Interaction of propylene with a V2O5/Al2O3 catalyst

IR-spectroscopic studies indicate that on the oxidized surface of V₂O₅/Al₂O₃ catalysts propylene interacts mainly with Brönsted acid centers to form an alcoholate type complex transforming into acetone. On the reduced surface propylene is stabilized as a -complex of V³⁺ and V⁴⁺ ions.

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- , V₂O₅/Al₂O₃ , . - V³⁺ V⁴⁺.

     

Active site for hydrogenation on reduced V2O5/Al2O3 catalyst

Active sites for C₂H₄ hydrogenation produced by reduction of V₂O₅/Al₂O₃ catalyst pretreated at 450°C were found to be composed of both strong Lewis acid sites associated with V⁴⁺ and basic sites of Al₂O₃. C₂H₄ polymerization concurrent with hydrogenation was assumed to occur on Lewis acid sites with higher acid strengths than those of the hydrogenation sites.

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C₂H₄, V₂O₅/Al₂O₃, 450°C, , Al₂O₃. , , , C₂H₄.

     

IR study of ammonia adsorption on Lewis acidic sites on a V2O5/Al2O3 catalyst

Reduction of V₂O₅/Al₂O₃ catalyst has been shown to affect the adsorption of ammonia on Lewis acid sites. The band of NH₃ (ad) at 1243 cm^–3 is sensitive to oxygen under mild conditions. An adsorbed species with IR absorption at 1300 cm^–1 is likely to undergo dissociation to form NH₂.

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V₂O₅/Al₂O₃ . NH₃ () 1243 ^–1 . 1300 ^–1 , NH₂.

     

Kinetics of C2H4 polymerization on reduced V2O5/Al2O3 catalyst

Kinetic study of C₂H₄ polymerization on reduced V₂O₅/Al₂O₃ catalysts revealed that the rate equation can be expressed as V=k exp (-Y) K_aP_E/(1+K_aP_E) in the temperature range of –20 to 70°C. The deactivation constant, , was found to have a close relation with the yield and molecular weight of the polymer. C₂H₄ V₂O₅/Al₂O₃ –20 +70°C : V_p=k·exp(-Y_p)·K_aP_e/(1+K_aP_e). .     

Formation of aromatic carbonium ions on V2O5/Al2O3

A comparison of IR spectra of individual toluene, mesitylene, hexamethylbenzene, triene and their carbonium ions with IR spectra of the same molecules adsorbed on V₂O₅/Al₂O₃ has indicated the formation of carbonium ions on catalyst surface.

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- , , , , - , V₂O₅/Al₂O₃ Al₂O₃, t, V₂O₅/Al₂O₃ .

     

Effect of vanadium content on the character of acidic sites on V2O5/Al2O3 catalysts

By IR spectroscopy and TPD the effect of vanadium content on the relative proportion of strongly acidic sites of V₂O₅/Al₂O₃ catalyst was studied.

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- - V₂O₅/Al₂O₃.

     

IR-spectroscopic studies of strength and concentration of acid centers on V2O5/Al2O3 catalysts

The strength of protonic sites and the concentration of acid centers in V₂O₅/Al₂O₃ catalysts have been estimated according to pyridine and ammonium adsorption.

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V₂O₅/Al₂O₃.

     

Phase composition of a selective V2O5?Fe2O3 catalyst of methanol oxidation to formaldehyde

Redispersion of Re/SiO₂ catalysts during air-aging at ambient temperature has been confirmed by TEM analysis. The splitting of large primary crystallites (>10 nm) under the influence of the strain energy of the oxide layer formed on the Re surface has been proposed to explain the observed phenomenon.

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Re/SiO₂ . , Re(>10 nm), , .

     

SiO2改性的V2O5-MoO3/ TiO2催化剂抗碱中毒性能研究

以陶瓷为骨架,用溶胶凝胶法和浸渍法制备了V₂O₅-MoO₃/ TiO₂催化剂,并用SiO₂进行改性。采用浸渍法模拟碱K中毒,研究了SiO₂改性前后催化剂中毒脱硝效率的变化,并通过BET、H₂-TPR、NH₃-TPD等技术手段对催化剂进行了表征。结果表明,加入SiO₂后,催化剂的比表面积明显提高。SiO₂改性后新鲜催化剂还原温度向低温方向迁移10 ℃左右,氧化还原能力得到了提高,其表面酸强度和酸量也得到较大的提高。反应评价结果表明,SiO₂改性可以提高催化剂抗碱中毒的性能。     

Hydrogen effects on the electric conductivity of a Pt/Al2O3 catalyst

Hydrogen desorption, hydrogen spillover and reduction processes have been evidenced using a new experimental strategy based on AC electric conductivity measurements during TPD and TPR experiments on a 0.5% Pt/Al₂O₃ catalyst.     

TPR studies on steam reforming of 2-propanol on Rh/Al2O3, Ru/Al2O3 and Pd/Al2O3

Reaction pathways for steam reforming of 2-propanol (isopropyl alcohol, IPA) on Rh/Al₂O₃, Ru/Al₂O₃ and Pd/Al₂O₃ have been studied by temperature-programmed reactions (TPRs) of IPA and acetone in the presence of steam. The results of TPRs suggest that that of IPA on Rh/Al₂O₃ and Ru/Al₂O₃ proceeds via acetone, while the steam reforming of IPA on Pd/Al₂O₃ takes place via propene from acetone. This revised version was published online in August 2006 with corrections to the Cover Date.     

