ESCA study of (Mo+Pt)/SiO2, (W+Pt)/SiO2 and (Re+Pt)/SiO2 catalysts

Supported catalysts obtained from organometallic compounds have been studied by ESCA. The data obtained indicate a decrease in electron density on the Pt atoms as a result of interaction with Mo, W and Re ions bound to silica.

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, . , Mo, W, Re, .

     

Synergetic effect in thiophene hydrogenolysis on sulfied (Ni?Nb)/SiO2 catalysts

Nonadditive increase in the activity of sulfided (Ni–Nb)/SiO₂ catalysts, compared to Nb/SiO₂ and Ni/SiO₂, has been found, with the maximum synergetic effect observed at the atomic ratio =Ni/Ni+Nb=0.2.

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(Ni–Nb)/SiO₂ Nb/SiO₂ Ni/SiO₂, =Ni/(Ni+Nb)=0,2.

     

Influence of rare earth ions on the properties of Pd/SiO2 in CO hydrogenation

Systematic studies of the effect of the lanthanoid (Ln) nature on the activity and selectivity of (Pd+Ln)/SiO₂ catalysts obtained by decomposition of anchored Ln and Pd complexes in methanol synthesis from CO and H₂ have been carried out. It has been established that the highest promoting effect is observed for Pr and Ho ions.

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(Ln) (Pd+Ln)/SiO₂ , Ln Pd, CO H₂. Pr Ho.

     

EPR study of the nature of active sites and the type of their deactivation in CO hydrogenation on (Ni+Ti)/SiO2 catalysts

As shown by EPR, upon supporting Ni(-C₃H₅)₂ on Ti/SiO₂, the Ni complex is coordinated to Ti³⁺ ions. Deactivation of (Ni+Ti)/SiO₂ catalysts so obtained during CO hydrogenation is due to the oxidation of Ti³⁺ ions and metallic nickel particles by reaction products.

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, Ni(-C₃H₅)₂ Ti/SiO₂ Ni Ti³⁺. , (Ni+Ti)/SiO₂ CO Ti³⁺ .

     

Non-conventional preparation of Ru/SiO2 catalysts

A metal-supported catalyst (Ru/SiO₂) has been prepared using the sol-gel technique. The structural properties of the solid obtained are compared to those of a conventionally impregnated catalyst.

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(Ru/SiO₂) -. .

     

改性SiO2对铁基催化剂H2、CO吸附及加氢性能的影响

采用溶胶凝胶方法通过掺杂修饰剂M（M=Mn、Zn、Zr、Sr）制备出改性SiO₂载体,再用浸渍法将Fe元素负载于该载体上制成系列催化剂。采用X射线衍射（XRD）、氮气物理吸附-脱附、X射线光电子能谱（XPS）等手段表征了催化剂的织构性质、晶相组成和电子性质。利用程序升温手段研究了催化剂的H₂还原吸附性质和CO加氢性能。借助动力学分析方法研究了催化剂与H之间的相互作用。结果表明,少量掺杂的修饰剂对催化剂的Fe物相组成以及表面Fe物种电子状态基本没有影响,但降低了催化剂的比表面积以及活性相分散度,削弱了对H₂的吸附能力,降低催化剂的H₂脱附活化能。Zn、Zr的掺杂抑制了催化剂的还原,而Mn、Sr的掺杂却促进催化剂的还原。Mn、Zn、Zr的掺杂抑制催化剂表面CO的解离吸附,Sr则促进CO的解离吸附,Mn、Zn、Zr、Sr均促进低温区间C-C耦合和加氢反应,其中,Mn、Zr促进加氢的作用更显著。     

Conversion of hydrocarbons on supported catalysts prepared via decomposition of surface complexes. Preparation and properties of (Ga+Pt)/SiO2 and (Ga+Pt)/Al2O3 catalysts

The addition of gallium is shown to increase Pt dispersity and its stability to deactivation in n-hexane dehydrocyclization, to decrease the rate of n-hexane hydrogenolysis and to increase the selectivity to benzene, apparently, due to the interaction of Pt clusters with surface Ga ions.

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, -, - . .

     

Influence of Pr ions on the properties of Pd/SiO2 and Pt/SiO2 catalysts in oxidation of n-butane

It has been established that (M_VIII+Pr)/SiO₂ catalysts (M_VIII=Pd or Pt) obtained from organometallic precursors, have increased the dispersity of Pt, but their TN in deep oxidation of n-butane is by 3–6 times lower than that of unmodified M_VIII/SiO₂.

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(M_VIII+Pr)/SiO₂ ( M_VIII=Pd, Pt), , Pt, 3–6 - M_VIII/SiO₂.

     

Gas-phase hydroformylation of propylene on Ru/SiO2 catalysts

Ru/SiO₂ catalysts prepared by reduction of supported RuCl₃·xH₂O are active in gas-phase hydroformylation of propylene at low pressure (ca. 0.3 MPa) of H₂+CO+C₃H₆ mixtured and show unexpectedly high selectivity towards unbranched oxo-products. Data concerning the effect of electronic state and dispersity of Ru on their catalytic behavior have been obtained.

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Ru/SiO₂, RuCl₃·xH₂O, (0,3 ) - . .

     

X-ray spectral investigation by synchrotron radiation of supported Re/SiO2 and (Re+Pt)/SiO2 catalysts prepared via triethoxyrhenium

Using synchrotron radiation L_III absorption spectra of rhenium in Re/SiO₂ and (Re+Pt)/SiO₂ catalysts prepared via triethoxyrhenium have been studied. The conclusion has been drawn that reduced catalysts contain lowvalent rhenium ions and their composition is more uniform than that of the previously examined catalysts Re/Al₂O₃ and (Re+Pt)/Al₂O₃ prepared by a conventional impregnation technique.

