氧化锆担载镍甲烷干重整催化剂的载体形貌效应

煤层气是储量十分丰富的煤炭伴生资源,也是煤炭开采中最大的安全隐患之一,同时还是重要的温室气体.研究煤层气的高效、清洁资源化利用具有资源和环境双重意义.因此,世界主要产煤国均十分重视煤层气的开发和利用.煤层气的主要成分是甲烷,目前主要通过两种方式实现其资源化利用:(1)直接转化,主要通过氧化偶联、催化氧化官能团化或脱氢芳构化等途径将其转化为高碳烃、含氧化合物及芳烃等;(2)间接转化,甲烷首先经催化重整反应制取合成气,而后再经Fischer-Tropsch合成、甲醇化和氢甲酰化等过程来合成饱和烃、烯烃、甲醇及其他含氧化物.对于前者,由于热力学限制,反应收率很低,应用前景较差,而经由合成气这一平台产物的间接转化路线被认为是一条甲烷资源化利用颇具工业前景的转化路线.因此,甲烷催化重整制合成气备受关注.研究表明,贵金属具有较好的甲烷重整催化性能,但其储量有限、价格昂贵的内在缺陷不利于甲烷大规模转化和资源化利用.Ni基催化剂具有与贵金属可比的催化活性和选择性,且其储量丰富,价格低廉,因此在甲烷重整反应中备受青睐.但是,相对于贵金属,Ni基催化剂易于积碳和烧结失活,这已成为制约其大规模工业化应用的瓶颈.迄今,大量文献报道关注如何提高Ni基催化剂的催化稳定性.而载体形貌调控是调节负载型催化剂的有效途径.本文开展了用作载Ni催化剂的氧化锆载体的形貌调控研究,以期可以有效调节载Ni催化剂的物化性质,进而调控载Ni催化剂的甲烷重整催化性能.采用水热法成功制备了松球状和鹅卵石状的单斜相氧化锆载体,进一步负载镍,制备了载镍催化剂,用于甲烷重整制合成气反应.具有分级结构的松球状氧化锆载Ni催化剂(Ni/ZrO2-ipch)展示出比鹅卵石状氧化锆和常规氧化锆纳米粒子载Ni催化剂显著好的催化活性和稳定性.采用XRD、N2吸附、TEM、H2-TPR、CO化学吸附、CO2-TPD、XPS和TGA等手段研究了松球状氧化锆载Ni催化剂高催化活性和稳定性的原因和机制.发现,其较高的催化活性主要归因于高的Ni分散度、改善的可还原性、促进的氧流动性以及较多的碱性位和较强的碱性,这些物化性质依赖于氧化锆载体的独特形貌.分级结构的松球状氧化锆载Ni催化剂高的甲烷重整催化稳定性主要源于催化剂的高抗烧结、抗积碳性能.加强的金属载体效应和介孔限域效应可以阻止金属Ni的高温烧结,而优良的抗积碳稳定性主要源于催化剂良好的氧流动性、较多的碱性位、较强的碱性以及小的Ni粒子尺寸.鉴于分级结构松球状氧化锆载Ni催化剂高的催化活性和优良的抗积碳、抗烧结稳定性,该催化剂用于甲烷重整制合成气具有广阔前景.而所制备的分级结构松球状氧化锆由于具有独特的结构和优良的热稳定性,可以作为性能优良的载体用于其他反应,尤其对于高温转化过程可望表现出明显优势.     

The promoting effect of energetic activation of a methane molecular-beam in the direct catalytic partial oxidation of methane

Energetic activation of a methane molecular-beam promoted remarkably the direct catalytic partial oxidation on Pt and Rh foils, in particular, hydrogen formation was dramatically enhanced.     

Effects of surface states over core-shell Ni@SiO_2 catalysts on catalytic partial oxidation of methane to synthesis gas

In the present work, core-shell Ni@Si O2 catalysts were investigated in order to evaluate the relevance of catalytic activity and surface states of Ni core as well as Ni nanoparticles size to catalytic partial oxidation of methane(POM). The catalysts were characterized by N2 adsorption,H2-TPR, XRD, TEM and XPS techniques. The catalytic performance of the core-shell catalysts was found to be dependent on the surface states of catalyst, which influenced the formation of products. It was considered that carbon dioxide formed on the oxidized nickel sites(Ni O)and carbon monoxide produced on the reduced sites(Ni). The surface states of active metal in the dynamic were influenced both by the size of Ni core and the porosity of silica shell. However, the catalytic activity would be debased when the size of Ni core was under a certain extent,which can be ascribed to the fact the carbon deposition increased with the increasing content of Ni O. The effects of surface states of Ni@Si O2 catalyst on the catalytic performance were discussed and the reaction pathway over Ni core encapsulated inside silica shell was proposed.     

