Particle size dependence for CO chemisorption on supported Ru catalysts

The stoichiometry of CO chemisorption on highly dispersed zeolite-supported Ru has been investigated. This stoichiometry, which can be expressed as CO/H, increases with decreasing Ru particle diameter. For diameters <1.6 nm this ratio approached a limiting value of 4–5, indicating the formation of surface carbonyls. No direct influence of the support on this ratio could be detected.

---

CO Ru, . , CO/H, Ru. <1,6 n 4–5, . .

     

Measurement of the dispersity of supported ruthenium catalysts by oxygen chemisorption

A highly dispersed (Ø (Ru)<10 Å, from electron microscopy) Al₂O₃-supported catalyst and not so well dispersed silica supported Pt, Ru, Pt, Ru-alloy catalysts were investigated. Oxygen coverage of Ru is found to be close to 2 at 20 °C over the monometallic Ru catalysts as well as over the Pt, Ru-alloy catalysts.

---

(Ø (Ru)<10 Å ) Al₂O₃ Pt Ru Pt Ru . Ru 2 20°C Ru, Pt Ru.

     

Influence of particle size on the stoichiometry of chemisorption of oxygen on supported nickel catalysts

It has been found that the stoichiometry of adsorption of oxygen on nickel supported on silica is linearly correlated to the particle size of the metal. It is shown that the combined use of hydrogen and oxygen chemisorption at room temperature allows to determine both the dispersity and reduction degree of nickel.

---

, . , , .

     

Some aspects of reversible chemisorption on supported platinum catalysts

Hydrogen and carbon monoxide chemisorption on supported platinum catalysts have been studied volumetrically and the adsorption heats determined by microcalorimetric measurements. From the results of this study is concluded that the use of reversible (or second) isotherms as a measure of weak chemisorption would appear inadequate.     

Characterization of titania and zirconia supported molybdenum oxide catalysts by low temperature oxygen chemisorption

Low temperature oxygen chemisorption (LTOC) has been applied to characterize a series of TiO₂ and ZrO₂ supported Mo-oxide catalysts. The monolayer coverage of the surface is completed when the Mo loading reaches 6% and 4% on the TiO₂ and ZrO₂ supports, respectively. The results are explained with the help of a Patch model of the Mo-oxide phase.

---

Mo- TiO₂ ZrO₂ . Mo TiO₂ ZrO₂ 6% 4%, . Patch Mo- .

     

Gas phase hydrogenation of o-xylene on Ru supported catalysts

The gas phase hydrogenation of o-xylene on supported ruthenium catalysts has been studied. Metal dispersity, acidity of the support and carbonaceous residues modified the stereoselectivity of Ru. Following the rollover model for the reaction, the results are explained in terms of the residence time of the reactive species on the metal surface.     

Hydrogen chemisorption on supported platinum, gold, and platinum-gold-alloy catalysts

Alloyed catalysts receive considerable attention, because of their unique catalytic properties; they often show higher selectivity, activity, and stability compared to the pure metal particles. To provide insights in the origins of these features, we report the structure and the interaction of hydrogen with each of the metals in an intimately mixed platinum-gold catalyst and compare these characteristics to those in the single metal particles. X-Ray absorption spectroscopy (XAS) and electron microscopy analysis showed that the structure of the mixed particle differed from the single metal particles. The interaction of platinum with hydrogen is stronger than the H-Au interaction and the adsorption sites were different. EXAFS analysis showed that the structure of the platinum clusters changes with increasing hydrogen coverage, observed as a relaxation of the contracted Pt-Pt distance and an increase in the Pt-Pt coordination number. No such changes were observed for gold clusters. Well-mixed PtAu-alloy clusters, with a bulk Au-to-Pt ratio of two, supported on SiO(2), adsorb hydrogen on both platinum and gold atoms, which indicates that gold cannot be regarded as an inert metal. The heat of adsorption on the platinum ensembles does not decrease upon alloying; the weakening of the overall hydrogen adsorption strength when alloying platinum with gold is an ensemble-size effect.     

Surface reorganization of carbon supported cobalt catalysts during CO chemisorption

Different monometallic catalysts containing Fe, Co or Ni and a Fe–Co bimetallic catalyst have been prepared by impregnation of an activated carbon. The formation of subcarbonyl species during CO adsorption, as detected by the slow adsorption rate, was observed. From the CO adsorption isotherms, the possibility of a surface reorganization in the Co catalysts induced by the interaction with CO is deduced.

---

, Fe, Co Ni Fe–Co . CO . Co , CO.

     

An extended Hückel study of hydrogen and oxygen chemisorption on Ru(001) surface

Extended Hückel MO theory has been applied to treat the chemisorption of hydrogen and oxygen atoms on Ru(001) surfaces. The site of chemisorption, surface-adatom distance, chemisorption energy and the vibrational frequency of the adatom on the surface have been calculated. For different sites, the chemisorption energy (E_c) results are as follows: For hydrogen, |E_c|(centre) > |E_c|(top) > |E_c|(bridge); while for oxygen, |E_c|(bridge) > |E_c|(top) > |E_c|(centre). These results are critically discussed in the light of the recent results obtained from the electron energy-loss spectroscopy (EELS) experiments.     

