Activity of bifunctional Pt-Dy/Al2O3 catalysts in hydrocarbon reactions

The conversions ofn-hexane and methylcyclopentane on Pt–Dy/Al₂O₃ containing different amounts of Dy have been investigated in a pulsed microcatalytic reactor. The poisoning effect of thiophene on the activity of Pt–Dy/Al₂O₃ for n-hexane conversion has been studied. The influence of Dy over Pt–Dy/Al₂O₃ is also discussed.     

Lithium promoted Pt?Sn/Al2O3 catalysts for dehydrogenation ofn-decane: Influence of lithium metal precursors

Four lithium metal precursors (LiNO₃, CH₃COOLi, LiOH, LiCl) have been used as promoters in Pt–Sn/Al₂O₃ catalysts to improve activity, selectivity and stability in a modeln-decane dehydrogenation reaction. Acidity, TPR and TPCO measurements have shown that the precursors affect the acid site distribution in the support, modify the reducibility and dispersity of Pt–Sn active species, coke lay-over patterns, stability and also selectivity for formation of monoolefins in the dehydrogenation ofn-decane.     

Enhancement of Pt?Sn/Al2O3 catalyst stability for butane dehydrogenation by modification with Sm and Li

Stabilization methods of Pt–Sn/Al₂O₃ dehydrogenation catalysts by modification with Sm and Li are introduced. Pt crystallite dispersion on the support can be promoted by Sm. Li, especially when corporated with Sm, very effectively inhibits carbonization and prolongs the life of the catalysts.     

Catalytically Promoted NOx Sorption by ZrO2-Based Oxides

Metal promoted zirconia-based oxide sorbents, such as Pt–ZrO₂/Al₂O₃ for NO _x have been investigated. To clarify the role of the catalyst component, sorption of NO and NO₂ was compared using the samples with and without Pt. The catalytic oxidation of NO to NO₂ and successively to nitrate ions is an important role for the Pt catalyst. The experimental results indicate that a high-temperature calcination is essential to remove residual Cl from Pt–ZrO₂–Al₂O₃ prepared from H₂PtCl₆ in order to provide more active NO _x sorption sites. Of M–ZrO₂–Al₂O₃ samples investigated, ruthenium as well as Pt demonstrated relatively good performance as a catalyst component in the sorbent. The FT-IR spectra after sorption of NO and NO₂ demonstrated a strong band attributed to stored nitrate ions. The Pt catalyst was more resistant to sulfur poisoning than a base metal catalyst. However, the NO _x sorptive capacities of the Pt–ZrO₂/Al₂O₃ sorbents were expected to be deteriorated in dilute SO₂ as far as observed from FT-IR spectra.     

A study of the properties of active sites on PtY/Al2O3

The catalytic performance and the properties of active sites on PtY/Al₂O₃ have been studied using a pulse microreactor, TEM and poisoning technique. The study shows that PtY/Al₂O₃ shows higher activity and selectivity for n-hexane conversion and the dehydrogenation of cyclohexane, as compared to Pt/Al₂O₃. The changes in PtY/Al₂O₃ geometric patterns and in both the total numbers of active sites (TNAS) and the active site distribution (ASD) caused by Y are likely to be responsible for the catalytic improvements.     

Effect of tetrabutyltin on the acidity and reducibility of platinum-tin alumina supported sol-gel catalysts

Tin precursor effect in Pt−Sn/Al₂O₃ sol-gel catalysts has been studied. It is shown that catalysts prepared with tetrabutyltin allow a better reduction of platinum than catalysts prepared with tin tetrachloride and with tin tetra-tert-amyloxide. The solids prepared with tetrabutyltin are catalysts showing a high activity in isopropanol decomposition and cyclohexane dehydrogenation.     

The support and characterization of C60 and MoO3 on Al2O3

A new type of catalyst from supporting C₆₀ on MoO₃ and Al₂O₃ has been prepared. The effect of different order of impregnation and calcination atmosphere on catalyst are investigated by the solution test in toluene, UV-VIS spectroscopy and temperature programmed reduction (TPR). The results show that when the catalyst was prepared by supporting MoO₃ on C₆₀/Al₂O₃ and calcined in N₂, there is a stronger interaction between C₆₀, MoO₃ and Al₂O₃, but when supporting C₆₀ on MoO₃/Al₂O₃, the interaction is relatively weak. We consider that in the former method a new complex, Mo–C₆₀–O–Al, is formed.     