Microwave effect on partial oxidation of methane to syngas

In this paper the results of the partial oxidation of methane over Ni-based and Co-based catalysts activated by two different heating modes (conventional and microwaves) are reported. Compared with a conventional heating mode, the temperature of the catalytic bed is much lower and there is a higher selectivity of CO and H₂ with microwave irradiation.     

The influence of the active component and support nature, gas mixture composition on physicochemical and catalytic properties of catalysts for soot oxidation

Physicochemical and catalytic properties of compositions Fe(Ce)–Mn–O/support (gamma-, theta-, alpha-Al₂O₃, SiO₂ as the support) and Pt/CeO₂/theta-Al₂O₃ for oxidation of soot were characterized. It was established that the phase composition of the initial catalysts depended mainly on the nature of the active component and preparation conditions. Non-isothermal treatment of the soot–catalyst compositions at the temperature up to 1000 °C resulted in a change in the phase composition depending mainly on the final treatment temperature. The catalyst surface area was determined by the support nature. It was established that catalyst activities for oxidation of soot are determined by both catalyst nature and composition of gas mixture. The process of the soot oxidation is thought to involve oxygen from the catalyst surface. The higher proportion of weakly bound surface oxygen, the higher was the catalyst activity. An increase in the oxygen concentration from 5% O₂/N₂ to 15% O₂/N₂ is shown to lead to a decrease of the temperature of the soot oxidation. The influence of the oxygen concentration on the process of soot oxidation becomes weaker in the presence of water vapor. Results showed that the presence of NO in the gas mixture favors a decrease in the oxidation temperature of the soot, the higher being the nitrogen oxide concentration, the more pronounced effect. Introduction of SO₂ in amount of 50 ppm in the gas mixture has no noticeable effect on the process of the soot oxidation. Among the catalysts under study, Fe–Mn–K–O/gamma-Al₂O₃ is most effective to oxidation of the soot at otherwise identical conditions.     

State of supported rhodium nanoparticles for methane catalytic partial oxidation (CPO): FT-IR studies

The effect of pretreatments as well as of rhodium precursor and of the support over the morphology of Rh nanoparticles were investigated by Fourier transform infrared (FT-IR) spectroscopy of adsorbed CO. Over a Rh/alumina catalyst, both metallic Rh particles, characterized by IR bands in the range 2070-2060 cm-1 and 1820-1850 cm-1, and highly dispersed rhodium species, characterized by symmetric and asymmetric stretching bands of RhI(CO)2 gem-dicarbonyl species, are present. Their relative amount changes following pretreatments with gaseous mixtures, representative of the catalytic partial oxidation (CPO) reaction process. The Rh metal particle fraction decreases with respect to the Rh highly dispersed fraction in the order CO approximately CO/H2 > CH4/H2O, CH4/O2 > CH4 > H2. The metal particle dimensions decrease in the order CH4/O2 > H2 > CH4/H2O > CO > CO/H2. Grafting from a carbonyl rhodium complex also increases the amount and the dimensions of Rh0 particles at the catalyst surface. Increasing the ratio (extended rhodium metal particles/highly dispersed Rh species) allows a shorter conditioning process. The surface reconstruction phenomena going on during catalytic activity are related to this effect.     

The promoter effect of lanthana on MgO supported ruthenium catalysts for ammonia synthesis

When activated at high temperature (873 K) doped lanthana such as La₂O₃, Ce₂O₃, Sm₂O₃ derived from nitrate showed remarkable effect on the MgO-supported ruthenium activity for ammonia synthesis. The activity treated with hydrogen at 873 K became 5 times as active as that treated at 623 K. The activity levels were almost the same as those of the Ru-lanthana (support) system under the same activation condition. It was thought that the lanthana was partly reduced and a strong metal support interaction occurred. The partially reduced lanthana was thought to donate electrons to the contacting Ru atoms forming the active centers. The other characters such as the stability were also discussed by comparing with alkali promoters.     

