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جستجوی مقالات مرتبط با کلیدواژه "selectivity" در نشریات گروه "شیمی"

تکرار جستجوی کلیدواژه «selectivity» در نشریات گروه «علوم پایه»
  • آرش وجود، محمد خدادادی مقدم، غلامرضا ابراهیم زاده رجائی*، سحر مهاجری، علی شامل

    در مقاله حاضر، ابتدا واکنش فورموس برای تولید پلی ال ها در حلال متانول و در حضور کاتالیست معدنی آروزیل (فیوم سیلیکا) مورد بررسی قرار گرفته است. مکانیسم واکنش فورموس در واقع همان تراکم آلدولی است که در محیط قلیایی انجام می پذیرد و وجود کاتالیزور ناهمگن آن را تسریع می نماید. محصولات مشاهده شده در محیط واکنش، اتیلن گلیکول و گلیسرآلدهید می باشند. نهایتا گزینش پذیری سنتز این دو محصول پلی الی با دو محصول متناظر سنتز شده از طریق واکنش فورموس در حلال آب مورد مقایسه و ارزیابی قرار گرفت. مطالعه حاضر نشان می دهد که در حضور کاتالیزور فیوم سیلیکا در حلال آب، با افزایش pH از 6/7 تا 3/9 میزان تولید اتیلن گلیکول کاهش می یابد، درحالیکه تبدیل اتیلن گلیکول به گلیسرآلدهید افزایش می یابد. در نتیجه مقدار اتیلن گلیکول موجود در مخلوط واکنش در pH های قلیایی، در مقایسه با pH های خنثی کاهش می یابد، ولی در مقابل، گزینش پذیری واکنش نسبت به تولید گلیسرآلدهید افزایش می یابد. تغییر حلال از آب به متانول نیز باعث کاهش تولید محصول می گردد. بنابراین، این امر نشان دهنده گزینش پذیری پایین محیط متانولی در مقایسه با محیط آبی نسبت به تولید دو محصول 1،2-اتان دی ال و 2،3-دی هیدروکسی پروپانال است.

    کلید واژگان: پیدایش حیات, واکنش فورموس, تراکم آلدولی, حلال متانول, گزینش پذیری, فیوم سیلیکا, پلی ال
    Arash Vojood, Mohammad Khodadadi-Moghaddam, Gholamreza Ebrahimzadeh-Rajaei *, Sahar Mohajeri, Ali Shamel

    In the present paper, the Formose reaction to produce polyols in methanol solvent in the presence of an aerosil (fumed silica) catalyst is first investigated. The mechanism of Formose reaction is actually the same aldol condensation that occurs in an alkaline media and is accelerated by the presence of a heterogeneous catalyst. The products observed in the reaction medium are ethylene glycol and glyceraldehyde. Finally, the selectivity of the synthesis of these products was compared and evaluated with the two corresponding products synthesized through the Formose reaction in aqueous solvent. The present study shows that in the presence of fumed silica catalyst in aqueous solvent, the production of ethylene glycol decreases with increasing pH from 7.6 to 9.3, while the conversion of ethylene glycol to glyceraldehyde increases. As a result, the amount of ethylene glycol in the reaction mixture decreases at alkaline pHs compared to neutral pHs; in contrast, the selectivity of the reaction to the production of glyceraldehyde increases. Changing the solvent from water to methanol also reduces production efficiency. Therefore, it indicates the low selectivity of the methanolic medium compared to the aqueous medium to produce two products, 1,2-ethanediol and 2,3-dihydroxypropanal.

    Keywords: Origin of life, Formose reaction, Aldol condensation, Methanol solvent, Selectivity, Fumed silica, polyol
  • Marzieh Daryanavard, Behzad Mohammadi, Shirin Nadri, Mohammad Joshaghani

    The Mizoroki-Heck coupling reaction has been carried out using Pd(OAc)2 and bisimidazolium (1,1′-methylene-3,3′-bis[(N-(isopropyl)imidazol-2-ylidene]dibromide) for aryl bromides as well as less reactive chlorobenzene with mono- and di-substituted olefins. Only 0.025 mol% of Pd(II) shows a high activity toward the coupling reaction with turnover number (TON) ≈ 600-3960. Further, this catalyst system, Pd(OAc)2/Bisimidazolium, exhibits the excellent selectivity for the trans-isomer coupling products and the terminal arylation coupling products for mono- and di-substituted olefins, respectively. The nature of olefins (n-butyl acrylate, styrene, and 1,1-disubstituted olefins) has a significant contribution on the yield of the coupling products.

