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Tailor-made Al-containing mesostructured catalysts for BTXs production from biomass resources 从生物质资源生产BTXs的定制含al介结构催化剂
IF 5.3 2区 化学 Q1 CHEMISTRY, APPLIED Pub Date : 2025-09-10 DOI: 10.1016/j.cattod.2025.115562
Gabriel O. Ferrero , Verónica R. Elías , Madalina G. Idriceanu , Griselda A. Eimer , Marcelo E. Domine
Benzene, toluene, and xylene (BTXs) are the major commodity chemicals serving a wide range of industries with large global economic impact and are currently obtained exclusively from petroleum feedstock. Alternative renewable sources from biomass are raised as a solution to satisfy the pressing needs for a fully sustainable bio-commodities industry. For this reason, the chemistry of materials has focused on the synthesis of catalysts that can transform biomass into renewable chemical compounds of interest. In this work, the SBA-15 material was modified with Al to incorporate a specific Br/Le acid sites ratio to make a low-cost tailor-made catalyst for the aromatization reaction of furanic dienes and dienophiles from renewable biomass sources. In order to correlate the catalytic activity of materials with their structure and nature, the solids were characterized by several techniques such as XRD, TEM, ICP, N2 physisorption and FT-IR of adsorbed pyridine. The goal of this work was to maximize the production of p-xylene (PX) by fine-tuning the Al content in SBA-15 and optimizing the reaction conditions. The presence of Lewis (Le) and Brønsted (Br) acid sites in Al-SBA-15 materials with different Al contents was determined and the catalysts were evaluated in the aromatic reaction of 2,5-dimethylfuran with ethylene. The optimal combination of Le sites, to produce the first cycloaddition, and Br sites, for subsequent dehydration, was achieved with the Al(1.28)SBA-15 catalyst. After optimization of main reaction parameters (i.e., pressure, temperature and reagents and catalyst concentrations), a 42 % yield of p-xylene was achieved and maintained even after three consecutive re-cycles of solid catalyst. Finally, the possible extended scope of this catalytic system for producing toluene and trimethylbenzene from the corresponding starting reactants was also evaluated.
苯、甲苯和二甲苯(BTXs)是主要的商品化学品,服务于广泛的行业,对全球经济产生重大影响,目前仅从石油原料中获得。从生物质的替代可再生资源被提出作为一个解决方案,以满足一个完全可持续的生物商品工业的迫切需要。由于这个原因,材料的化学集中在催化剂的合成上,这些催化剂可以将生物质转化为可再生的化合物。在这项工作中,用Al修饰SBA-15材料,使其加入特定的Br/Le酸位比,以制造一种低成本的定制催化剂,用于可再生生物质来源的呋喃二烯和亲二烯的芳构化反应。为了将材料的催化活性与其结构和性质联系起来,采用XRD、TEM、ICP、N2物理吸附和FT-IR等技术对固体进行了表征。通过调整SBA-15中Al的含量和优化反应条件,实现对二甲苯(PX)产量的最大化。测定了不同Al含量的Al- sba -15材料中Lewis (Le)和Brønsted (Br)酸位的存在,并对2,5-二甲基呋喃与乙烯的芳香族反应的催化剂进行了评价。Al(1.28)SBA-15催化剂的最佳组合是产生第一个环加成的Le位点和随后脱水的Br位点。在优化了主要反应参数(即压力、温度、试剂和催化剂浓度)后,对二甲苯的收率达到了42% %,即使在连续三次循环使用固体催化剂后也能保持。最后,对该催化体系从相应的起始反应物生产甲苯和三甲苯的可能扩展范围进行了评价。
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引用次数: 0
Effect of A-site substitution for Pt supported La0.8A0.2FeO3 perovskite for aqueous-phase aerobic oxidation of ethylene glycol to glycolic acid using O2 Pt负载La0.8A0.2FeO3钙钛矿a位取代对乙二醇水相氧氧化制乙醇酸的影响
IF 5.3 2区 化学 Q1 CHEMISTRY, APPLIED Pub Date : 2025-09-08 DOI: 10.1016/j.cattod.2025.115548
