镍基钙钛矿型催化剂的结构调控及其在甲烷干重整反应中的应用

钙钛矿材料在催化领域具有广泛的应用,其微观结构的调控对催化性能有显著的影响.我们采用柠檬酸配合法、溶胶凝胶法、燃烧法和浸渍法一系列不同的制备过程对镍基钙钛矿材料的结构进行调控,并将其应用于甲烷干重整反应,研究了制备方法对活性组分Ni的化学形态、Ni与基底的相互作用以及活性氧物种的调控,进而影响其催化活性和抗积碳能力.结果表明,燃烧法可以显著提高催化剂的结晶度,从而提高Ni与基底的相互作用以及表面氧物种的含量,使其具有较强的抗积碳能力.燃烧法合成的Ni基钙钛矿催化剂在CH4∶CO2=1.25∶1,800℃的条件下反应300 h后,积碳量仅为1.0%,而在同样条件下浸渍法合成的催化剂积碳量则高达14.6%.     

Selective Hydrogen Oxidation in the Presence of C3 Hydrocarbons Using Perovskite Oxygen Reservoirs

Perovskite‐type oxides, ABO₃, can be successfully applied as solid “oxygen reservoirs” in redox reactions such as selective hydrogen combustion. This reaction is part of a novel process for propane oxidative dehydrogenation, wherein the lattice oxygen of the perovskite is used to combust hydrogen selectively from the dehydrogenation mixture at 550 °C. This gives three key advantages: it shifts the dehydrogenation equilibrium to the side of the desired products, heat is generated, thus aiding the endothermic dehydrogenation, and it simplifies product separation (H₂O vs H₂). Furthermore, the process is safer since it uses the catalysts’ lattice oxygen instead of gaseous O₂. We screened fourteen perovskites for activity, selectivity and stability in selective hydrogen combustion. The catalytic properties depend strongly on the composition. Changing the B atom in a series of LaBO₃ perovskites shows that Mn and Co give a higher selectivity than Fe and Cr. Replacing some of the La atoms with Sr or Ca also affects the catalytic properties. Doping with Sr increases the selectivity of the LaFeO₃ perovskite, but yields a catalyst with low selectivity in the case of LaCrO₃. Conversely, doping LaCrO₃ with Ca increases the selectivity. The best results are achieved with Sr‐doped LaMnO₃, with selectivities of up to 93 % and activities of around 150 μmol O m^?2. This catalyst, La_0.9Sr_0.1MnO₃, shows excellent stability, even after 125 redox cycles at 550 °C (70 h on stream). Notably, the activity per unit surface area of the perovskite catalysts is higher than that of doped cerias, the current benchmark of solid oxygen reservoirs.     

Catalytic properties of La0.8Sr0.2Co0.5M0.5O3 (M Co, Ni, Cu) in methane combustion1

A set of perovskite-type catalysts of general formula La_0.8Sr_0.2Co_0.5M_0.5O₃ (M = Co, Ni, Cu) were prepared by alanine solution combustion method and used successfully for the methane combustion. The property of these materials were characterized by XRD, and TPR measurements. The effects of transition-metal ions on site B on structure and performance of the catalysts were studied. The result indicated that the structure and catalytic activities of the catalysts can remarkably affect by transition-metal ions on site B, the decrease of the electrons filled in d orbitals in the atom on site B is propitious to increase the catalytic activity for methane combustion, and the sequences of catalysts activities are La_0.8Sr_0.2CoO₃ τ; Ce_0.8Sr_0.2CoO₃ τ; Nd_0.8Sr_0.2CoO₃.     

BaTiO3 and PbTiO3 perovskite as catalysts for methane combustion

Unsupported and γ-Al₂O₃-supported Ba and Pb titanate catalysts were prepared, characterized and studied in the combustion of methane, as a test reaction for VOCs’ catalytic combustion. They present good catalytic activities, and after dispersion (5%) on γ-Al₂O₃ the specific activity of the supported perovskite phase increased 25 and 30 times, respectively, compared with the unsupported samples. PbTiO₃/γ-Al₂O₃ shows the best catalytic properties among the tested samples.     