    Keywords: Bisimidazolium, Heck reaction, Homogeneous, Mono-, di-substituted olefins, Selectivity
  • زهرا آوخ، محمد شادمان لاکمه سری*، بهمن فرجمند، محمدعلی رضوانی

    وجود ترکیبات گوگردی و مرکاپتان ها در برش های نفتی، موجب آلودگی محیط زیست شده و در خطوط انتقال و مخازن نگهداری، باعث خوردگی می شود. بنابراین لازم است تا مقدار گوگرد و مرکاپتان ها در برش های نفتی تا حد استانداردهای بین الملی کاهش یابد. چارچوب های فلز-آلی دسته ی از جاذب های نانو-متخلخل هستند که برای ذخیره سازی و جداسازی گازها و بهره برداری از انرژی و اصلاح محیط زیست مناسب تشخیص داده شده است. این مقاله با استفاده از آزمایشات تجربی و نیز شبیه سازی مولکولی تلاش می کند تا حذف ترکیبات گوگرددار از بنزین را مورد بررسی قرار دهد. در آزمایش های تجربی گوگردزدایی از تیوفن و بنزوتیوفن که ترکیبات آروماتیک گوگرددار در بنزین هستند به عنوان بنزین مدل شده استفاده شد. فرآیند گوگردزدایی توسط برخی چارچوبهای فلز-آلی با جرم g05/0 در مدت زمان 8 ساعت و در دمای K308 انجام شد. در قسمت شبیه سازی مولکولی نیز برای بنزین یک مدل تعریف شد که شامل مخلوط دوتایی از نرمال-هگزان/بنزوتیوفن، نرمال-هگزان/تیوفن و نرمال-هگزان/اتان تیول بود. مقدار جذب و گزینندگی ترکیبات گوگرددار در چارچوبهای فلز-آلی مورد بررسی قرار گرفت. بهترین جداسازی در مخلوط نرمال-هگزان و ترکیبات گوگرددار مربوط به کسر مولی 01/0 در دمای K318 بود که این مقدار برای مخلوط بنزوتیوفن و نرمال-هگزان برابر با 92/12852، برای مخلوط تیوفن و نرمال-هگزان برابر با 94/628 و برای مخلوط اتان تیول و نرمال-هگزان برابر با 699/50 بدست آمد. نتایج نمودارهای جذب و گزینندگی ترکیبات گوگرددار بر چارچوب های فلز-آلی -در هر دو بخش تجربی و شبیه سازی- نشان داد که MIL-47(V) دارای بیشترین گزینندگی و جذب برای ترکیبات گوگرددار است. در هر دو بخش تجربی و شبیه سازی مولکولی مشخص شد که چارچوبهای فلز-آلی می توانند حذف کننده ی مناسبی برای ترکیبات گوگرددار، جهت بدست آوردن سوخت پاک باشند.

    کلید واژگان: برش های نفتی, چارچوبهای فلز-آلی, گزینندگی, گوگردزدایی, جذب فیزیکی, شبیه سازی مولکولی
    Zahar Avakh, Muhammad Shadman Lakmehsari *, Bahman Farajmand, MohammadAli Rezvani

    The presence of sulfur compounds and mercaptans in oil cuts causes environmental contamination and leads to corrosion in transmission lines and storage tanks. Therefore, it is necessary to reduce the amount of sulfur and mercaptans in oil cuts to international standards. Metal- organic frameworks are a class of nano-porous adsorbents that have been identified for storing and separating gases and utilizing energy and environmental regeneration. This paper using experiments and molecular simulations, attempts to investigate the removal of sulfur compounds from gasoline. In experimental desulfurization tests thiophene and benzothiophene, which are aromatic sulfur compounds in gasoline were used as a model. The desulfurization process was selected by some metal-organic frameworks with 0.05g of mass for 8 hrs at 308K. In the molecular simulation part, a model was defined for gasoline that included a binary mixture of normal-hexane/benzothiophene, normal-hexane/thiophene, and normal-hexane/ethanethiol. The amount of adsorption and selection of sulfur compounds in metal-organic frameworks was investigated. The best separation in the mixture of normal-hexane and sulfur compounds was related to a molar fraction of 0.01 at 318K, which was equal to 12602.92 for benzothiophene and normal-hexane mixtures, for the mixture of thiophene and normal-hexane is 628.49, and obtained for the mixture of ethanethiol and normal hexane at 50.699. The results of adsorption and adsorption diagrams of sulfur compounds on metal-organic frames-in both experimental and simulation sections showed that MIL-47(V) had the highest selectivity and adsorption for sulfur compounds. In both experimental and molecular simulations, it was found that metal-organic frameworks could be a good detergent for sulfur compounds to obtain clean fuel.