Seungdon Kwon, Nagyeong Kim, Hyeonji Yeom, Hanbit Jang, Kyungsu Na
Selective oxidation of biomass-derived polyols into value-added chemicals is a promising strategy for sustainable chemical production. Among these, ethylene glycol (EG) serves as a versatile platform molecule due to its simple structure and dual hydroxyl functionality. In this study, a series of perovskite-type oxides with the general formular of La0.8A0.2FeO3 (A = Mg, Ca, Sr, Ba) was synthesized and impregnated with 1 wt% Pt to investigate structure–activity relationships in the aerobic oxidation of EG to glycolic acid (GA). Physicochemical characterizations using XPS, H2-TPR, O2-TPO, and ethanol chemisorption revealed that A-site substitution significantly affected Pt dispersion, oxidation state, and oxygen vacancy concentration. Notably, Sr-substituted catalysts exhibited high EG conversion and GA selectivity under both pressurized and ambient conditions, which was attributed to the presence of metallic Pt0, abundant oxygen vacancies, facile oxygen activation, and enhanced interaction with –OH containing reactants. These findings propose the critical role of A-site engineering in tailoring perovskite-supported Pt catalysts and provide valuable insights into the rational design of heterogeneous oxidation catalysts for polyol upgrading.
生物质多元醇选择性氧化成增值化学品是一种有前途的可持续化学品生产策略。其中乙二醇(EG)结构简单,具有双羟基功能,是一种多功能平台分子。本研究合成了一系列通式为La0.8A0.2FeO3 (a = Mg, Ca, Sr, Ba)的钙钛矿型氧化物,并以1 wt% Pt浸渍,研究了EG有氧氧化制乙醇酸(GA)的构活性关系。利用XPS、H2-TPR、O2-TPO和乙醇化学吸附进行的理化表征表明,a位取代显著影响了Pt的分散性、氧化态和氧空位浓度。值得注意的是,sr取代的催化剂在加压和环境条件下都表现出较高的EG转化率和GA选择性,这是由于金属Pt0的存在、丰富的氧空位、容易的氧活化以及与含-OH的反应物的相互作用增强。这些发现提出了a位点工程在定制钙钛矿负载Pt催化剂中的关键作用,并为多元醇升级的多相氧化催化剂的合理设计提供了有价值的见解。
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引用次数: 0
Bias-controlled catalytic selectivity via metal–semiconductor schottky nanodiodes 偏压控制的金属半导体肖特基纳米二极管催化选择性
IF 5.3 2区 化学 Q1 CHEMISTRY, APPLIED Pub Date : 2025-09-08 DOI: 10.1016/j.cattod.2025.115559
Yeji Yoon , Kyoungjae Song , Jeong Young Park , Si Woo Lee
The selective oxidation of methanol serves as a model reaction for probing the fundamental principles of heterogeneous catalysis, where control over product distribution remains a central challenge. Here, we report a catalytic nanodiode platform based on a Pt/n-type TiO2 Schottky junction that enables active modulation of reaction selectivity via applied electrical bias. By systematically varying the bias direction and magnitude during methanol oxidation under oxygen-rich conditions, we demonstrate that accumulation of negative charge on the Pt surface under reverse bias leads to a consistent decrease in methyl formate selectivity, indicating a shift toward full oxidation pathways. Electrical measurements confirm the suppression of current under reverse bias, supporting the formation of an electron-rich catalytic interface. These results provide direct experimental evidence that external control of interfacial charge can influence reaction selectivity, establishing catalytic nanodiodes as a promising platform for electronically tunable heterogeneous catalysis.