Effect of stoichiometric ratio of organic fuel to oxidizer on performance of La0.8Sr0.2CoO3 catalysts for CH4 combustion

Perovskite-type La_0.8Sr_0.2CoO₃ mixed oxides were prepared by d,l-alanine solution combustion synthesis and used successfully in CH₄ combustion as catalysts. These samples were characterized by means of XRD, FTIR, BET, and H₂-TPR methods. The effects of stoichiometric ratio (φ) of organic fuel to oxidizer on the structure and catalytic activities of the catalysts were studied. The results indicate that all La_0.8Sr_0.2CoO₃ mixed oxides with different φ have perovskite structures. Their structures and catalytic activities vary along with the change of φ. The catalytic activity of La_0.8Sr_0.2CoO₃ mixed oxide with φ = 1.52 is the best among all the samples, whose T ₅₀ and T ₁₀₀ (the temperatures of methane conversions reaching 50 and 100%, respectively) are respectively 470 °C and 550 °C, which can be explained in terms of the smaller of average crystal size, higher specific surface area, bigger lattice distortion, lower activation energy, and higher mobility of chemically adsorbed oxygen on the surface and vacancy of the catalysts.     

Catalytic Combustion of Methane on Fe-TiO2 Catalysts Prepared by Sol-Gel Method

Two different series of titania-supported iron catalysts prepared by the sol-gel method have been characterised and tested in the combustion of methane at atmospheric pressure. In each series, the effect of metal loading (1, 5 and 10 wt%) and gelation pH (3 and 9) were studied. Characterisation data of calcined catalysts, carried out by specific area measurement, TPR, X-ray diffraction, XPS and EPR revealed no significant changes in metal dispersion. The catalytic activity of the solids were evaluated in the combustion of methane under stoichiometric mixture of CH₄/O₂ from 473 K up to the temperature required for total combustion. The best performance was shown by catalysts having 5 wt.%, which is ascribed to a balance of factors like the presence of a sufficient concentration of iron at the surface, achievement of relatively high dispersion state for iron and the presence of Fe⁺³ ions incorporated to the lattice of titania.     

Bifunctional catalysis of Mo/HZSM-5 in the dehydroaromatization of methane with CO/CO2 to benzene and naphthalene

The catalytic dehydrocondensation of methane to aromatics such as benzene and naphthalene was studied on the Mo carbide catalysts supported on micro- and mesoporous materials such as HZSM-5 (0.6 nm) and FSM-16 (2.7 nm). The Mo catalysts supported on H-ZSM-5 having appropriate micropores (0.6 nm size) and Si/Al ratios (20-70) exhibit higher yields (90-150 nmol/g-cat/s) and selectivities (higher than 74% on the carbon basis) in methane conversion to aromatic products such as benzene and naphthalene at 973 K and 1 atm, although they are drastically deactivated because of substantial coke formation. It was demonstrated that the CO/CO₂ addition to methane effectively improves the catalyst performance by keeping a higher methane conversion and selectivities of benzene formation in the prolonged time-on-stream. The oxygen derived from CO and CO₂ dissociation suppresses polycondensation of aromatic products and coke formation in the course of methane conversion. XAFS and TG/DTA/mass-spectrometric studies reveal that the zeolite-supported Mo oxide is endothermally converted under the action of methane around 955 K to nanosized particles of molybdenum carbide (Mo₂C) (Mo-C, coordination number = 1,R- 2.09 å; Mo-Mo, coordination number = 2.3–3.5;R = 2.98 å). The SEM pictures showed that the nanostructured Mo carbide particles are highly dispersed on and inside the HZSM-5 crystals. On the other hand, it was demonstrated by IR measurements of pyridine adsorption that the Mo/HZSM-5 catalysts having the optimum SiO₂/Al₂O₃ ratios around 40 show the maximum Brönsted acidity among the catalysts with the SiO₂/Al₂O₃ ratios of 20–1900. There is a close correlation between the activity of benzene formation in the methane aromatization and the Brönsted acidity of HZSM-5 due to the bifunctional catalysis.     