    Keywords: Oil cuts, Metal-Organic Frameworks, Selectivity, Desulfurization, Physical Adsorption, Molecular Simulation
  • Nastaran Parsafard *, MohammadHassan Peyrovi, Mahdi Abdali Hajiabadi

    A co-impregnation method was applied to the Ni/Zr-HMS/HZSM-5 catalyst (with various amounts of zirconium) during the hydrogenation of benzene. The physicochemical properties of the prepared nickel catalyst were characterized using X - ray diffraction, X - ray fluorescence, Fourier transform infrared spectroscopy, ultraviolet-visible diffuse reflectance spectroscopy, temperature-programmed desorption of ammonia, H2 chemisorption, N2 adsorption - desorption, and thermogravimetric analysis. The catalytic performance was assessed on a fixed-bed reactor (reaction temperature between 130 °C and 190 °C). The results indicated that the nickel catalyst with Si/Zr = 35 exhibited better catalytic performance and stability than others, so providing a better selectivity in long-term performance.

    Keywords: Impregnation, Hydrogenation, Conversion, Selectivity, Stability
  • AbdolHossein Dabbagh, Marzie Naderi, Mehdi Zamani *

    The influence of NaNO2, HNO3 and H2SO4 on the structure and morphology of gamma-alumina was investigated by XRD, BET, SEM and FT-IR spectroscopy. Selected amounts of NaNO2, HNO3 and H2SO4 were added to a solution of aluminum isopropoxide (as a precursor for the boehmite synthesis). The boehmite samples were calcined at 350 and 600 ℃ to form the semi-crystalline high surface area gamma-Al2O3. The reactivity and selectivity of the modified gamma-alumina catalysts were examined using dehydration reaction of 2-octanol. There was a good correlation between reactivity, selectivity and the amounts (and type) of the modification. The dominant product was cis-2-octene for all of the catalysts. Low conversion and high selectivity were obtained for dehydration of 2-octanol over alumina modified with NaNO2. High conversion, low selectivity and excessive isomerization were found for gamma-alumina catalyst modified with H2SO4.

    Keywords: Alumina, Dehydration, Alcohol, reactivity, Selectivity
  • Nastaran Parsafard *, Mohammad Hasan Peyrovi, Mahdi Abdali

    Ni catalysts supported on Nano porous catalysts were prepared by the impregnation method and tested for vapor phase hydrogenation of benzene. The textural and physico-chemical properties of Ni catalysts were characterized by the X-ray diffraction, Fourier-transform infrared spectroscopy, scanning electron microscope and N2 adsorption-desorption analysis. The catalytic evaluation revealed that the best selectivity to benzene (> 84%) and high stability with the low coke deposition (< 1.1%) are related to Ni/Folded Sheets Mesoporous Materials-No. 16. The kinetics of benzene hydrogenation has been examined as a function of benzene and hydrogen pressures at various temperatures. Two kinetic models based on power law and Langmuir-Hinshelwood mechanisms were developed for the reaction and compared with the obtained experimental data. The apparent kinetic parameters were estimated using the multiple regression analysis. Both these models present the good results.

    Keywords: Hydrogenation, Nano porous catalysts, Activity, Stability, Selectivity, Coke deposition
  • Nastaran Parsafard *, Mohammad Hassan Peyrovi, Mehdi Abdali Hajiabadi

    Ni/Al-HMS/HZSM-5 catalysts with varying amounts of Si/Al ratios were prepared via the impregnation method and evaluated for the hydrogenation of benzene at 130−190 °C. To study the catalyst characterization, various methods were used as X-ray diffraction, X-ray fluorescence, Fourier transform infrared spectroscopy, ultraviolet-visible diffuse reflectance spectroscopy, temperature-programmed desorption of ammonia, H2 chemisorption, N2 adsorption-desorption, and thermogravimetric analysis. The effect of reaction temperature and residence time on catalytic performance was considered and kinetic of this reaction was investigated under different pressures. The results demonstrated that the composite catalysts have high benzene conversion (~80%), medium to low toluene and xylene conversion (16–80%), moderate benzene selectivity (~50%) in the mild reaction condition, and good catalytic stability against the coke deposition.