Dehydrogenative activity of catalysts with low palladium content

Catalysts containing as little as 0.5 mass. % Pd are highly active in the dehydrogenation of cyclohexane when Sibunite® or active alumina (for gas dehumidification) are used as catalyst supports. Dehydrogenative activity of the Pd/Al₂O₃ catalyst is further increased upon surface sulfidation and addition of 0.25–0.5 mass. % Re.Translated fromIzvestiya Akademii Nauk. Seriya Khmicheskaya, No. 2, pp. 422–423, February, 1993.     

Catalytic activity of NiMo/TiO2?Al2O3 systems in thiophene hydrodesulfurization

A correlation exists between the number of surface acid sites and the catalytic activity of NiMo/TiO₂–Al₂O₃ systems in thiophene hydrodesulfurization. The catalytic activity for thiophene hydrodesulfurization and surface concentration of Brönsted acid sites increase with the titania content in the TiO₂–Al₂O₃ support.     

Formation of β- and β″-Al2O3 by the solid state reaction between NaAlO2 and γ-Al2O3

The solid state reaction of NaAlO₂ with γ-Al₂O₃ was investigated kinetically. Powdered compacts with various compositions (Al₂O₃/NaAlO₂ = 1–5) were fired at 700–1200°C for 1–768 hr. The amounts of the reaction product were determined by peak heights of X-ray diffraction patterns. β″-Al₂O₃ was formed predominantly from the sample with Al₂O₃/NaAlO₂ = 2. The firing time for the β″-Al₂O₃ formation was shortened as the firing temperature was raised, and the activation energy, E_a, for formation was about 130–135 kcal/mole. The sample of Al₂O₃/NaAlO₂ = 5 formed m-Al₂O₃ with the mullite structure and was observed to transform gradually to β-Al₂O₃. E_a for the m-Al₂O₃ formation and for the transition were about 55–60 and 40 kcal/mole, respectively, which resulted in E_a of about 95–100 kcal/mole for the β-Al₂O₃ formation. The mechanism of the m-Al₂O₃ formation is discussed briefly.     

锶助剂对铂锡催化剂正丁烷脱氢催化性能的影响

负载型ＰｔＳｎ／Ａｌ２Ｏ３催化剂已广泛地应用于工业生产中［１］，人们正尝试着添加不同助剂以改变催化剂的反应性能。文献的工作主要集中在研究铂锡催化剂中添加助剂对载体表面酸性的调变作用。在烃类重整催化剂中，加入氟、氯等元素可增强载体的表面酸性［２］，提高...     

Pt LIII-edge XANES and EXAFS studies on γ-Al2O3 supported Pt catalysts

Pt L_III-edge XANES and EXAFS were employed to investigate the nature of Pt/γ-Al₂O₃, Pt−Sn/γ-Al₂O₃ and Pt−Fe/γ-Al₂O₃ catalysts. The results indicated that Pt species on these catalysts were all in the oxidized states before reduction, and in the metallic states after reduction. The dispersity of the Pt species on the catalysts was very high after reduction. The electronic properties of the highly dispersed Pt species were different from that of the bulk Pt in large crystallites. An interaction between Pt and the metal-oxide modified γ-Al₂O₃ support is proposed. The interaction improved the dispersity of the Pt species on the catalysts and is thought to be the reason for the enhanced activity and selectivity for dehydrogenation reactions over these catalysts.     

Promoting effect of Mg in supported Mo/HBeta–Al2O3 catalyst for cross-metathesis of ethene and butene-2 to propene

Promoting effects of Mg in heterogeneous Mo/HBeta–Al₂O₃ catalyst have been carefully studied for cross-metathesis of ethene and butene-2 to propene. The catalyst shows good stability with Mg content in the range of 1–2 wt%. Such effect may be attributed to the elimination of weak acid sites through introduction of Mg which suppresses the side olefin oligomerization reaction, as evidenced from NH₃-TPD and ¹H MAS NMR results. Addition of more Mg content to 3 wt% may change the state and reducibility of Mo species, as indicated from the UV–vis, UV-Raman and H₂-TPR measurements. The increasing difficulty for the reduction of Mo(VI) species is closely related with the poor performance of 3 wt% Mg–4Mo/HBeta–30% Al₂O₃ catalyst in the metathesis reaction.     

