کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
60808 47548 2015 11 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Skeletal isomerisation of oleic acid over ferrierite: Influence of acid site number, accessibility and strength on activity and selectivity
کلمات کلیدی
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی کاتالیزور
پیش نمایش صفحه اول مقاله
Skeletal isomerisation of oleic acid over ferrierite: Influence of acid site number, accessibility and strength on activity and selectivity
چکیده انگلیسی


• Ferrierite shows high activity and selectivity in alkyl isomerisation of oleic acid.
• Initial pore conversion correlates with Brønsted acidity in the 10-MR channels.
• A low density of external acid sites reduces oligomerisation.
• High branching yield is linked to a high ratio of Brønsted to Lewis acid sites.
• Few but strong Brønsted acid sites in the 10-MR channels favour mono-branching.

Protonated ferrierite shows superior activity and selectivity in the liquid-phase isomerisation of linear unsaturated fatty acids to (mono-)branched-chain unsaturated fatty acids, (Mo)BUFA. This high selectivity is remarkable, as most of the interior surface of the zeolite is blocked already at the onset of reaction, limiting reaction to the pore mouth. A detailed study of the relationship between ferrierite acidity and performance is reported for five commercial catalysts; significant differences were found, independently of their bulk Si/Al ratios. Initial pore conversion correlates with Brønsted acidity in the 10-MR channels, as determined by adsorption/desorption of pyridine and FTIR. A low density of external acid sites reduces oligomerisation of fatty acids, while a high ratio of Brønsted to Lewis sites explains the observed high BUFA yield. The combination of FTIR with CO adsorption, and temperature-programmed desorption of NH3, confirms that the presence of strong but few Brønsted acid sites in the 10-MR channels increases selectivity to MoBUFA.

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ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Journal of Catalysis - Volume 329, September 2015, Pages 195–205
نویسندگان
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