    Keywords: Hydrogenation of benzene, Composite catalyst, Kinetic, Selectivity, Stability
  • Abbas Shahsavani, Zohreh Ahadi, Vahid Sokhanvaran, Maryam Taghizadeh, Mostafa Hadei, Muhammad Shadman Lakmehsari *

    This study aimed to investigate the adsorption of CH4, CO2, H2S at a temperature of 298.15 K and pressurerange of 0.1 to 30 atm, and compare the results with experimental data for MIL-47 using GCMC. Themaximum CH4, CO2 and H2S adsorptions were 3.6, 10.45, and 12.57 mol.kg-1, respectively. In addition, theselectivity for binary mixtures of CH4/CO2 and CH4/H2S was calculated. The results for CH4/CO2 mixturesat 10 atm showed that: 1) MIL-47 only adsorbed CO2 in a 0.05 CH4/ 0.95 CO2 mixture, and 2) by increasingthe mole fraction of CH4, the selectivity toward CO2 decreased. The results for H2S/CH4 mixture at 10atm showed that: 1) H2S was adsorbed only in mole fractions of 0.95, 0.75, and 0.50 of H2S, and 2)the observed selectivity was about 132.7 and 63.2 at H2S mole fractions of 0.25 and 0.05, respectively.The MD simulations and RDF analyses were used to investigate 0.5 CH4/0.5 CO2 and 0.75 CH4/0.25 H2Smixtures. The results showed that the adsorption mostly occurs on the metallic part of MIL-47. Wefound that V and O atoms were the active adsorption sites in MIL-47. H2S and CH4 showed to have thehighest and lowest levels of self-diffusions, respectively. The MD simulations were used to study the selfdiffusionfor mixtures across all mole fractions. In the binary mixture of 0.95 CO2/0.05 CH4, the maximumself-diffusion was 1.49×10-12 m2s-1 for CO2. The maximum self-diffusion for H2S in the mixture of 0.05CH4/0.95 H2S was 2.62×10-10 m2s-1.