甲醇的选择性氧化作为一种模型反应,用于探索多相催化的基本原理,其中对产品分布的控制仍然是一个中心挑战。在这里,我们报道了一个基于Pt/n型TiO2肖特基结的催化纳米二极管平台,该平台可以通过施加电偏置来主动调节反应选择性。通过系统地改变富氧条件下甲醇氧化过程中的偏压方向和大小,我们证明了在反向偏压下Pt表面负电荷的积累导致甲酸甲酯选择性的持续下降,表明向全氧化途径的转变。电测量证实了反向偏压下电流的抑制,支持富电子催化界面的形成。这些结果为界面电荷的外部控制可以影响反应选择性提供了直接的实验证据,从而建立了催化纳米二极管作为电子可调多相催化的有前途的平台。
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引用次数: 0
Optimizing structural properties of zeolite support to enhance branched isomer yield in gasoline range in Fischer-Tropsch synthesis reaction 优化沸石载体的结构性能以提高费托合成反应中汽油范围支链异构体的产率
IF 5.3 2区 化学 Q1 CHEMISTRY, APPLIED Pub Date : 2025-09-06 DOI: 10.1016/j.cattod.2025.115549
Jeong-Chul Kim , Daeyoung Bae , Subin Son , Junsang Lee , Shin Hyuk Kim , Doyeon Lee , Joo-Il Park , Kyung Duk Kim , Kanghee Cho
In Fischer-Tropsch synthesis reaction using cobalt nano-catalyst, the role of zeolite nanosponge containing Brønsted-Lowry acid sites at mesopore walls was revealed to be important to enhance the yield of isomer hydrocarbon in gasoline range. The acid sites on the external surface where the product shows facile diffusion facilitate isomerization action and cracking. By performing systematic investigation, we confirmed that the yield of branched isomers in gasoline range (i-C5–11) gradually increases with increasing the external surface area of the MFI zeolite. This result indicates that the large external surface area is good for high dispersion of cobalt nanoparticles and high concentration of the external acid sites, consequently advantageous to form i-C5–11. Meanwhile, the i-C5–11 selectivity is varied significantly with respect to the acid concentration; the optimal Si/Al ratio, which determines the concentration of Brønsted-Lowry acid sites, was found to be 50, yielding a maximum i-C5–11 fraction of 25.6 %. Consequently, the zeolite MFI nanosponge synthesized using di-quaternary ammonium surfactant, with Si/Al = 50 is the most suitable supporting material for Co nanoparticles in Fischer-Tropsch synthesis reaction for the purpose producing high-value gasoline fuels.
在采用钴纳米催化剂的费托合成反应中,发现在介孔壁上含有Brønsted-Lowry酸位点的沸石纳米海绵对提高汽油范围内异构体烃的产率有重要作用。产品外表面的酸位易于扩散,有利于异构化作用和裂解。通过系统的研究,我们证实了随着MFI分子筛外表面积的增加,汽油范围(i-C5-11)支化异构体的产率逐渐增加。该结果表明,大的外表面积有利于钴纳米粒子的高分散和高浓度的外酸位,从而有利于形成i-C5-11。同时,i-C5-11的选择性随酸浓度变化显著;决定Brønsted-Lowry酸位浓度的最佳Si/Al比为50,最大i-C5-11分数为25.6 %。因此,采用双季铵表面活性剂合成的Si/Al = 50的沸石MFI纳米海绵是Co纳米颗粒在费托合成反应中制备高价值汽油燃料的最合适载体材料。
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引用次数: 0
Activating properties of residual coke after incomplete oxidative regeneration of ferrierite used in skeletal 1-butene isomerization 骨架1-丁烯异构化用铁素体不完全氧化再生后残焦的活化性能
IF 5.3 2区 化学 Q1 CHEMISTRY, APPLIED Pub Date : 2025-09-06 DOI: 10.1016/j.cattod.2025.115545
Karoline L. Hebisch , Pawel A. Chmielniak , Violet A. Cutler , Carsten Sievers