Hydrogenolysis of glycerol over HY zeolite supported Ru catalysts

An enhanced active and selective catalyst consisting of ruthenium supported on dealuminated HY zeolite has been prepared by a wet impregnation method. It was found that BET surface area of Ru/HY catalysts significantly increases after HCl treatment. This treatment also increases the concentration of strong acid sites in the catalyst. The hydrogenolysis of glycerol over 5 wt% Ru/HY catalyst was investigated at 190-220 ℃, an initial H2pressure of 3-6 MPa, and in 20 wt% glycerol aqueous solution. The results indicate that HCl treated Ru/HY catalyst shows higher activity compared with the untreated Ru/HY catalyst, and that the glycerol hydrogenolysis efficiency is influenced by the porosity and acidity of the support. A selectivity to 1,2-PDO of 81.3% at a glycerol conversion of 60.1% under 3 MPa H2pressure and 220 ℃ for 10 h was achieved over the modified Ru/HY catalyst with a 1.0 mol/L HCl treatment. It has also been shown that a longer reaction time, a higher temperature and a higher H2pressure have the positive effects on the glycerol hydrogenolysis efficiency of the enhanced Ru/HY.     

Oxygen chemisorption on silver catalysts

Silver dispersity in the catalysts studied has been investigated. Equilibrium values of oxygen adsorption on silver catalysts with different mean sizes of metal crystallites are found and compared.

---

. .

     

Wormholelike mesoporous carbon supported Pt Ru catalysts toward methanol electrooxidation

Wormholelike mesoporous carbons(WMCs) with three different pore diameters(D_p),namely WMC-F7(D_p=8.5nm),WMC-F30(D_p=4.4nm),and WMC-FO(D_p = 3.1nm) are prepared via a modified sol-gel process.Then PtRu nanoparticles with the particle size(d_(Pt)) of ~3.2 nm supported on WMCs are synthesized with a modified pulse microwave-assisted polyol method.It is found that the pore diameter of WMCs plays an important role in the electrochemical activity of PtRu toward alcohol electrooxidation reaction.PtRu/WMC-F7 with Dp 2d_(Pt) exhibits the largest electrochemical surface area(ESA) and the highest activity toward methanol electrooxidation.With the decrease in D_p,PtRu/WMC-F30 and PtRu/WMC-FO have much lower ESA and electrochemical activity,especially for the isopropanol electrooxidation with a larger molecular size.When D_p is more than twice d_(Pt),the mass transfer of reactants and electrolyte are easier,and thus more PtRu nanoparticles can be utilized and the catalysts activity can be enhanced.     

Cellulose conversion to polyols on supported Ru catalysts in aqueous basic solution

It is of great significance and challenge to achieve direct conversion of cellulose to specific polyols, e.g., ethylene glycol and propylene glycol. For such selective conversion, a novel one-pot approach was studied by combination of alkaline hydrolysis and hydrogenation on supported Ru catalysts. A wide range of bases including solid bases, e.g., Ca(OH)₂ and La₂O₃, and phosphate buffers were examined in the cellulose reaction in water, and the cellulose conversions and polyol products depended largely on the basicity or pH values in the aqueous solutions. Ethylene glycol, 1,2-propanediol, and especially 1,2,5-pentanetriol were obtained with selectivities of 15%, 14% and 22%, respectively, at 38% cellulose conversion at pH 8 in phosphate buffer solution. These preliminary results provide potentials for efficient conversion of cellulose to targeted polyols by using the advantages of bases.     

Exchange of molecular oxygen with the oxygen of supported palladium catalysts

Heterogeneous exchange of molecular oxygen with the oxygen of supported platinum catalysts and bulk palladium oxide has been studied. A correlation has been established between the exchange rate and the dispersity of supported palladium oxide.

---

. , .

     

Ru/Co-Al-O负载型催化剂的制备及其加氢脱氧性能研究

先采用共沉淀法制备出Co-Al类水滑石,其经煅烧后形成的复合氧化物用作载体制备出一系列Ru/Co-Al-O负载型催化剂,并采用XRD、BET、FT-IR等方法对其结构性能进行表征分析,最后以木质素生物质油的典型含氧化合物对甲基苯酚为模型,测试所制催化剂的加氢脱氧性能。主要研究了载体中Co/Al物质的量比、催化剂还原温度等因素对催化剂加氢脱氧活性的影响,并优化了HDO反应温度。结果表明,当Co/Al物质的量比为3∶1,催化剂还原温度为350℃,反应温度为275℃时,催化剂的加氢脱氧活性最高,催化对甲基苯酚加氢脱氧反应的转化率和脱氧率都达到了100%。     

