کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
146173 456363 2015 10 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Fluidized bed ODH of ethane to ethylene over VOx–MoOx/γ-Al2O3 catalyst: Desorption kinetics and catalytic activity
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
پیش نمایش صفحه اول مقاله
Fluidized bed ODH of ethane to ethylene over VOx–MoOx/γ-Al2O3 catalyst: Desorption kinetics and catalytic activity
چکیده انگلیسی


• ODH of ethane is studied using VOx–MoOx/γ-Al2O3 as catalyst/source of oxygen.
• TPR, XRD, Raman, and FTIR analysis show availability of VOx, MoOx on γ-Al2O3.
• NH3-TPD kinetics analysis shows low activation energy of NH3 desorption.
• Low desorption energy confirms easy availability of lattice oxygen for ODH.
• ODH of ethane in fluidized conditions gives high ethylene selectivity.

Oxidative dehydrogenation (ODH) of ethane is studied in a gas phase oxygen free conditions using a VOx–MoOx/γ-Al2O3 catalyst which also acts as a carrier of lattice oxygen. The prepared catalyst and the support γ-Al2O3 are characterized using various physicochemical techniques. XRD, Raman, and FTIR analysis show the availability of VOx and MoOx species on the alumina support. The TPR analysis gives two distinct peaks for the reduction of VOx and MoOx species, respectively. The cyclic TPR/TPO shows consistent reduction behavior of the catalyst over repeated reduction and oxidation cycles. Desorption kinetics analysis reveals low activation energy for ammonia desorption from VOx–MoOx/γ-Al2O3 surface. This indicates a minimum interaction between VOx–MoOx and γ-Al2O3 confirming easy availability of lattice oxygen for reaction. The ODH of ethane experiments are conducted in a fluidized CREC Riser Simulator at temperature range of 500–650 °C. The contact time is varied between 10 and 50 s. Under the studied reaction conditions, ethylene, carbon dioxide, carbon monoxide and water are the major products. At fluidized condition, VOx–MoOx/γ-Al2O3 shows significant higher ethane conversion due to the intense mixing between the catalyst and the feed. High temperature and longer contact times lead to further oxidation of the desired product ethylene to give undesired products COx. In repeated ODH of ethane and re-oxidation cycles, VOx–MoOx/γ-Al2O3 shows stable ethane conversion and product selectivity which is consistent to the TPR/TPO evaluation results.

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ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Chemical Engineering Journal - Volume 278, 15 October 2015, Pages 207–216
نویسندگان
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