This study demonstrates that partial oxidative regeneration of spent ferrierite zeolite (H-FER / H-ZSM-35) used in skeletal 1-butene isomerization effectively restores catalyst activity, while residual carbonaceous deposits significantly reduce the catalyst startup time. By employing catalyst characterization techniques such as X-ray powder diffraction (XRD), X-ray photoelectron spectroscopy (XPS), operando UV-Vis spectroscopy, and density functional theory (DFT) calculations, the findings reveal that oxidative regeneration of spent H-FER at 500 °C removes external polycyclic aromatic carbonaceous deposits that block pore mouths. However, this process also promotes the migration of internal carbonaceous deposits to the external surfaces, where they condense into polycyclic aromatic structures. These structures obstruct pore access until the total carbonaceous deposits are reduced to below ∼1 wt%. Beyond this threshold, further oxidative removal of coke is not beneficial, as the residual carbonaceous deposits promote catalyst startup in subsequent cycles and inhibit strong acid sites that contribute to side product formation. In addition to offering a practical strategy for accelerating catalyst startup, this partial regeneration approach provides valuable insights into the nature of catalytically active species at the pore mouth. The results suggest that residual carbonaceous fragments can enhance catalyst activation speed by up to threefold. Utilizing these residual deposits as both coke precursors and selective poisons represents a promising method for efficient partial oxidative regeneration of catalysts affected by coke deposition.
本研究表明,用于骨架1-丁烯异构化的废铁沸石(H-FER / H-ZSM-35)的部分氧化再生有效地恢复了催化剂的活性,而残余的碳质沉积物显著缩短了催化剂的启动时间。通过x射线粉末衍射(XRD)、x射线光电子能谱(XPS)、operando UV-Vis光谱和密度泛函理论(DFT)计算等催化剂表征技术,研究结果表明,在500 °C下,废H-FER的氧化再生可以去除堵塞孔口的外部多环芳香族碳质沉积物。然而,这一过程也促进了内部碳质沉积物向外表面的迁移,在那里它们凝结成多环芳香族结构。这些结构阻碍孔隙进入,直到总碳质沉积物减少到1 wt%以下。超过这个阈值,进一步氧化去除焦炭是无益的,因为残余的碳质沉积物促进催化剂在随后的循环中启动,并抑制有助于副产物形成的强酸位点。除了提供加速催化剂启动的实用策略外,这种部分再生方法还提供了对孔口催化活性物质性质的有价值的见解。结果表明,残余碳质碎片可使催化剂的活化速度提高三倍。利用这些残余沉积物作为焦炭前体和选择性毒物对焦炭沉积影响的催化剂进行部分氧化再生是一种很有前途的方法。
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引用次数: 0
Stimuli-responsive Pickering emulsions: From interfacial design to catalytic opportunities 刺激反应皮克林乳液:从界面设计到催化机会
IF 5.3 2区 化学 Q1 CHEMISTRY, APPLIED Pub Date : 2025-09-05 DOI: 10.1016/j.cattod.2025.115534
Pavel Svec, Niccolo Lusiani, Ondrej Sedlacek
Stimuli-responsive Pickering emulsions stabilized by solid nanoparticles with properties modulated by external triggers represent a versatile platform for sustainable biphasic catalysis. Unlike conventional surfactant-based systems, these emulsions offer robust, surfactant-free interfaces with enhanced control over emulsification, demulsification, and even phase inversion, enabled by stimuli such as pH, temperature, light, redox conditions, or magnetic fields. This perspective article provides a concise overview of recent advances in the design of such "smart emulsions "with a focus on functional polymeric and hybrid nanoparticle stabilizers engineered for responsiveness. These systems not only facilitate on-demand catalyst recovery and product separation but also enhance catalytic efficiency through increased interfacial area and selective localization of the catalyst. While addressing current challenges in their scalability and long-term reusability, we highlight their applications in interfacial catalysis, biocatalysis, and environmental remediation. By integrating major advances in colloid science with responsive materials, these systems emerge as a promising avenue toward sustainable chemical processing.