Selective deposition of Sn on the Pt surface of Pt/ZnAl2O4 catalyst and addition effect on isobutane dehydrogenation

Pt−Sn bimetallic catalysts were prepared by a CVD technique in which Sn was added by passing volatile organometallic compounds over Pt/ZnAl₂O₄ in a H₂ flow. Mixed Pt−Sn sites improve the activity of isobutane dehydrogenation, while Sn on the support improves the selectivity.     

乙烷氧化脱氢用Ni/Al2O3催化剂中活性镍物种前驱体（英文）

Ni/Al2O3 catalysts for oxidative dehydrogenation(ODH) of ethane were prepared by impregnation of Al2O3 with nickel acetate or nickel nitrate,and by mechanical mixing of NiO and Al2O3.The Ni-based catalysts were characterized by N2 adsorption-desorption,X-ray diffraction,diffuse reflectance UV-visible diffuse reflectance spectroscopy,and temperature-programmed reduction of hydrogen.The results showed that formation of crystalline NiO particles with a size of < 8 nm and/or non-stoichiometric NiO species in the Ni/Al2O3 catalysts led to more active species in ODH of ethane under the investigated reaction conditions.In contrast,tetrahedral Ni species present in the catalysts led to higher selectivity for ethene.Formation of large crystalline NiO particles(22-32 nm) over Ni/Al2O3 catalysts decreased the selectivity for ethene.     

Selective hydrogenation of phenylacetylene on Pd/Al2O3: Effect of the addition of Pt and particle size

Phenylacetylene hydrogenation on Pd, Pt and Pd–Pt/Al₂O₃ catalysts has been studied. In all catalysts activity was found not to depend on particle size. However, selectivity to styrene was found to depend on Pd/Al₂O₃ catalysts. Carbon deposition in both metal and support explains such a behavior. Nevertheless, in small Pd particles a longer residence time of styrene may control the selectivity.     

Deactivation of a fixed bed Cr2O3/Al2O3 catalyst during butene-1 dehydrogenation, II. Model predictions

A model has been used to predict the temperature, butene and carbon concentration profiles in a fixed bed reactor during butene-1 dehydrogenation when Cr₂O₃/Al₂O₃ is used as a catalyst. Furthermore, the model gives information about the temperature, butene and carbon concentration profiles inside the pellet.     

Catalytic hydrogenation of C60 fullerene

Catalytic hydrogenation of C₆₀ with H₂ or by hydrogen transfer reactions using Pd/SiO₂, Rh/Al₂O₃ and Ru/Al₂O₃ has been studied. The final products containing partially hydrogenated C₆₀ fullerence C₆₀H₄₂–C₆₀H₄₆ were characterized by FTIR, UV and NMR methods.     

Toluene methylation on AlPO4-Al2O3 catalysts (5–15 wt.% Al2O3)

The alkylation of toluene with methanol over AlPO₄-Al₂O₃ (5–15 wt.% Al₂O₃) catalysts produces a mixture of xylenes (XYL) although trimethylbenzenes (TMB) were also found. The TMB selectivity increased with temperature at the expense of XYL selectivity. Isomer distribution was approximately 48, 24 and 27 mol% foro-, m- andp-XYL, and 74, 26 and 0 mol% for 1,2,3-, 1,2,4- and 1,3,5-TMB, both quite different from the equilibrium isomer composition. The catalytic activity increased with alumina content, however, it decreased on increasing the calcination temperature in the 923–1273 K range. Good correlations between catalytic activity and the increase in acidic properties with Al₂O₃ loading (as determined by base chemisorption, in the gas phase,versus pyridine and 2,6-dimethylpyridine) have been obtained.     

CpTiCl3-alumina-silica system reduced with NaNp

The system CpTiCl₃/Al₂O₃–SiO₂ (0–100 wt.% of Al₂O₃), (Cp=cyclopentadienyl) was reduced with a tenfold excess of NaNp (Np=naphthalene) in THF and argon atmosphere at room temperature. Only titanium(IV) and titanium(III) compounds were found by the polarographic method in the systems studied. The amount of the titanium(III) compounds is influenced by the acidity of supports.