    Keywords: Adsorption, CO2, H2S, MIL-47, Selectivity
  • Muhammad Nurdin*, Nasriadi Dali, Irwan Irwan, Maulidiyah Maulidiyah, Zul Arham, Ruslan Ruslan, Baharuddin Hamzah, Sarjuna Sarjuna, Dwiprayogo Wibowo
    Pb2+ ion was investigated by voltammetry selectivity using TiO2-Ionophores hexa(p-tert butyl)hexa(ethyl ester)calix[6]arene (BEK6) composite to increase the selectivity and sensitivity of carbon paste electrode (CPE). The BEK6 was synthesized by using hydrolysis method, meanwhile the TiO2-P25 and graphite powder were mixed as an electrode composite. The Scanning Electron Microscopy (SEM) shows that the CPE doped TiO2-BEK6 (CPE/TiO2-BEK6) have morphology likes a rough, non-porous, composed of fine particles, and homogeneously. The presence of Pb2+ ion in pH 5 citrate buffer electrolyte causes the peaks appearance on Epa and Epc were 0.17 V and 0.37 V with  the peak potential current generated of 15.15 μA and -12.0 μA, respectively. The 0.005 g BEK6 was increased significantly the peak current of the Pb2+ ion with the LOD value of 0.1756. In addition, the presence of TiO2-BEK6 composite shows the measurement current stability by %RSD of 0.83.
    Keywords: Pb2+, Ionophore, TiO2-BEK6, Cyclic voltammetry, Selectivity
  • Nastaran Parsafard *, Mohammad Hasan Peyrovi, Mehrdad Valipour Shokoohi
    The total oxidation of toluene at a wide temperature range (200–500 oC) over micro/mesoporous platinated catalysts has been investigated about activity, selectivity to CO2 and CO, catalyst's stability versus coke deposition and reaction kinetics. Kinetic of toluene oxidation was measured under various oxygen and toluene pressures and also the effect of the reaction conditions on the catalytic performance was studied. For more study, two kinetic models have also been selected and tested to describe the kinetics for this reaction. The results show that the Langmuir-Hinshelwood model provides a good fit for the experimental data. The obtained results showed that Pt/HZSM-5(30)-HMS have a better ability than other catalysts for the oxidation reaction of toluene, such as maximum toluene conversion (>97%), high selectivity to CO2 (100%), good catalytic stability against coke deposition and appropriate kinetic parameters
    Keywords: Toluene oxidation, Kinetics, Conversion, Selectivity, stability, Langmuir-Hinshelwood model
  • Gyanendra Singh, * Kalash Chandra Yadav
    A new acetate selective poly (vinyl chloride) membrane sensor based on newly synthesized nickel complex of Schiff base, N,N'-benzene-1,2-diylbis[1-(1H-pyrrol-2- yl)ethanimine] as an ionophore was prepared. The electrode show Nernstian slope of 31.4±1 mV/decade with improved linear range of 1.6×10-7 to 1.0×10-2 M, with a lower detection limit of 1.0×10-7 M between pH range of 3.0-9.5, giving a relatively fast response within (5s) and can be used for at least 2 months without any divergence in potential. The selectivity coefficient was calculated using matched potential method. The proposed electrode was successfully applied as an indicator electrode for the titration of arsenate ion with sodium thiocynide. It was also be used for the determination of arsenate ion in different water samples.
    Keywords: Ion, selective electrode, Selectivity, Nickel, Schiff base, Acetate
  • Reza Mehrani, Ahmad Tavasoli *, Mohammad Barati, Ali Karimi, Masoumeh Ghalbi Ahangari
    Bagasse as a real biomass was converted to hydrogen rich gas via catalytic supercritical water gasification process. To find the effect of Cu on selectivity of products, Cu promoted Ni-γAl2O3 catalysts were prepared with 1 to 20wt% Ni and 0.5 to 10wt% Cu loadings via impregnation method. Catalysts were characterized by ICP, BET, XRD, H2 chemisorption and TEM technique as well CHNS analysis was carried out for elemental analysis of bagasse. The biomass supercritical water gasification process was performed in a batch micro-reactor at 400oC and 240 bars. The total gas yield increased with increasing in Ni and Cu loadings up to 15wt% Ni and 7.5 wt% Cu and became approximately constant. The catalytic process increased hydrogen yield to 9.5, CO yield to 2.2 and light hydrocarbons to 0.59 mmol/g bagasse. Total H2 selectivity (THS) ratio increased with increasing in Ni and Cu loading reached a maximum at 15%wt Ni and 7.5%wt Cu and then began to decrease.
    Keywords: Supercritical water gasification, Bagasse, Hydrogen, Selectivity, Nickel, Cupper
  • Dharampal Singh Tyagi, Aishwarya Singh