由固体纳米颗粒稳定的刺激响应皮克林乳液具有外部触发器调节的特性,代表了可持续双相催化的多功能平台。与传统的基于表面活性剂的体系不同,这些乳液提供了强大的、无表面活性剂的界面,通过pH、温度、光、氧化还原条件或磁场等刺激,增强了对乳化、破乳甚至相转化的控制。这篇前瞻性文章简要概述了这种“智能乳剂”设计的最新进展,重点是功能性聚合物和杂化纳米颗粒稳定剂的响应性设计。这些系统不仅促进了按需催化剂回收和产物分离,而且通过增加界面面积和催化剂的选择性定位提高了催化效率。在解决当前在可扩展性和长期可重用性方面的挑战的同时,我们重点介绍了它们在界面催化、生物催化和环境修复方面的应用。通过将胶体科学的主要进展与反应材料相结合,这些系统成为可持续化学处理的有希望的途径。
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引用次数: 0
Methane partial oxidation over Rh/ZSM-5 catalysts in a high-pressure continuous flow reactor 高压连续流反应器中Rh/ZSM-5催化剂上甲烷部分氧化
IF 5.3 2区 化学 Q1 CHEMISTRY, APPLIED Pub Date : 2025-09-05 DOI: 10.1016/j.cattod.2025.115558
A.K.M. Kazi Aurnob , Mark B.F. Berko , Jialin Yu , David Chadwick , Kang Li , Richard J. Lewis , Thomas Davies , Stuart H. Taylor , Graham J. Hutchings , James J. Spivey , Kunlun Ding
Zeolite-supported Rh catalysts have been shown to be highly effective in catalyzing the oxidative carbonylation of methane to produce acetic acid. However, most of the research reported so far employed high-pressure batch reactors with long residence times. Continuous flow reactors have been seldomly used, with the majority of earlier works focused on ambient pressure studies. In this contribution, we constructed a high-pressure continuous flow reactor with steam cofeeding to bridge the knowledge gap that exists between these two distinct approaches. The production of CH3OH, CH3COOH, and other oxygenates, using a reactant mixture of CH4, CO, O2, and steam, was observed over Rh/ZSM-5 catalysts. The primary oxygenates, CH3OH and CH3COOH, reached productivities of 45 and 102 µmol/(gcat.•h), respectively. The influence of space velocity, Rh loading, Si/Al ratio of the zeolite support, and CO partial pressure were investigated.
沸石负载的Rh催化剂在催化甲烷氧化羰基化制乙酸方面具有很高的效率。然而,目前报道的研究大多采用停留时间较长的高压间歇反应器。连续流反应器很少被使用,早期的大部分工作都集中在环境压力研究上。在这篇文章中,我们构建了一个高压连续流反应器与蒸汽共馈,以弥合这两种不同方法之间存在的知识差距。在Rh/ZSM-5催化剂上,用CH4、CO、O2和蒸汽的反应物混合物,观察了CH3OH、CH3COOH和其他含氧物的生成。初级氧合物CH3OH和CH3COOH的产率分别为45µmol/(gcat)和102µmol/(gcat)。•h),分别。考察了空速、Rh负载、沸石载体硅铝比、CO分压等因素的影响。
{"title":"Methane partial oxidation over Rh/ZSM-5 catalysts in a high-pressure continuous flow reactor","authors":"A.K.M. Kazi Aurnob ,&nbsp;Mark B.F. Berko ,&nbsp;Jialin Yu ,&nbsp;David Chadwick ,&nbsp;Kang Li ,&nbsp;Richard J. Lewis ,&nbsp;Thomas Davies ,&nbsp;Stuart H. Taylor ,&nbsp;Graham J. Hutchings ,&nbsp;James J. Spivey ,&nbsp;Kunlun Ding","doi":"10.1016/j.cattod.2025.115558","DOIUrl":"10.1016/j.cattod.2025.115558","url":null,"abstract":"<div><div>Zeolite-supported Rh catalysts have been shown to be highly effective in catalyzing the oxidative carbonylation of methane to produce acetic acid. However, most of the research reported so far employed high-pressure batch reactors with long residence times. Continuous flow reactors have been seldomly used, with the majority of earlier works focused on ambient pressure studies. In this contribution, we constructed a high-pressure continuous flow reactor with steam cofeeding to bridge the knowledge gap that exists between these two distinct approaches. The production of CH<sub>3</sub>OH, CH<sub>3</sub>COOH, and other oxygenates, using a reactant mixture of CH<sub>4</sub>, CO, O<sub>2</sub>, and steam, was observed over Rh/ZSM-5 catalysts. The primary oxygenates, CH<sub>3</sub>OH and CH<sub>3</sub>COOH, reached productivities of 45 and 102 µmol/(g<sub>cat.