Temporal decay of the catalytic oxidation of methane over palladium supported on silica

The temporal decay of the oxidation of methane(CH4-O2reaction)over palladium supported on silica is determined experimentally at different temperatures,comparing the results with those of various classical models which show the behavior of the adsorbed phase as the cause of the phenomenon.This effect is visualized through Monte Carlo simulations of the CH4-O2reaction on a mixed lattice whose partial poisoning,due to the configuration of the OH groups on the surface of the adsorbate,is translated into a gradual decay of the reaction’s activity.     

Preparation and catalytic activity for ammonia synthesis of several ruthenium supported catalysts

Ruthenium supported catalysts were prepared from RuCl₃ · 3H₂O and K₄[Ru(CN)₆] · 3 H₂O solutions, upon several acid/base pretreated γ-Al₂O₃ samples, using water and acetone as solvents. Metallic adsorption was found to be dependent on solvent and precursor used. An increasing final ruthenium content of the catalysts with increasing acid site content of the support is observed, when K₄[Ru(CN)₆] · 3 H₂ is used as a precursor. The catalytic activity was followed at atmospheric pressure and 593 K (N₂/H₂ = 1/3). Catalysts prepared from K₄[Ru(CN)₆] · 3 H₂O were about ten fold more active than those prepared from RuCl₃ · 3 H₂O. The catalytic activity of catalysts prepared from K₄[Ru(CN)₆] · 3 H₂O was found to be sensitive to the acid-pretreatment of γ-Al₂O₃, while the activity of those prepared from RuCl₃ · 3 H₂O was not sensitive to the pretreatment of the support.     

Coke formation during high pressure catalytic partial oxidation of methane to syngas

Summary Carbonization of the surface of alumina-based catalysts has been studied with respect to the composition of the catalysts and conditions of the propionitrile ammonolysis. It was shown that the surface concentration of carbon increases with the increase in temperature and with time of the reaction and depends on the catalysts nature in the order: Al-Zr(5)-O < Al-Zr(40)-O < Al-O < Al-Mg-O. The surface concentration of the Brönsted acidic sites follows the same sequence.     

Catalytic partial oxidation of methane to synthesis gas over a ruthenium catalyst: the role of the oxidation state

The catalytic partial oxidation of methane to synthesis gas over ruthenium catalysts was investigated by thermogravimetry coupled with infrared spectroscopy (TGA-FTIR) and in situ X-ray absorption spectroscopy (XAS). It was found that the oxidation state of the catalyst influences the product formation. On oxidized ruthenium sites, carbon dioxide was formed. The reduced catalyst yielded carbon monoxide as a product. The influence of the temperature was also investigated. At temperatures below the ignition point of the reaction, the catalyst was in an oxidized state. At temperatures above the ignition point, the catalyst was reduced. This was also confirmed by the in situ XAS spectroscopy. The results indicate that both a direct reaction mechanism as well as a combustion-reforming mechanism can occur. The importance of knowing the oxidation state of the surface is discussed and a method to determine it under reaction conditions is presented.     

Yttria promoted metallic nickel catalysts for the partial oxidation of methane to synthesis gas

A metallic Ni catalyst was prepared with nickel sponge, followed by acid treatment. It was further promoted with yttria by an impregnation method. The catalysts were characterized by SEM, BET, XRD, TPR, XPS, etc., and studied in the partial oxidation of methane to syngas. The characterization results showed that the yttria promoted metallic Ni catalysts had high specific surface area and more NiO. The reaction results showed that the yttria promoter increased the CH4 conversion and the selectivity for H2 and CO.     

Size and support effects for CO oxidation on supported Pd catalysts

Science China Chemistry - Supporting Pd catalysts characterized significant different size distribution were obtained using PdCl2, [Pd(NH3)4](NO3)2 and Pd(acac)2 as precursors. High-resolution...     

Effects of calcination and support on supported manganese catalysts for the catalytic oxidation of toluene as a model of VOCs

The conventional impregnation method was used to prepare 15 wt% Mn-supported catalysts, which were applied to the catalytic oxidation of volatile organic compounds (VOCs; toluene, benzene, and o-xylene). The effects of calcination temperatures in the range of 500–900 °C and supports (γ-Al₂O₃, SiO₂, and TiO₂) on the property and performance of 15 wt% Mn-supported catalysts were investigated. Their physicochemical characteristics were analyzed by the BET, XRD, NH₃–TPD, H₂–TPR, and XPS. The calcination temperature greatly affected the crystalline structure and O1s _D (defect oxides)/O1s _L (lattice oxides) area ratio of the 15 wt% Mn/γ-Al₂O₃ (15 Mn/Al) catalyst. The order of the O1s _D/O1s _L area ratios of the 15 Mn/Al catalysts with respect to calcination temperature was 900 > 500 > 700 °C, which was in good agreement with that observed for the catalytic activity. In addition, the activity order of the 15 wt% Mn-supported catalysts with respect to the type of support was γ-Al₂O₃ > SiO₂ > TiO₂. The 15 wt% Mn/Al catalyst, which had a higher O1s _D/O1s _L area ratio, showed better activity than the 15 wt% Mn/SiO₂ (15 Mn/Si) and 15 wt% Mn/TiO₂ (15 Mn/Ti) catalysts. Defect oxides played a significant role in the catalytic oxidation of VOCs. The catalytic activity with respect to the type of VOC decreased in the order of benzene > toluene > o-xylene.     