    1,1’-[benzene-1,4-diyldimethylylidene]bis(3-phenylurea)) was synthesized and tested for the fabrication of aluminum selective membrane electrode. The membrane electrode with dimethyl phthalate (DMP) as plasticizer works satisfactorily in the linear concentration range of 1.3×10-6 to 1.0×10-1 M with best optimized composition of DMP: PVC: ionophore: NaTPB of 60:35:3:2 (%, w/w). The membrane electrode has a fast response time (5 s) and wide pH range (2.5–8.5). The selectivity coefficients were calculated with fixed interference method. The membrane sensor was also used as an indicator electrode for the titration of Al(III) with EDTA and Na3PO4.
    Keywords: Aluminum, Ion, selective electrode, Ionophore, Selectivity
  • Tavasolia., Karimis., Nikookarh., Fadakar, H
    An extensive study of Higher Alcohols Synthesis (HAS) from syngas using alkalized MoS2 catalysts supported on Carbon Nanotubes (CNTs) is reported. Up to 30wt.% of Mo and 8wt.% K are added to the CNTs by impregnation method. The catalysts were characterized by different methods and the performance of the catalysts was assessed in a micro-reactor. TEM images showed that most of the metal particles were homogeneously distributed inside the tubes and the rest on the outer surface of the CNTs, with particle sizes in the range of 3 to 16 nm. Temperature Programmed Reduction (TPR) tests showed that increasing the amount of Mo decreased the first TPR peak from 518 to 503oC and increased the second TPR peak temperature from 782 to 825oC. The diffraction peaks representing the characteristic K-Mo-O phase (these species can enhance formation of higher alcohols) were observed in the XRD of catalysts. The catalyst with 20 wt.% Mo and 8 wt.% K showed the highest conversion. The total alcohol selectivity reached a maximum of 45.3 wt.% on the catalyst with 15 wt.% Mo. The catalyst with 15 wt.% Mo exhibited selectivity of 35.3 wt.% towards higher alcohols.
    Keywords: Higher Alcohols Synthesis (HAS), Molybdenum, Loading, Carbon nanotubes, Physicochemical properties, Activity, Selectivity
  • Tavasolia., Karimis., Zolfaghariz., Taghavis., Amirfirouzkouhih., Babatabar, M
    An extensive study of Higher Alcohol Synthesis (HAS) from synthesis gas using cobalt (Co) promoted alkalized MoS2 catalysts supported on Carbon NanoTubes (CNTs) is reported. Up to 5wt.% of Co is added to the 15wt.% Mo-8wt.%K/ CNTs by incipient wetness impregnation method. Most of the metal particles were homogeneously distributed inside the tubes and the rest on the outer surface of the CNTs. The catalysts are extensively characterized by different methods and the activity and selectivity of the catalysts were assessed in a fixed bed micro-reactor. Temperature Programmed Reduction (TPR) tests showed that addition of cobalt decreased the second TPR peak temperature from 801 to 660oC. The diffraction peaks that represent the characteristic K-Mo-O phase (i.e. K2Mo2O7, K2MoO4, K2Mo7O20, KMo4O6, and K0.33MoO3; these species can enhances formation of higher alcohols) were observed in the X- Ray Diffraction (XRD) patterns of unpromoted Mo-K/CNTs and to a greater extent in the XRD patterns of Co-promoted Mo-K/CNTs catalysts. Co addition to Mo-K/CNTs not only increased the number of surface sites, but also decreased the average active metal particle sizes from 7.53 to 5.33 nm and increased the percentage dispersion from 51.1 to 68.2%. Among the catalysts with different Co loadings, catalyst with 5 wt.% Co showed the highest %CO conversion of 38.8%. The total alcohol selectivity reached a maximum of 59.7 wt.% on the catalyst promoted with 3 wt.% cobalt. The catalyst with 3 wt.% Co exhibited selectivity of 41.65 wt.% towards higher alcohols.
    Keywords: Higher alcohols synthesis, Molybdenum, Cobalt, Carbon nanotubes, Physicochemical properties, Activity, Selectivity
  • اسماعیل زنجیری، مصطفی فضلی*، سید رضا سیف محدثی، محمد تیموری، معصومه آقابابایی
    با توجه به لزوم مصرف بنزین با استاندارد یورو 5 و اهمیت محصولات ایزو پارافینی نسبت به آروماتیکی در آن، استفاده از کاتالیست مناسب در فرآیند تبدیل کاتالیستی از اهمیت ویژه ای برخوردار است. با اضافه نمودن فلز قلع به کاتالیست های دو فلزی رایج در این فرآیند ((Pt-Re /γ-Al 2O3 می توان مرحله پیش گوگرد زنی کاتالیست را که در آن احتمال مسمومیت کاتالیست وجود دارد حذف کرده و ضمنا با افزایش جمعیت نسبی سایت های اسیدی متوسط، میزان ایزوپارافین ها را در محصول افزایش داد. در این پروژه، کاتالیست سه فلزی Pt-Re-Sn/γ-Al 2O3 با استفاده از روش تلقیح مرطوب تهیه و تحت شرایط عملیاتی مطابق با پالایشگاه های ایران، در رآکتور دیفرانسیلی واحد پایلوت پژوهشکده کاتالیست و نانو فناوری پژوهشگاه صنعت نفت مورد آزمایش تعیین فعالیت با خوراک