Development and testing of granular catalysts for combustors of regenerative gas turbine plants

Two types of granular catalysts for effective methane combustion in combustors of gas turbine plants (GTPs) were developed: (1) catalysts based on noble metals with a low Pd content (1–2 wt %), characterized by a low methane ignition temperature, and (2) catalysts based on manganese oxides and hexaaluminates, which have an increased thermal stability. The methane oxidation kinetics was investigated, and combustion in the catalyst chamber of the GTP was simulated. For optimizing the combustion technology, the following two-step process using a combined catalytic package is suggested. The inlet zone of the combustor is filled with a highly active Pd catalyst, which initiates methane oxidation and ensures that the temperature at the exit of this zone is the initial temperature of methane combustion. This takes place in the next zone, which is filled with an oxide catalyst tolerant to high temperatures. The pilot testing of the catalysts was carried out in a model catalytic combustor. The results are in satisfactory agreement with calculated data. Long-term tests indicate the high stability of the catalysts. The Pd catalyst was demonstrated to retain its high activity and to provide an ignition temperature of 240°C. The initial activity of the hexaaluminate-based catalysts remains unchanged after tests at 930°C. The use of a combined charge of the palladium (7–15%) and manganese (85–93%) catalysts in the model GTP combustor allows a high natural gas combustion efficiency to be achieved at a low level of hazardous emissions (NO _x , 0–1 ppm; CO, 1–3 ppm; hydrocarbons, 3–10 ppm).     

Atomic‐Scale Insights into Surface Lattice Oxygen Activation at the Spinel/Perovskite interface of Co3O4/La0.3Sr0.7CoO3

Surface lattice oxygen in transition‐metal oxides plays a vital role in catalytic processes. Mastering activation of surface lattice oxygen and identifying the activation mechanism are crucial for the development and design of advanced catalysts. A strategy is now developed to create a spinel Co₃O₄ /perovskite La_0.3Sr_0.7CoO₃ interface by in situ reconstruction of the surface Sr enrichment region in perovskite LSC to activate surface lattice oxygen. XAS and XPS confirm that the regulated chemical interface optimizes the hybridized orbital between Co 3d and O 2p and triggers more electrons in oxygen site of LSC transferred into lattice of Co₃O₄ , leading to more inactive O^2? transformed into active O^2?x. Furthermore, the activated Co₃O₄/LSC exhibits the best catalytic activities for CO oxidation, oxygen evolution, and oxygen reduction. This work would provide a fundamental understanding to explain the activation mechanism of surface oxygen sites.     

Relationship between oxygen species and activity/stability in heteroatom (Zr,Y)-doped cerium-based catalysts for catalytic decomposition of CH3SH

CeO₂, Ce_1–xZr_xO₂, and Ce_1–xY_xO_2–δ (x = 0.25, 0.50, 0.75, and 1.00) have been rapidly synthesized to estimate their catalytic behavior in decomposing CH₃SH. The role of oxygen vacancies, and the relationship between the oxygen species and catalytic properties of CeO₂ and Zr-doped and Y-doped ceria-based materials are investigated in detail. Combining the observed catalytic performance with the characterization results, it can be deemed that surface lattice oxygen plays a critical role in methanethiol catalytic conversion over cerium oxides. Ce_0.75Zr_0.25O₂ shows higher catalytic activity for CH₃SH decomposition due to the large amount of surface lattice oxygen, readily available oxygen species, and excellent redox properties. Ce_0.75Y_0.25O_2–δ displays better catalytic stability owing to the greater number of oxygen vacancies that would promote bulk lattice oxygen migration to the surface of the catalyst in order to replenish surface lattice oxygen. In addition, the results show that the difference in chemical valence between Ce and the heteroatoms would strongly influence the amount of surface lattice oxygen as well as the mobility of bulk-phase oxygen in these catalysts, thus affecting their activity and stability.     

Structure, microstructure, and size dependent catalytic properties of nanostructured ruthenium dioxide