Effect of electron irradiation on the catalytic properties of supported Pd catalysts

The effect of electron irradiation on the properties of the systems 1% Pd/C, 1% Pd/Al₂O₃, and 1% Pd/TiO₂ is studied in gas-phase and liquid-phase toluene hydrogenation. An increase in the irradiation dose to 120–900 Mrad increases the catalytic activity by a factor of 2–8 relative to that of the original system. XPS data for the Pd/C catalyst suggest that, after irradiation with high-energy electrons, the metal particles are stabilized on the surface of the carbon support, their degree of dispersion is increased, and their sintering is suppressed. These inferences are consistent with the observed changes in catalytic properties.     

Effect of support and loading on oxidation of methane over platinum catalysts

Catalytic combustion of methane was carried out using platinum catalysts supported on low-and high-surface area alumina (denoted respectively as LSA and HSA) and platinum supported on silica. Methane conversion was the highest for platinum supported on LSA alumina, smaller for Pt/HSA alumina and the smallest for Pt/silica. However, the 3 wt.% Pt/HSA catalyst was found to show the highest selectivity.     

Influence of the chemical nature of deposited metal ions on their catalytic properties in oxidation of methane by nitrous oxide

The catalytic properties of deposited metal ions in the reaction between methane and nitrous oxide were studied. On the basis of a previously proposed mechanism for the heterogeneous-catalytic reaction, an interpretation was given for the observed activity and selectivity series with respect to the formation of methanol, carbon monoxide and dioxide. The determining factor regulating the catalytic properties in this system is the bond energy of metal ions with the adsorbed oxygen anion radicals O.Translated from Teoreticheskaya i Éksperimental'naya Khimiya, Vol. 24, No. 4, pp. 455–461, July–August, 1988.The authors wish to express their gratitude to V. M. Lukyanchuk for providing samples of the catalysts, and to A. N. Korol' for his assistance in carrying out the chromotographic analysis.     

Insight into the structure of supported palladium catalysts during the total oxidation of methane

The combination of in situ X-ray absorption spectroscopy, X-ray diffraction and on-line catalytic data provided insight into the structure-performance relationship of a flame-made Pd/ZrO(2) catalyst during the total oxidation of methane: upon heating, a sudden reduction accompanied by sintering of the Pd-particles, leads to a significantly lower catalytic activity and a hysteresis during cooling down.     

载体性质对Pd催化剂加氢脱硫性能的影响

以Si O2、全硅MCM-41(Si-MCM-41)、通过机械混合Si-MCM-41与ZSM-5得到的Z-MCM-41-M以及通过在ZSM-5外部包覆MCM-41制备得到的Z-MCM-41四种材料为载体,制备了四种负载型Pd催化剂。采用XRD、HRTEM、N2吸附-脱附、NH3-TPD手段对Pd催化剂进行了表征;以二苯并噻吩(DBT)为模型化合物,在固定床反应器上对四种催化剂的加氢脱硫(HDS)活性、加氢路径选择性和加氢裂化活性进行了考察,研究了不同类型载体对Pd催化剂加氢脱硫性能的影响。结果表明,载体的性质会显著影响负载型Pd催化剂的加氢脱硫性能。载体的比表面积对负载型Pd催化剂加氢脱硫活性影响不大,但是HYD路径的选择性与载体的孔道结构有关;具有介孔孔道结构有利于加氢路径选择性的提高。酸性载体负载的Pd催化剂表现出较好加氢脱硫活性和加氢选择性,这与氢溢流有关。介孔材料的孔道结构与微孔沸石的酸性有机结合,所得到的Z-M CM-41复合材料是是潜在的贵金属Pd加氢脱硫催化剂优良载体,可有效提升其加氢脱硫活性。