صنعتی (HSRG) قرار گرفت. مقدار فلزات پلاتین و رنیوم موجود در کاتالیست های تهیه شده ثابت بوده و به ترتیب برابر با 22/0 و 44/0 درصد وزنی و مقدار فلز قلع از 06/0 تا 3/0 درصد وزنی می باشد. پس از آنالیز محصول مایع خروجی از رآکتور، گزینش پذیری واکنش تولید ایزوپارافین نسبت به واکنش تولید آروماتیک برای این کاتالیست ها مقایسه شد. نتایج نشان می دهد گزینش پذیری تولید ایزو پارافین ها نسبت به تولید آروماتیک ها در دمای 490 درجه سانتی گراد برای بهترین کاتالیست ساخته شده (3/0 درصد وزنی قلع) و کاتالیست تجاری به ترتیب 5/39 و 7/29 درصد و در دمای 510 درجه سانتی گراد به ترتیب 4/4 و 2/13درصد می باشد. بنابراین کاتالیست با 3/0 درصد وزنی قلع در دمای 490 درجه سانتی گراد در مقایسه با کاتالیست تجاری و سایر کاتالیست های ساخته شده از نظر گزینش پذیری نسبت به ایزوپارفین ها دارای عملکرد بهتری می باشد.
    کلید واژگان: کاتالیست سه فلزی, تبدیل کاتالیستی, گزینش پذیری, ایزو پارافین, آروماتیک
    Esmaeel Zanjiri, Mostafa Fazli *, Reza Seif Mohaddecy, Mohammad Tyimouri, Masoume Aghababaei
    Gasoline with euro 5 standard and improvement of selectivity of isomer products to aaromatic products in gasoline is very important in oil refinery. In this paper، Pt-Re-Sn Al2O3 catalyst prepared with imperegnation procedur. Then، The activity and catalytic reactor tests for prepared catalysts and commercial catalyst with same of commercial catalytic reforming process conditions and industrial feed in differential plug flow reactor of catalysis and nano technology division، research institute of petroleum industry pilot plant were done. The composition of Pt and Re in catalyst prepared was 0. 22 and 0. 44 and range of Sn composition was 0. 06،0. 1، 0. 2 and 0. 3 weight percent. After activity test and analysis of products، selectivity of isoparaffins products to aromatics products was compared. The results show that the selectivity of isoparaffin to aromatic products at two different temperatures (490-510 °C) for prepared catalyst with 0. 3 weight percent of tin and commercial catalyst were 39. 5، 29. 7، 4. 4 and 13. 2، Respectively. Finally، comparison of selectivity of four prepared catalysts and commercial catalyst in two operation conditions show that prepared catalyst with 0. 3 weight percent of tin at 490°C is suitable for new catalytic reforming process.
    Keywords: Triple catalyst, Catalytic Reforming, Selectivity, Isoparaffin, Aromatic
  • محمد فیروزی، مرتضی بقالها، موسی اسدی
    چکیده: در این پژوهش، کاتالیست زئولیتی ZSM-5 با نسبت بالای سیلیسیوم به آلومینیم برابر 800 برای فرایند تبدیل متانول به پروپیلن (MTP) سنتز شده است. در سنتز این کاتالیست از قالب آلی تترا پروپیل آمونیوم برمید استفاده شده است که نسبت به تترا پروپیل آمونیوم هیدروکسید که به طور معمول به عنوان قالب آلی استفاده می شود، به مراتب ارزان تر است. آزمون راکتوری کاتالیست سنتز شده در شرایط عملیاتی دما 460 درجه سانتیگراد، فشار اتمسفری، WHSV برابر 1-h 1 و خوراک شامل محلول 50 درصد وزنی آب و متانول انجام شده است.
    نتیجه های به دست آمده از آزمون راکتوری کاتالیست سنتز شده با نتیجه های آزمون راکتوری یک کاتالیست تجاری در شرایط یکسان مقایسه شده است. برای تعیین ویژگی های کاتالیست از تجزیه های XRD، SEM، TPD، BET و ICP استفاده شده است. نتیجه ها بیانگر آن است که بالاترین میزان گزینش پذیری کاتالیست سنتز شده نسبت به اولفین های سبک به ویژه پروپیلن 54 درصد می باشد که این عدد برای کاتالیست تجاری 40 درصد است. همچنین پس از گذشت 150 ساعت از عمر کاتالیست، کاتالیست سنتز شده دارای درصد تبدیل بالاتری نسبت به کاتالیست تجاری می باشد که به ترتیب 7/99 و 5/99 می باشد.
    کلید واژگان: پروپیلن, هیدروترمال, گزینش پذیری, ZSM, 5, MTP
    Mohammad Firoozi, Morteza Baghalha, Mousa Asadi
    In this research, ZSM-5 zeolite with high ratio of Si to Al of 800 was synthesized to act as the catalyst for the conversion of Methanol To Propylene (MTP). Instead of tetra-propyl ammonium hydroxide, here, tetra-propyl ammonium bromide which is much cheaper was used as the template. The reaction was investigated in a fixed-bed flow reactor under the operating conditions of T=460 °C, P=1atm, and WHSV = 1 h-1. The obtained results with the synthesized catalysts were compared with those of a commercial catalyst. The catalysts were characterized using XRD, SEM, TPD, BET and ICP techniques. The obtained results indicated that the selectivity of methanol conversion to light olefins, including propylene is 54%. This value is significantly higher than the 40% selectivity obtained with the commercial catalyst. Aging and deactivation after 150 hours of reactor operation was less severe for the synthesized catalyst compared to the commercial catalyst.
    Keywords: Propylene, Hydrothermal, Selectivity, ZSM, 5, MTP
