کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
147852 456400 2014 10 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Comparison of Ni and Ni–Ce/Al2O3 catalysts in granulated and structured forms: Their possible use in the oxidative dehydrogenation of ethane reaction
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
پیش نمایش صفحه اول مقاله
Comparison of Ni and Ni–Ce/Al2O3 catalysts in granulated and structured forms: Their possible use in the oxidative dehydrogenation of ethane reaction
چکیده انگلیسی


• Ni and Ni–Ce/Al2O3 coatings on metallic foams were active and selective for the ODE.
• The cerium addition increased considerably the ethylene productivity.
• Catalytic features of the structured systems depend on the calcination temperature.
• The presence of chromium in the catalytic coatings mainly affects the selectivity.
• The structured systems showed higher ethylene productivity than powder catalysts.

Ni and Ni–Ce/Alumina catalysts in structured form were prepared, characterized by different techniques and tested in the oxidative dehydrogenation of ethane (ODE). In order to gain further insight into active species, catalysts in granulated form were also synthesized, characterized and evaluated in the same reaction test.The results indicated that the Ni and Ni–Ce/Al2O3 granulated catalysts were active and selective for this reaction. The addition of cerium using two atomic ratios (Ce/Ni = 0.11 and 0.25) significantly increased the ethylene productivity by kg of nickel mainly motivated by the marked increment in ethane conversion. This behavior could be explained by the smaller nickel oxide crystallite size and the incorporation of nickel into the ceria lattice.The structured systems showed similar active species but achieved a better performance in terms of ethane conversion and ethylene productivity, compared with the granulated forms. The higher catalytic activity could be associated with the presence of lower crystallite sizes of the active phases and also related to a better utilization of active sites due to a higher accessibility of the reagents to the catalyst surface.The existence of certain species (mainly chromium oxide) in the coverage also contributed to obtain higher conversion even though the selectivity to ethylene decreased. Lower temperature treatments applied to the structured support (550 °C instead of 700 °C) reduced the amount of these undesired species that favor the total oxidation of ethane.

Figure optionsDownload as PowerPoint slide

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Chemical Engineering Journal - Volume 246, 15 June 2014, Pages 343–352
نویسندگان
, , , ,