</sub>•h), respectively. The influence of space velocity, Rh loading, Si/Al ratio of the zeolite support, and CO partial pressure were investigated.</div></div>","PeriodicalId":264,"journal":{"name":"Catalysis Today","volume":"462 ","pages":"Article 115558"},"PeriodicalIF":5.3,"publicationDate":"2025-09-05","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145020271","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"化学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
LaFe1-xMnxO3−δ as effective redox catalysts for CO2 splitting and methane partial oxidation in a cyclic redox scheme LaFe1-xMnxO3−δ作为循环氧化还原方案中CO2裂解和甲烷部分氧化的有效氧化还原催化剂
IF 5.3 2区 化学 Q1 CHEMISTRY, APPLIED Pub Date : 2025-09-04 DOI: 10.1016/j.cattod.2025.115546
Sherafghan Iftikhar , William Martin , Andrew Pedersen, Sam Portillo, Junchen Liu, Fanxing Li
The current study reports LaFe1-xMnxO3−δ redox catalysts (RCs) for CO2-splitting and methane partial oxidation (CH4-POx) in a cyclic redox scheme. Lanthanum (La) was chosen as the A-site cation whereas iron (Fe) and manganese (Mn) were chosen as the B-site cations, respectively. La, Fe, and Mn were incorporated into the perovskite structure (LaFe1-xMnxO3−δ) at various Fe/Mn ratios to tailor the equilibrium oxygen partial pressures for CO2-splitting and methane partial oxidation. Compared to the standalone redox pairs of Fe and Mn (i.e., Fe2O3/Fe3O4, Fe3O4/FeO, and Mn2O3/Mn3O4) which, from a thermodynamic standpoint, favor the complete combustion of CH4, the perovskite structured redox catalysts (RCs, i.e., LaFe1-xMnxO3−δ) favored the selective oxidation of CH4 to syngas. In addition, impregnating the RCs with 1 wt% ruthenium (Ru) led to a significant improvement in their redox kinetics without affecting their redox thermodynamics. The Ru-impregnated, perovskite structured RCs (i.e., LaFeO3, LaFe0.625Mn0.375O3, and LaFe0.5Mn0.5O3 ) exhibited excellent redox performance in terms of the syngas yield (92 – 100 %) and CO2 conversion (95–98 %). Long-term redox testing over Ru-impregnated LaFeO3 and LaFe0.5Mn0.5O3 demonstrated relatively stable performance for 100 redox cycles whereas activity loss was observed for LaFe0.625Mn0.375O3, LaFe0.375Mn0.625O3, and LaMnO3 respectively. Among RCs containing both Mn and Fe, LaFe0.5Mn0.5O3 exhibited the best performance, maintaining satisfactory activity over 100 cycles and higher oxygen capacity. XRD and XPS analysis suggest that the ability to regenerate the perovskite phase under a CO2 environment and a near surface A:B site cation ratio close to the perovskite stoichiometry would likely correspond to more stable performance. Additionally, the inclusion of Mn on the B-site enhances the coke resistance of the redox catalyst when compared to undoped LaFeO3.