改性二氧化钛负载贵金属Ru催化剂催化降解苯胺溶液

苯胺类废水污染物具有结构复杂、浓度高、不易生物降解、生物毒性大等特点,传统的苯胺降解措施存在着许多弊端,很难达到排放标准.催化湿法氧化技术(CWAO)主要针对降解高浓度难降解的有机废水,表现出降解效率高、反应时间短、对生物毒性物质的废水降解效果良好等优点,越来越受到人们的重视.但催化剂在使用过程中,需要在高温高压下进行,且有机物降解产生了有机酸,使得催化剂的活性组分流失和载体的物理化学性质发生变化,导致其催化活性下降.因此,需要开发出一种降解活性高,性能稳定的催化剂成为此技术在工业中广泛应用的关键.本文采用溶胶凝胶法对二氧化钛进行改性,制备了Ti0.9Zr0.1O2和Ti0.9Ce0.1O2载体,采用过量浸渍法将三氯化钌负载到载体表面制备了2%Ru/Ti0.9Zr0.1O2和2%Ru/Ti0.9Ce0.1O2催化剂.在高温高压反应条件下,以苯胺为催化湿法氧化污染物,对不同催化剂湿法降解苯胺进行比较研究,系统地探究了催化降解的反应温度和反应压力对苯胺降解的影响.此外,利用HPLC-MS鉴定出催化降解产生的中间产物,确定了催化降解的反应路径图.在改性的催化剂中,2%Ru/Ti0.9Zr0.1O2催化剂表现出最高的催化降解活性和稳定性.在初始苯胺浓度4 g/L,催化剂浓度4 g/L,反应温度180℃,O2压力1.5 MPa下,反应时间5 h后,苯胺完全转化,COD转化率达88.3%.并且催化剂进行三次循环试验后,苯胺转化率仍接近100%.X射线衍射和N2物理吸附结果表明,Ce,Zr掺杂到TiO2晶格中形成了共溶体,其晶格尺寸更小,比表面积和孔体积更大.负载贵金属后,并未出现其他晶相,说明贵金属均匀分散在载体表面.透射电镜结果表明,贵金属负载在改性TiO2上表现出较好的分散性和较小的颗粒尺寸,为催化降解苯胺提供更多的催化活性位点,而Ru/TiO2催化剂表面,贵金属发生团聚现象且颗粒尺寸大.X射线光电子能谱结果表明,Ce,Zr的掺杂使得TiO2表面活性氧和四价Ru的含量增加,更多的表面活性氧成为催化降解苯胺的直接原因.H2程序升温还原结果表明,在300?400oC处还原峰对应于催化剂载体晶格氧的还原,改性后,其还原峰增至2倍,即使在贫氧环境下,改性催化剂可以及时从载体中释放晶格氧,为催化降解苯胺提供更多的活性氧.     

Electron microscopic and chemisorption studies of the dispersity of supported rhodium catalysts of various compositions

The dispersity and size distribution of metal particles in mono- and bimetallic rhodiumcontaining catalysts prepared via decomposition of SiO₂- and Al₂O₃-supported complexes and impregnation of the support by inorganic metal compounds have been studied.

---

, SiO₂ Al₂O₃ .

     

介孔炭的孔结构对其负载的Ru基氨合成催化剂性能的影响

采用模板法合成了介孔炭(MC),研究了其孔结构对其负载的Ru基氨合成催化剂Ba-Ru-K/MC性能的影响,采用N₂吸附脱附、扫描电镜和透射电镜等手段对介孔炭的孔结构进行了表征.研究发现,介孔炭载体的孔结构取决于模板剂的用量,当SiO₂/C质量比为1.0时,所制介孔炭比表面积最大.介孔炭负载的Ba-Ru-K催化剂活性与其介孔比表面积相关.在425℃,10MPa和10000h^-1条件下,合成氨的反应速率为139mmol/(g_cat·h).     

An ESR study of electron transfer and oxygen adsorption on 95Mo supported catalysts

ESR studies using molybdenum enriched in ⁹⁵Mo have confirmed that (O₂^?)_s is stabilised at Mo⁶⁺ sites at 77 K on silica and alumina supported molybdenum. Warming the Mo/Al₂O₃ to 300 K leads to an increase in the number of (O₂^?)_s ions observed due to electron transfer from reduced molybdenum sites to give additional (O₂^?)_s adsorbed at Al³⁺ sites on the support. Molybdenum is not involved at the adsorption site of (O₂^?)_s on the magnesia supported catalyst.     

Influence of oxygen on catalytic properties of supported palladium catalysts in CO hydrogenation

It has been established that the addition of oxygen to synthesis gas has a positive effect of the activity and selectivity of supported palladium catalysts in methanol synthesis. The degree of the effect of oxygen depends on the chemical nature of the support and the conditions of catalysis, preceding the addition of oxygen to the reaction mixture. The probable causes for the influence of oxygen on the catalytic properties of palladium, supported on oxide supports, have been discussed.Translated from Teoreticheskaya i Éksperimental'naya Khimiya, Vol. 25, No. 5, pp. 557–563, September–October, 1989.