منوی کاربری
  • پشتیبانی: ۴۲۲۷۳۷۸۱ - ۰۴۱
  • سبد خرید

دانلود رایگان مقاله تاثیر دی اکسید گوگرد بر فعالیت مرتبه ای کاتالیزور مبتنی بر پالادیم

عنوان فارسی
تاثیر دی اکسید گوگرد بر فعالیت مرتبه ای کاتالیزور مبتنی بر پالادیم در احتراق متان
عنوان انگلیسی
The effect of sulfur dioxide on the activity of hierarchical Pd-based catalysts in methane combustion
صفحات مقاله فارسی
0
صفحات مقاله انگلیسی
12
سال انتشار
2017
نشریه
الزویر - Elsevier
فرمت مقاله انگلیسی
PDF
کد محصول
E220
رشته های مرتبط با این مقاله
شیمی و مهندسی محیط زیست
گرایش های مرتبط با این مقاله
شیمی کاتالیست و آلودگی هوا
مجله
تجزیه کاربردی B: محیط زیست - Applied Catalysis B: Environmental
دانشگاه
گروه علوم شیمیایی و صنایع دارویی، دانشگاه تریست، ایتالیا
کلمات کلیدی
دی اکسید گوگرد، کاتالیزور اکسیداسیون متان، پالادیوم، سریا-زیرکونیا، XPS
۰.۰ (بدون امتیاز)
امتیاز دهید
چکیده

Abstract


SO2 poisoning of methane oxidation over alumina-supported, Pd@CexZr1−xO2 nanoparticle catalysts was systematically studied by means of advanced PhotoElectron Spectroscopy (PES) methods. The Pd@CexZr1−xO2 units were synthesized and deposited on two modified-alumina supports, i.e. high surface area modified alumina and a model alumina prepared by Atomic Layer Deposition (ALD) of alumina on Indium Tin Oxide (ITO)/quartz slides. The model support was designed to be suitable for PES analysis and was stable to high temperature treatments (850 °C). Characterization of the high-surface-area (HSA) catalysts by X-Ray Diffraction (XRD), N2 physisorption, CO chemisorption and Transmission Electron Microscopy (TEM) indicated formation of CeO2–ZrO2 (CZ) mixed-oxide crystallites that stabilize the Pd active phase against sintering. Correlation of methane-oxidation rates with PES results demonstrated two distinct mechanisms for deactivation by SO2. Below 450 °C, the presence of SO2 in the feed led to partial reduction of the active PdO phase and to the formation of sulfates on the Pd. Above 500 °C, poisoning by SO2 was less severe due to spillover of the sulfates onto the oxide promoter. Pd@ZrO2 catalysts showed the best resistance to SO2 poisoning, outperforming analogous Pd@CZ mixed-oxide catalysts, because there was less sulfate formation and the sulfates that did form could be removed during regeneration.

نتیجه گیری

5. Conclusions


The self-assembly methodology described previously [32] was modified in order to synthesize nanostructured Pd@CexZr1−xO2 (Pd@MOx) units in the whole compositional range (0 < x < 1). The synthesis of dispersed Pd@MOx allowed the preparation of a series of high-surface-area Si-Al2O3 supported catalysts and model catalysts having similar nanostructure and surface chemistry. Comparison of results on the two types of catalysts allowed the SO2 poisoning ofmethane oxidationonPd-basedcatalysts to be systematically studied to elucidate the role of the MOx promoter and the aging conditions. At lower temperatures (<450 ◦C), the PdO active phase is irreversibly poisoned by SO2 due to interaction with sulfates which are not able to spillover to the support/promoter. At higher temperatures (>500 ◦C), poisoning is slowed by formation of sulfate species on the oxide promoter. Due to partial decomposition of sulfates at 500 ◦C, Pd@ZrO2-based catalysts showed the best sulfur-poisoning resistance, attaining complete regeneration even after prolonged aging, and thus they are the best candidates for real application. Pd@Ce0.6Zr0.4O2 catalysts showed intermediate sulfur tolerance compared to Pd@CeO2 and Pd@ZrO2, in agreement with previously reported results [23]. The high chemical sensitivity of PES techniques provided direct evidence for previously suggested formation of sulfate species on individual metal cations in CexZr1−xO2 mixed oxides [23]. Finally, the modelcatalyst approaches developed here should allow the study of metal-support interactions in other catalytically relevant systems by simply varying the ALD-deposited thin film composition.


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