本研究报道了LaFe1-xMnxO3−δ氧化还原催化剂(RCs)在循环氧化还原方案中用于co2裂解和甲烷部分氧化(CH4-POx)。选择镧(La)作为a位阳离子,选择铁(Fe)和锰(Mn)分别作为b位阳离子。将La, Fe和Mn以不同的Fe/Mn比掺入钙钛矿结构(LaFe1-xMnxO3−δ)中,以调整二氧化碳分裂和甲烷部分氧化的平衡氧分压。从热力学角度来看,Fe和Mn的独立氧化还原对(即Fe2O3/Fe3O4, Fe3O4/FeO和Mn2O3/Mn3O4)有利于CH4的完全燃烧,而钙钛矿结构的氧化还原催化剂(即LaFe1-xMnxO3−δ)有利于CH4的选择性氧化生成合成气。此外,用1 wt%钌(Ru)浸渍RCs,在不影响其氧化还原热力学的情况下,显著改善了它们的氧化还原动力学。钌浸透的钙钛矿结构rc(即LaFeO3、lafe0.625 mn0.3750 o3和LaFe0.5Mn0.5O3)在合成气收率(92 - 100 %)和CO2转化率(95-98 %)方面表现出优异的氧化还原性能。钌浸渍LaFeO3和LaFe0.5Mn0.5O3的长期氧化还原测试表明,lafe0.625 mn0.3750 o3、LaFe0.375Mn0.625O3和LaMnO3的氧化还原循环在100次循环中表现出相对稳定的性能,而lafe0.625 mn0.3750 o3和LaMnO3的氧化还原活性分别出现损失。在含锰和铁的rc中,LaFe0.5Mn0.5O3表现最好,在100次循环中仍保持令人满意的活性和较高的氧容量。XRD和XPS分析表明,在CO2环境下再生钙钛矿相的能力和接近钙钛矿化学计量的近表面a:B位阳离子比可能对应更稳定的性能。此外,与未掺杂的LaFeO3相比,b位上Mn的加入提高了氧化还原催化剂的抗焦性。
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引用次数: 0
Tailoring Ni particle size to improve catalytic methane decomposition on La2Ce2O7 supports 调整Ni颗粒尺寸以改善La2Ce2O7载体上催化甲烷分解
IF 5.3 2区 化学 Q1 CHEMISTRY, APPLIED Pub Date : 2025-09-04 DOI: 10.1016/j.cattod.2025.115550
Sung-Bin Choi , Da-Bin Kang , Su-Ji Kim , Gwan-Joong Park , Youngji Kim , Woohyun Kim , Chang Hyun Ko
Catalytic decomposition of methane (CDM) provides a CO₂-free route for hydrogen production, where the structure and dispersion of Ni particles play a critical role in determining catalytic performance. In this study, Ni-based catalysts supported on Ce-rich La–Ce mixed oxides were synthesized using two different precipitation methods: co-precipitation (CP) and deposition- precipitation (DP). The CP method resulted in the incorporation of Ni species within the support lattice, which led to stronger metal–support interaction but limited surface accessibility. In contrast, the DP method produced Ni particles mainly on the support surface, enhancing methane activation at low Ni loadings. However, when the Ni loading exceeded 20 wt%, the DP catalysts showed significant particle aggregation and partial detachment from the support. Despite retaining moderately ordered carbon structures, this structural degradation reduced CDM activity due to diminished dispersion and weaker particle anchoring. Among all catalysts tested, the DP–NLC–10 sample with approximately 30 nm Ni particles exhibited the highest carbon yield, attributed to its optimal particle size and surface dispersion. These results demonstrate that not only the amount, but also the spatial arrangement and stability of Ni particles must be carefully controlled to achieve high and stable performance in methane decomposition.