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L_III- Re/SiO₂ (Re+Pt)/SiO₂, . , , Re/Al₂O₃ (Re+Pt)/Al₂O₃, .

     

Acidic properties of TiO2?SiO2 catalysts

The acidic properties of a series of TiO₂–SiO₂ catalysts with different Ti/Si mole ratios have been studied. In order to determine the amount of acid centers and the acid strength distribution, the Benesi method of discontinuous titration has been used. Thermogravimetric measurements were also carried out.

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TiO₂–SiO₂ Ti/Si. , - . .

     

Catalytic hydrogenation of carbon monoxide on RuFe/SiO2 catalysts

The H₂+CO reaction on silica supported Ru, Fe and RuFe catalysts prepared from metal carbonyl clusters has been investigated under atmospheric and 20 bar pressure. According to the change of selectivity values with temperature and with pressure, the participation of surface carbon proposed earlier by several authors seems to be confirmed by this work.

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H₂+CO Ru, Fe RuFe, , 20 . , , , .

     

Reduction kinetics of benzylideneaniline over Pd/SiO2?AlPO4 and Pd/sepiolite catalysts

The liquid-phase hydrogenation of benzylideneaniline over various Pd catalysts, using gaseous hydrogen has been studied. We have synthesized several Pd catalysts (3 wt.%) over SiO₂–AlPO₄ and sepiolite supports, and determined their metal surface area by X-ray diffraction. The study performed shows that the process follows a Langmuir-Hinshelwood kinetics with zero order in benzylideneaniline, r_i=k_okP_H2 (1+KP_H2)^–1.

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Pd, . Pd (3 .%) SiO₂–AlPO₄ . - . , - , r_i=k_okP_H2 (1+KP_H2)^–1.

     

Modification of the catalytic activity of Ni/SiO2 in ethane hydrogenolysis, benzene and co hydrogenation by reduction at high temperatures and restoration by O2?H2 treatments

An increase of the temperature of reduction of Ni/SiO₂ from 900 to 1120 K results in a decrease of catalytic activity per unit area in benzene hydrogenation and ethane hydrogenolysis. O₂–H₂ treatments restore the activities. This behavior is similar to that observed on Pt-based catalysts. In contrast, the CO+H₂ reaction on nickel is not affected by such treatments.

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Ni/SiO₂ 900 1120 . O₂–H₂ . , , CO+H₂ .

     

Liquid-phase hydrogenation on new AlPO4?SiO2 supported rhodium catalysts

The liquid-phase catalytic hydrogenation of various organic compounds was carried out using new rhodium catalysts supported on AlPO₄–SiO₂ (2080 wt. %) system, in methanol as solvent, under low hydrogen pressure (0.55 MPa) and at 293 K. Neither alkene isomerization nor hydrogenolysis products were detected in any of the cases.

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AlPO₄–SiO₂ (2080 . %), , , (0,55 MPa) 293 . , .

     

Dispersity and reducibility of the molybdenum oxide phase in SiO2, SiO2?Al2O3 and γ-Al2O3 supported molybdena catalysts

XRD, isothermal and temperature-programmed reduction (TPR) experiments were carried out with SiO₂, SiO₂–Al₂O₃ and -Al₂O₃ supported catalysts. Molybdena is in a more disperse state on supports containing more alumina and it is more reducible on SiO₂–Al₂O₃ than on SiO₂ or -Al₂O₃. TPR curves were shown to reflect connections between reduction kinetics and dispersity.

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-, , SiO₂, SiO₂–Al₂O₃ -Al₂O₃. , , SiO₂–Al₂O₃ SiO₂ -Al₂O₃. .

     

CO and NO adsorption on photoreduced Mo/SiO2 catalysts

CO and NO adsorption on photoreduced Mo/SiO₂ catalysts has been studied by IR and mass-spectrometric methods. Products of interaction between adsorbed molecules and surface molybdates of various structures have been identified.

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- - CO NO CO Mo/SiO₂ . .

     

Effect of residual chlorine on the activity of Pd/SiO2 catalysts during the selective hydrogenation of styrene

Precipitates obtained from sodium aluminate and mixtures of nitric acid and silicofluoric acid have been investigated. Properties of supports prepared from these materials are strongly affected by the chemical and phase composition of the precipitates. These substances are suitable for the preparation of large — pore supports for hydrorefining catalysts.     

Hydrogen pressure dependence of the reaction of neopentane with hydrogen over Pd/SiO2 and Pt/SiO2 catalysts

H₂ pressure influences in different ways the reaction rates of neopentane conversion over Pd/SiO₂ and Pt/SiO₂ catalysts. It seems that on Pt/SiO₂ both isomerization and hydrogenolysis involve a common surface intermediate (probably an adalkyl), whereas on Pd/SiO₂ the hydrogenolysis goes via more dehydrogenated species than those involved in isomerization.

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H₂ Pt/SiO₂ Pd/SiO₂. , Pt/SiO₂ (, ), Pd/SiO₂ , .

     

(Pd+Pr)/zeolite catalyst for the synthesis of C2?C4 hydrocarbons from CO and H2

The activity of (Pd+Pr)/ZSM-5 catalyst is an order of magnitude higher compared to unmodified Pd/ZSM-5. Its selectivity towards C₂–C₄ hydrocarbons containing olefins is about 50 wt. %.

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(Pd+Pr)/CBK - Pd/CBK, C₂–C₄ , , j50% .