Nanostructured powders of ruthenium dioxide RuO₂ were synthesized via a sol gel route involving acidic solutions with pH varying between 0.4 and 4.5. The RuO₂ nanopowders were characterized by X-ray diffraction, scanning and transmission electron microscopy (SEM and TEM). Rietveld refinement of mean crystal structure was performed on RuO₂ nanopowders and crystallized standard RuO₂ sample. Crystallite sizes measured from X-ray diffraction profiles and TEM analysis varied in the range of 4-10 nm, with a minimum of crystallite dimension for pH=1.5. A good agreement between crystallite sizes calculated from Williamson Hall approach of X-ray data and from direct TEM observations was obtained. The tetragonal crystal cell parameter (a) and cell volumes of nanostructured samples were characterized by values greater than the values of standard RuO₂ sample. In addition, the [Ru-O₆] oxygen octahedrons of rutile structure also depended on crystal size. Catalytic conversion of methane by these RuO₂ nanostructured catalysts was studied as a function of pH, catalytic interaction time, air methane composition, and catalysis temperature, by the way of Fourier transform infrared (FTIR) spectroscopy coupled to homemade catalytic cell. The catalytic efficiency defined as FTIR absorption band intensities I(CO₂) was maximum for sample prepared at pH=1.5, and mainly correlated to crystallite dimensions. No significant catalytic effect was observed from sintered RuO₂ samples.     

Mn离子掺杂对K2MnxAl12-xO19-δ催化剂结构及其甲烷燃烧性能的影响

采用反相微乳液-金属醇盐水解法制备了K作为镜面阳离子,锰离子作为活性组分的一系列六铝酸盐催化剂K₂Mn_xAl_12-xO_19-δ(x=0、1.0、1.5、2.0、2.5、3.0) 。通过X射线衍射、差热 热重和程序升温还原等实验技术及甲烷燃烧,对催化剂的结构和性质进行了考察。主要考察了不同Mn离子的掺杂量对催化剂结构及对甲烷催化燃烧活性的影响。结果表明,K作为镜面阳离子,不但可以形成完整的六铝酸盐,而且所制备的催化剂具有较高的催化活性。不同的Mn离子掺杂对于催化剂的特性有较大的影响。当Mn的掺杂量在六铝酸盐K₂Mn_xAl_12-xO_19-δ结构式中为x=1时,制备的催化剂K₂MnAl₁₁O_19-δ具有较高的催化活性,起燃温度Tl0%为458℃,至676℃甲烷完全转化,Mn掺杂量增多导致晶体结构中出现钙钛矿杂质。     

Tap study of the impact of the oxidation state of Pt/PrCeZrO and Pt/GdCeZrO catalysts on their reactivity in the partial/deep oxidation of methane

The temporal analysis of products (TAP) technique coupled with the oxygen TPD was used to elucidate the effects of the Pt-supported fluorite-like doped ceria–zirconia oxide chemical composition and the type of pretreatment on their oxygen bonding strength, mobility, and reactivity as related to catalytic properties in the partial oxidation of methane into synthesis gas. A rapid evolution of hydrogen under CH₄ pulse observed for oxidized catalysts agrees with the direct route of the methane selective oxidation into syngas. This route is favored by the Pt-support interaction and a moderate bonding strength of surface oxygen species along with a high lattice oxygen mobility.     

Samarium Based High Surface Area Perovskite Type Oxides SmFe1-XAlXO3 (X=0.00, 0.50, 0.95). Part II, Catalytic Combustion of CH4

The catalytic combustion of methane with stoichiometric amounts of oxygen to CO₂ and H₂O has been studied over samarium based high surface area perovskite type oxides SmFe_1-xAl_xO₃ (x=0.00, 0.50 0.95) prepared via a new sol-gel method. A comparison to other lanthanum perovskites prepared by the ceramic method shows higher catalytic activity for SmFeO₃ and SmFe_0.5Al_0.5O₃ samples.     

Syngas production from methane over CeO2-Fe2O3 mixed oxides using a chemical-looping method

A series of mixed oxides Ce_{1 ? x} Fe _x O₂ was prepared by a hydrothermal method. XRD and Raman spectra were measured to study the structure of the prepared materials. The temperature-programmed reduction was undertaken to estimate reducibility of the oxides. Syngas generation from methane using these materials as oxygen carriers/catalysts via a chemical-looping procedure was investigated in detail. This procedure includes catalytic oxidation and decomposition of methane to produce H₂-rich gas at the first step followed by the production of the CO-rich gas by oxidizing the carbon deposited on deactivated catalysts. The results showed that all iron ions were incorporated into the ceria lattice with the formation of oxygen vacancies in the Ce_0.9Fe_0.1O₂ sample, while isolated Fe₂O₃ particles were distributed on the surface of the Ce_0.8Fe_0.2O₂ sample. TPR measurements and the analysis of the two-step chemical-looping reactions indicated a strong interaction between the Ce and Fe species which accounts for an increased activity of the mixed oxides in the syngas generation compared to that of individual oxides. Among the several samples, the Ce_0.8Fe_0.2O₂ catalyst showed the highest activity for methane partial oxidation due to the synergetic effects caused by the interaction of surface iron entities and Ce-Fe solid solution. In addition, selective oxidation of carbon by oxygen to CO can also be found over this material since gaseous products are formed at the carbon oxidation step with the selectivity to CO reaching 91.2%. Evidence is presented that syngas can be feasibly produced from methane with high selectivity via the chemical-looping procedure over the CeO₂-Fe₂O₃ mixed oxides.     