  • Arpit Singh, Sanjay Singh*, Gyanendra Singh
    The three chelates 1,5-bis(o-aminobenzoate)-3-thiapentane (L1), 1,5-bi (omethoxybenzoate)- 3-thiapentane (L2), 1,5-bis(o-chlorobenzoate)-3-thiapentane (L3) have been synthesized and explored as a neutral ionophores for preparing poly(vinyl chloride) based membrane sensors selective to Er3+. The addition of sodiumtetraphenylborate and various plasticizers, viz., o-NPOE, TBP, DBBP, TEP and DOS has been found to substantially improve the performance of the sensor. The best performance was obtained with the sensor no.6 having membrane of ionophore (L2) with composition PVC: o-NPOE: ionophore (L2): NaTPB (%w/w) of 35:56:2:7. This sensor exhibits Nernstian response with slope 22.1±0.3 mV decade-1 of activity in concentration range 3.0×10-9 to 1.0×10-2 M Er3+, performs satisfactorily over wide pH range (1.5-6.7), with a fast response time (8 s). The sensor was also found to work satisfactorily in partially non-aqueous media up to 20% content of methanol, ethanol or acetone and could be used for a period of 5 months without any change in response characteristics. The Er3+ selective sensor was used as an indicator electrode for the titration of 25 ml 1×10-3 M EDTA solution and for the determination of Er3+ ion in different synthetic samples. The proposed electrode no. 6 was also used for the determination of fluoride ion in two mouth wash sample.
    Keywords: Sensor, Potentiometry, Ionophore, Erbium, Selectivity
  • Sulekh Chandra*, Deepshikha, Anjana Sarkar
    Novel polymeric membrane electrode based on o-hydroxyacetophenone carbohydrazone (OHAC) as a neutral ionophore carrier has been prepared and explored as silver(I) ion selective electrode. The addition of lipophilic anion excluder (NaTBP) and various plasticizers viz. o-nitrophenyl octyl ether (o-NPOE), dibutyl phthalate (DBP) and butyl acetate (BA) have found to improve the performance of membrane sensor which have a composition of I:NaTBP:NPOE:PVC in the ratio 3:2:62:33 (w/w; mg). The electrode exhibit Nernstian slope for silver (I) ions over wide concentration ranges from 1.0×10-7 M to 1.0×10-2 M with limits of detection 1.6×10-7 M. The response time was found to be 10 s. The potentiometric responses were independent of the pH of the test solutions in the pH range of 3.0 to 8.0. The proposed electrode revealed good selectivity over a wide variety of other cations including alkali, alkaline earth, transition and heavy metal ions. The proposed PVC electrode was used as an indicator electrode in the potentiometric titration of Ag+ ions with KI and NaCl solutions and in direct determination in different water samples and urine sample of peoples working as jewelry maker.
    Keywords: Polymeric membrane, Carbohydrazone, Silver Selective Electrode, Detection Limit, Selectivity
  • Rajesh Narayanrao Singru*
    Copolymer resin (8-HQ5-SAOF-IV) synthesized by the condensation of 8-hydroxyquinoline5-sulphonic acid and oxamide with formaldehyde in the presence of acid catalyst, was proved to be selective chelating ion-exchange copolymer for certain metals. The chelating ion-exchange properties of this copolymer were studied for Fe (III), Cu (II), Ni (II), Co (II), Zn (II), Cd (II) and Pb (II) ions in the form of their metal nitrate solutions. A batch equilibrium method was employed in the study of the selectivity of metal ion uptake involved in the measurements of the distribution of a given metal ion between the copolymer sample and a solution containing the metal ion. The study was carried out over a wide pH range, shaking time and in media of various ionic strengths of different electrolytes. The copolymer showed a higher selectivity for Fe (III), Cu (II), and Ni (II) ions than for Co (II), Zn (II), Cd (II) and Pb (II) ions. Distribution ratios (D) of metal ions were found to be increased by increasing pH of the solutions; hence the resin can be used to recover certain metal ions from waste solutions and used for the purpose of purification of waste water and removal of iron from boiler water. The ion-exchange capacity of metal ions has also been determined experimentally and compare with other commercial resins. The morphology of the copolymer was studied by scanning electron microscopy (SEM); showing amorphous nature of the resin therefore can be used as a selective ion-exchanger for certain metal ions.
    Keywords: Adsorption, Degree of Polymerization (DP), Ion Exchangers, Metal, polymer Complexes, Resins, Selectivity
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