فهرس المقالات Gamma-alumina

• حرية الوصول المقاله
  • صفحة الملخص
  • نص كامل
  
  1 - CATALYTIC REFORMING OF n-HEPTANE ON PLATINUMNIOBIUM SUPPORTED ON GAMMA-ALUMINA
  Mehdi Vadi Gholamreza Farmani Hamidreza Seyedjafari M. Sohrabi
  The series of mono-metallic and bi-metallic catalysts have been prepared by impregnatingwith solutions containing compound of H2PtC15,NbC15 and lml HC1 (0.1 mol). The activityand selectivity of the catalysts have been determined under conditions at 450-500°C, 15-30a أکثر

  The series of mono-metallic and bi-metallic catalysts have been prepared by impregnatingwith solutions containing compound of H2PtC15,NbC15 and lml HC1 (0.1 mol). The activityand selectivity of the catalysts have been determined under conditions at 450-500°C, 15-30atm. Molar ratio H2/C7H16=5 and VVH=1.5/h for converting n-heptane. Under theseexperimental conditions it has been established that the conversion of n-heptane intobranched aliphatic isomers is catalyzed by a bifunctional mechanism. The results show thatwhen Nb is present, the catalysts are much more stable and have much higher selectivities forisomerization reaction. At a given conversion the bimetallic catalysts produce much lowerconcentrations of cracked products. It is shown that Nb modifies the acidity of the support,resulting to higher selectivity for isomerization and lower selectivity for cracking and alsomodifies the properties of the Pt. تفاصيل المقالة
• حرية الوصول المقاله
  • صفحة الملخص
  • نص كامل
  
  2 - Catalytic Reforming of n-Heptane on Platimum - Rhenium Supported on Gamma-Alumina
  M. Vadi M. Bazargani N. Astaneh M. Alipour
  Catalyitic reforming is one of the refinery processes in catalyst conversion that results to anincreases in octane number of naphtan which leads to production of gasoline with higher octanenumber. Hydrocarbons with high octan number that are produced in reforming proces أکثر

  Catalyitic reforming is one of the refinery processes in catalyst conversion that results to anincreases in octane number of naphtan which leads to production of gasoline with higher octanenumber. Hydrocarbons with high octan number that are produced in reforming process are as;aromatics, paraffins, isomers and etc.Not only Aromatics are used as fuel for motors but they are also useful in petrochemical industry.Also hydrogen is produced as a subsidiary in the process. In this research, platinium-rhenium isused as a catalyst with the combination of "Re=0.4"and"Pt=0.3".the activity and selectivity of thecatalysts have been determined under condition at 350- 450oC and 30at. Pressure molar ratioH2/C7H16=5 and VVH=1.5 mL/h.Our results proved that this catalyst produces good products under 30 atmosphere pressure andtemperature ranges between 350 - 450oC but at higher temperatures such as 490 oC and over willgenerate lots of cracking and low quality black products that can not be analyzed bychromatography. This shows that in these temperatures the action of cracking is very much.However in temperature lower than 490 oC, the products have yellow color and this shows theexistence of aromatic compounds.In comparison between two catalysts with different percentages 0.3Pt=0.4Re catalyst has moreactivity. It also shows more selectivity in aromatization in comparison with 0.3Pt-0.3Re catalyst. تفاصيل المقالة
• حرية الوصول المقاله
  • صفحة الملخص
  • نص كامل
  
  3 - CATALYTIC REFORMING OF n-HEPTANE ON PLATINUM-TUNGSTEN SUPPORTED ON GAMMA-ALUMINA
  M. Vadi A. Safavi A. Jamshidi
  The mono-metallic and bi-metallic catalysts have been prepared by impregnating with solutions containing a compound of H2PtCl6,WO3 and 1ml HCl (0.1 mol). It should be noted that the catalysts’ activity and selectivity have been determined under these conditions : أکثر

  The mono-metallic and bi-metallic catalysts have been prepared by impregnating with solutions containing a compound of H2PtCl6,WO3 and 1ml HCl (0.1 mol). It should be noted that the catalysts’ activity and selectivity have been determined under these conditions : 450-5000C ,and 15-25atm by H2. For converting n-heptane , the molar ratio H2/C7H16 is 5 , and LHSV is 1.5ml/h. It has been proved that , under these experimental conditions , the conversion of n-heptane into branched aliphatic isomers is catalyzed by a bifunctional mechanism. The results indicate that in the presence of W , the catalysts have much higher selectivity and stability for isomerization reaction. At a given conversion , the bi-metallic catalysts produce much lower concentrations of cracked products. According to the tests , W modifies the support acidity resulting to the higher selectivity for isomerization and the lower one for cracking , and it also modifies the Pt properties تفاصيل المقالة
• حرية الوصول المقاله
  • صفحة الملخص
  • نص كامل
  
  4 - Determination of Activity and Selectivity of n-Heptane by Reforming Catalytic Pt-V Supported on gamma-Alumina
  Mahdi Vadi Najimeh Astaneh
  Bimetallic Pt-V supported by Gamma-alumina is used to observe the changes of nheptanewhen passed over this catalyst. The Pt concentration was kept constant at0.1wt% while the concentration of the vanadium was 0.5wt%. The activity andselectivity of catalyst have been det أکثر