Design of coke-free methane dry reforming catalysts by molecular tuning of nitrogen-rich combustion precursors

The valorization of methane and carbon dioxide is a promising solution for mitigating global warming. The dry reforming of methane (DRM) is capable of concomitant conversion of these greenhouse gases into starting materials for production of synthetic fuels, promoting a carbon neutral avenue for fuel production. The development of efficient, stable, and economic catalysts presents a challenge owing to the comparatively rapid deactivation of DRM catalysts under reaction conditions. Here, Ni/La₂O₃ DRM catalysts are prepared by combustion synthesis of Ni and La complexes of nitrogen-rich precursors. We expound the relationship between structures of the combustion precursors, the thermochemistry of their combustion, the structures of the resultant Ni/La₂O₃ catalysts, and their performance under DRM conditions. We show that the best catalyst is derived from energetic precursor which has the sharpest exotherm and rapidly releases the largest amounts of nitrogen gas. These properties give rise to the crystallization of the Ni/La₂O₃ catalyst with high Ni dispersion and strong metal-support interactions. This work can act as starting point to expand the link between the chemistry of combustion precursors and the resulting catalyst properties, eventually realizing the rational design of high-performance catalysts prepared by combustion synthesis through tailoring the chemistry and structure of the nitrogen-rich precursors.     

负载型Pd/SnO2催化剂低温催化甲烷燃烧

天然气储量巨大,被广泛应用于发电和工业窑炉等.甲烷作为天然气中最主要的成分,是氢碳比最高的碳氢化合物,其温室效应显著.因此,不完全燃烧所引起的CH4排放,不仅导致能源浪费,同时也可造成环境污染.与传统火焰燃烧相比,CH4催化燃烧具有更高的燃烧效率,并可显著地减少大气污染物(CO,NOx和未完全燃烧的烃类)的排放.贵金属Pd催化剂对CH4催化燃烧表现出优异的催化性能,其中Pd颗粒的尺寸、Pd的化学状态、载体性质及其与Pd之间的相互作用等对其活性有显著影响.本文以不同温度(600,800,1000和1200℃)焙烧所得SnO2为载体,通过等体积浸渍法制备了Pd/SnO2催化剂,研究了SnO2焙烧温度对CH4催化燃烧性能的影响.结果表明,所制备的SnO2均为锐钛矿结构,并且随着SnO2焙烧温度的升高,晶型愈加完美,晶粒尺寸显著增大.催化剂中引入的Pd以高分散形式存在,CH4催化燃烧反应活性随着载体SnO2焙烧温度的升高而显著提高,其中Pd/SnO2(1200)表现出最高的CH4燃烧活性,起燃温度和最低全转化温度分别为265和390℃.在反应温度为300℃时,Pd/SnO2(1200)上甲烷的反应速率是Pd/SnO2(600)的36倍.XPS等结果表明,随着SnO2焙烧温度的升高,Pd的化学状态也有所差异:对于低温焙烧的SnO2(<800℃),Pd以Pd4+的形式进入到SnO2晶格内;随着焙烧温度的升高(>1000℃),Pd以Pd2+物种的形式存在于载体表面.结合活性评价结果推测,Pd的化学状态可能并非是影响催化剂活性的最关键因素.TEM等结果表明,Pd/SnO2(1000)上PdO的(101)晶面与载体SnO2的(101)晶面相近,分别为0.2641 nm和0.2638 nm.O2-TPD和CH4-TPR结果表明,Pd/SnO2(1200)催化剂上单位Pd原子上O2的脱附量是Pd/SnO2(600)的3倍,单位Pd原子上CH4的消耗量比催化剂Pd/SnO2(600)高出45%.因此,PdO和SnO2在构型上存在的晶面匹配可提高催化剂对O2的活化能力.综上所述,SnO2和贵金属之间的晶格匹配有利于氧在Pd-SnO2界面的活化,同时载体SnO2中的晶格氧亦可以通过"氧反溢流机理"补充到表面PdO/Pd上,从而增强催化剂对O2的吸附和活化能力,并提高CH4催化燃烧反应性能.升高SnO2的焙烧温度可强化SnO2和贵金属之间的晶格匹配,从而使催化剂活性随着SnO2焙烧温度升高而增大.     