甲烷的催化分解(CDM)为制氢提供了一条无CO₂的途径,其中Ni颗粒的结构和分散对催化性能起着关键作用。本文采用共沉淀法(CP)和沉积-沉淀法(DP)制备了负载在富ce La-Ce混合氧化物上的ni基催化剂。CP方法导致Ni物种在支撑晶格内的结合,这导致金属-支撑相互作用更强,但限制了表面可及性。相比之下,DP方法主要在支撑表面产生Ni颗粒,在低Ni负载下增强了甲烷的活化。然而,当Ni负载超过20 wt%时,DP催化剂表现出明显的颗粒聚集和部分脱离载体的现象。尽管保留了适度有序的碳结构,但由于分散性减弱和颗粒锚定性减弱,这种结构降解降低了CDM活性。在所有测试的催化剂中,含有约30 nm Ni颗粒的DP-NLC-10样品的碳收率最高,这归功于其最佳的粒径和表面分散。这些结果表明,要想在甲烷分解中获得高稳定的性能,不仅要控制Ni颗粒的数量,而且要控制Ni颗粒的空间排列和稳定性。
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引用次数: 0
Strain-driven adsorption site modification on Pd-based nano cube for fuel cell application 燃料电池用钯基纳米立方体的应变驱动吸附位点修饰
IF 5.3 2区 化学 Q1 CHEMISTRY, APPLIED Pub Date : 2025-09-03 DOI: 10.1016/j.cattod.2025.115547
Yeonwoo Do , Seohee Jang , Seokho Lee , Yiyun Yang , Yunjeong Jang , Hyun-Suk Kim , Kwun-Bum Chung , Kyung-Wan Nam , Yoon Kee Kim , Kihyun Shin
This research focused on maximizing the catalytic activity in nanocubes (NCs) with (100) facets. The primary goal was to reduce the adsorption energy of the adsorbate, thereby enhancing the activity of the fuel cell catalyst and approaching the optimal point on the volcano plot. We induced strain by introducing core elements such as Ru, Rh, Ir, Au, Ag, Ni, Pt, Cu, and their intermetallic compounds. The adsorption energy for intermediates (such as O, OH, and OOH) was calculated by exploring various adsorption sites. Studies of strain and charge analysis have been conducted, providing deeper insight into interactions at the atomic level. Strain analysis revealed how the different core elements affect the lattice parameters and consequently the adsorption energy of the intermediates. Charge analysis highlighted the redistribution of electron density upon adsorption, providing a clearer picture of the relationship between strain, electronic structure, and catalytic activity. The study illuminated the prospect of advancing fuel cell technology through a comprehensive understanding of the interplay between the surface reconstruction and strain on the (100) surface. Such understanding enabled effective manipulation of catalytic adsorption energy, offering promising strategies for further enhancing fuel cell catalyst activity.
本研究的重点是最大化纳米立方(NCs)的催化活性与(100)面。主要目标是降低吸附质的吸附能,从而提高燃料电池催化剂的活性,并接近火山地块上的最佳点。我们通过引入Ru、Rh、Ir、Au、Ag、Ni、Pt、Cu及其金属间化合物等核心元素诱导应变。通过探索不同的吸附位点来计算中间体(如O、OH和OOH)的吸附能。应变和电荷分析的研究已经进行,提供了更深入的了解原子水平上的相互作用。应变分析揭示了不同的核心元素如何影响晶格参数,从而影响中间体的吸附能。电荷分析强调了吸附时电子密度的重新分布,为应变、电子结构和催化活性之间的关系提供了更清晰的图像。该研究通过对(100)表面重构和应变之间相互作用的全面理解,照亮了推进燃料电池技术的前景。这样的理解使得有效地操纵催化吸附能量成为可能,为进一步提高燃料电池催化剂活性提供了有希望的策略。
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引用次数: 0
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Catalysis Today
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