  Bimetallic Pt-V supported by Gamma-alumina is used to observe the changes of nheptanewhen passed over this catalyst. The Pt concentration was kept constant at0.1wt% while the concentration of the vanadium was 0.5wt%. The activity andselectivity of catalyst have been determined under conditions at 450-500 degreescentigrade and 15-30 attn. The experimental results show that the addition of secondmetal to the Pt catalyst results in a modification of the metal and acid functions. Theresults show that when vanadium is present, the catalyst has high selectivity foraromatization reaction. تفاصيل المقالة
• حرية الوصول المقاله
  • صفحة الملخص
  • نص كامل
  
  5 - Operating condition effect on achieving higher propene yield in propane oxidative dehydrogenation process
  Yousef Zeinaly Seyed Mehdi Alavi
  Supported vanadia catalyst was successfully synthesized using wet impregnation of gamma-Alumina to study Propane Oxidative Dehydrogenation (POD). The prepared catalysts were characterized with XRD, BET, and TPR tests. In a broad temperature range (340 to 630°C), eff أکثر

  Supported vanadia catalyst was successfully synthesized using wet impregnation of gamma-Alumina to study Propane Oxidative Dehydrogenation (POD). The prepared catalysts were characterized with XRD, BET, and TPR tests. In a broad temperature range (340 to 630°C), effects of vanadia loading (2.7, 5.4, and 9 wt%) and propane to oxygen ratio (3/1 to 1/3) were investigated on propane conversion as well as propene yield at atmospheric pressure. Results indicate that by increasing the vanadia content the activity of catalyst increases while selectivity to propene decreases monotonically. As the temperature increases from 340°C to 630°C, yield to propene shows ascending behavior in case of all catalyst samples. Yield to propene shows a climax with changing propane to oxygen ratio from 3/1 to 1/3. The yield increases with increase in oxygen partial pressure of feed until equimolar ratio of propane and oxygen, then it declines with further increase of oxygen partial pressure. Higher propene yields were observed at higher temperatures and equimolar feed ratio of propane and oxygen (C3/O2=1/1). A maximum propene yield of 17% was experienced on catalyst with 2.7 wt% vanadia at temperatures at 550°C. تفاصيل المقالة
• حرية الوصول المقاله
  • صفحة الملخص
  • نص كامل
  
  6 - مطالعه هیدروژندارشدن کربن مونوکسید به فراورده باارزش درحضور کاتالیست های آهن با و بدون پیش-برنده بر پایه گاما آلومینا
  ندا چوداری میلانی یحیی زمانی سحر بنی یعقوب علی نخعی پور
  کاتالیست های آهن با و بدون پیش برنده در سنتز فیشر-تروپش با روش آغشته سازی تهیه شدند. این کاتالیست ها با توجه به نسبت وزنی به صورت 20%Fe/γ-Al2O3 و 20%Fe/5%Cu/3%Zr/γ-Al2O3 بودند. کاتالیست ها با روش‌های پراش پرتو ایکس (XRD)، تجزیه عنصری با روش پلاسمای جفت شده القایی (ICP)، أکثر

  کاتالیست های آهن با و بدون پیش برنده در سنتز فیشر-تروپش با روش آغشته سازی تهیه شدند. این کاتالیست ها با توجه به نسبت وزنی به صورت 20%Fe/γ-Al2O3 و 20%Fe/5%Cu/3%Zr/γ-Al2O3 بودند. کاتالیست ها با روش‌های پراش پرتو ایکس (XRD)، تجزیه عنصری با روش پلاسمای جفت شده القایی (ICP)، میکروسکوپی الکترونی روبشی (SEM)، کاهش برنامه ریزی شده گرمایی با هیدروژن (H2-TPR) و روش BET، شناسایی شدند. فعالیت کاتالیست ها در یک واکنشگاه بستر ثابت و در فشار 20 اتمسفر، نسبت H2/CO برابر با 1، دمای 270، 285 و 300 درجه سلسیوس و GHSV برابر با 2، 4 و l.h-1. gcat-1 6 مطالعه شدند. سپس، اثرهای دما، GHSV و پیش برنده های مس و زیرکونیم بر کارایی کاتالیست بررسی شدند. افزایش دما و GHSV موجب تغییر تبدیل CO و گزینش پذیری کاتالست ها نسبت به فراورده ها شد. کاتالیست¬های آهن با پیش برنده، گزینش‌پذیری نسبت به C5+ بالاتری نسبت به کاتالیست بدون پیش برنده داشتند، درحالی که گزینش پذیری نسبت به هیدروکربن های C2-C4 به دلیل استفاده هم زمان از مس و زیرکونیم برای پیش برندگی کاتالیست آهن، کاهش یافت. پیش برنده مس سرعت کاهش Fe2O3 را با ایجاد مکان‌های تفکیک H2 افزایش داد. کارایی کاتالیست های با و بدون پیش¬برنده مورد آزمون واکنشگاهی قرار گرفتند که در آن کاتالیست حاوی پیش برنده کارایی مطلوبی را نشان داد. تفاصيل المقالة