کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
58367 | 47148 | 2006 | 7 صفحه PDF | دانلود رایگان |
عنوان انگلیسی مقاله ISI
Dehydrogenation of paraffins: synergies between catalyst design and reactor engineering
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کلمات کلیدی
موضوعات مرتبط
مهندسی و علوم پایه
مهندسی شیمی
کاتالیزور
پیش نمایش صفحه اول مقاله
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چکیده انگلیسی
The dehydrogenation of paraffins, especially in the C3–C5 range, is a widely exploited way for large-scale production of pure olefins. Its industrial application is however complicated by clashing kinetic and thermodynamic constraints. The nature of these constraints is illustrated and the solutions proposed by different technology providers in terms of catalyst composition/morphology and selection of the type of reactor and means for supplying reaction heat are discussed. The solution to achieve an economically attractive commercial implementation lies in defining the optimal synergy between catalyst design and reactor engineering. Potential new ways to olefins are also examined.
ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Catalysis Today - Volume 111, Issues 1–2, 15 January 2006, Pages 133–139
Journal: Catalysis Today - Volume 111, Issues 1–2, 15 January 2006, Pages 133–139
نویسندگان
Domenico Sanfilippo, Ivano Miracca,