Isomerization and secondary metathesis of 2-butenes over a MoO3/Al2O3 catalyst

Transformation of cis- and trans-2-butene at 40°C was investigated over a MoO₃/A₂O₃ catalyst reduced with hydrogen and subjected to different pretreatments. Isomerization is accelerated by hydrogen preadsorbed either at low or high temperatures. The cometathesis of 2-butenes with the 1-butene intermediate, however, is enhanced only by hydrogen preadsorbed at low and suppressed by hydrogen adsorbed at high temperatures.

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- -2- 40°C MoO₃/Al₂O₃, . , , . 2- 1- , ; , .

     

Sulfurization of Pt/Al2O3?Cl catalysts. IV. Adsorption sites of H2S on Al2O3, Al2O3?Cl and Pt/Al2O3?Cl

Chemisorption of H₂S on Al₂O₃, Al₂O₃–Cl and Pt/Al₂O₃–Cl has been studied by gravimetry and IR spectroscopy. The influence of the amount of Cl on the H₂S adsorption equilibrium value and the nature of the adsorption sites at low and high coverages are discussed.

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H₂S Al₂O₃, Al₂O₃–Cl Pt/Al₂O₃–Cl . Cl H₂S, .

     

Die Bestimmung V2O2 und V4O5 nebeneinander in Kontaktkatalysatoren auf Kieselgurgrundlage

Ohne Zusammenfassung     

Effect of the extent of reduction of V2O5 on the adsorption of propylene and the oxidative dehydrogenation of propane to give propylene on V2O5 and V2O5/TiO2-SiO2

An increase in the propylene output in the oxidative dehydration of propane on V₂O₅/TiO₂-SiO₂ was observed after prior reduction of V₂O₅ in the reaction mixture to V₂O₄, which reduces the destructive chemisorption of propylene. A low titanium dioxide content in TiO₂-SiO₂ hinders the deep reduction of V₂O₅ to V₂O₃, which reduces the conversion of propane. __________ Translated from Teoreticheskaya i éksperimental’naya Khimiya, Vol. 43, No. 6, pp. 373–378, November–December, 2007.     

Products of V2O5?MoO3 catalyst reduction with benzene in the absence of oxygen

In the products of V₂O₅–MoO₃ catalyst reduction with benzene in the absence of oxygen, carbon monoxide and carbon dioxide were detected in all the reduction region of the catalyst. Maleic anhydride is formed at the beginning of the reduction (first several pulses), and p-benzoquinone was detected in some experiments at the very beginning (in the first few pulses). The remaining products, which were detected in catalytic oxidation of benzene, such as phenol, hydroquinone, biphenyl and acrylic acid, were absent in all the reduction region.

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V₂O₅–MoO₃ - . ( ) , , - , -. , , , , , .

     

Kinetics of SO2 oxidation on K2S2O7?V2O5 catalyst in non-steady conditions

Studies of SO₂ oxidation on a molten component of vanadium catalysts in non-steadystate conditions indicates that the kinetics agree fairly well with an oxidation-reduction mechanism. In the low temperature range (<790 K) tetravalent vanadium can be partially crystallized.

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. , - . ( 790 ) .

     

Role of the V=O double bond in the selective oxidation of benzene on V2O5 and V2O5?MoO3 catalysts

Infrared spectra of both fresh and reductively activated V₂O₅ and V₂O₅–MoO₃ catalysts were recorded and compared with the results of catalytic measurements. The results indicate that the presence of V=O double bonds in the catalytically active mass is not essential for the selective oxidation of benzene to maleic anhydride.

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, V₂O₅ V₂O₅–MoO₃. . , V=O .

     

Sorption of palladium chloride complexes on Al2O3 surface

Three types of sorption interactions with the corresponding Pd aquachlorocomplexes [Pd(H₂O)₂Cl₂]⁰, [Pd(H₂O)Cl₃]^– and [PdCl₄]^2– have been discovered on -Al₂O₃ at surface concentrations for the active component and the competing HCl ranging within 0.05–1.25 and 1.2–4.8 mol m^–2, respectively.

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0,05–1,25 /² 1,2 4,8 /² -Al₂O₃ , : [Pd(H₂O)₂Cl₂]⁰, [Pd(H₂O)Cl₃]^– [PdCl₄]^2–.

     

Ni-Mo/Al_2O_3催化剂上硫转移反应的研究

制备了以γ-Al2O3为载体的Ni-Mo催化剂,并用于FCC汽油的加氢硫转移反应。对Ni-Mo/Al2O3催化剂上的硫转移反应机理进行了研究,考察了不同反应条件对硫转移反应的影响。实验结果表明,硫醇与烯烃的反应在催化剂表面的加氢活性位上进行,小分子的硫醇发生加氢脱硫,生成吸附态H2S,吸附态的H2S与烯烃反应,生成大分子硫醇和硫醚;另外小分子硫醇还可直接与烯烃发生反应,生成硫醚。提高反应温度、压力、氢油比或降低空速,均可提高催化剂的硫转移反应活性,轻质硫转化率得到明显提高,且单烯选择性还能维持在98%左右。