THE ROLE OF LATTICE AND GASEOUS OXYGEN ON THE OXIDATIVE COUPLING OF METHANE STUDIED BY A PULSE REACTION TECHNIQUE

A comparative study of the role of lattice and gaseous oxygen in theoxidative coupling of methane over Na~ /Cao and Ca_xSr_(1-x)TiO_3 perovskiteoxide catalysts was performed by using a pulse reaction technique with CH_4,O_2 and mixtures of CH_4and O_2.It was found that there is an oxygen species onthe Surface of Cao which is active only for the total oxidation of methane at thereaction temperature.These oxygen species.once reacted with methane andconsumed,can be regenerated by the adsorption of oxygen molecules from thegas phase or by the migration of the lattice oxysen from the bulk onto thesurface.In contrast,no such oxygen species and no reaction can be detected bymethane pulsed over Ca_xSr_(1-x)TiO_3perovskite oxide catalysts.Na~ can heavilysuppress the non-selective oxygen species on the surface,and When 5mol%Na~ was incorporated onto the surface of Cao,the sample showed no reactivityto methane.When oxygen exists in the gas phase,or the pulse containsmethane and oxygen,the reaction over(Cao is mai     

The effect of active oxygen species in nano-ZnCr2O4 spinel oxides for methane catalytic combustion

The nano-ZnCr₂O₄ spinel oxides was synthesized by a ethylene glycol mediated solvothermal method. Catalytic combustion of methane test showed that an excellent activity over nano-ZnCr₂O₄ with T_10% = 300 °C and T_90% = 400 °C. The results of X-ray diffraction (XRD), scanning electron microscopy (SEM), N₂ adsorption-desorption measurements (BET) indicated that a uniform nano-ZnCr₂O₄ spinel oxides particles with the high surface area (96.2 m²g⁻¹) was successfully synthesized. Oxygen temperature programmed desorption (O₂-TPD) profile revealed there were two obvious desorption of oxygen species from nano-ZnCr₂O₄ in the range of 300–400 °C and 500–700 °C. It was clear that the desorption temperature range of the first oxygen species coincided with the methane catalytic combustion temperature. X-ray photoelectron spectroscopy (XPS) analysis exhibited that Cr⁶⁺ was present in the lattice of ZnCr₂O₄ apart from Cr³⁺. High valence cations of chromium in crystal lattice probable caused the presence of interstitial oxygen species in the structure to maintain the electroneutrality. Additionally, Raman spectra proved that there is the interstitial oxygen species in the crystal lattice of ZnCr₂O₄. Therefore, the excellent catalytic activity for methane combustion was contributed to the flexible interstitial oxygen in the ZnCr₂O₄.     

铈基复合氧化物催化碳烟燃烧的性能及其H2-TPR研究

采用溶胶-凝胶法或浸渍法制备了不同金属离子掺杂的铈基复合氧化物催化剂,并采用热重法考察其催化碳烟燃烧的活性,借助H₂-TPR(程序升温还原)手段探讨了催化剂氧化还原性对碳烟燃烧性能的影响. 结果表明,过渡金属的掺杂促使催化剂在低温下提供更多的表面氧和晶格氧,显著降低了碳烟的氧化温度,催化剂于200~400℃释放的活性氧数量对于碳烟燃烧性能提高至关重要; 而结构性助剂金属、碱金属或碱土金属的掺入可提高中温活性氧数量,虽然对碳烟起燃温度无明显改善,但加快了碳烟的燃烧速率.