakened SIMS gave rise to the formation of smaller NiO particles, and exhibited a stable production capacity of gas with a H2/CO ratio of around 2.17, and exhibited no deactivation during 100 h time-on-stream. Although Ni/MoZrCa-LTA in GSR was rapidly deactivated due to carbon deposit after running 40 h, the spent catalyst could be on-line regenerated by calcination at 700 °C in an air flow, which could also be proved by TPO results of spent catalysts. |
Databáze: | OpenAIRE |
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