Pub Date : 2025-10-01DOI: 10.1016/j.cattod.2025.115583
Andrei Y. Khodakov , Vitaly V. Ordomsky , Xiulian Pan
{"title":"C1 chemistry and catalysis: Current advances and future perspectives","authors":"Andrei Y. Khodakov , Vitaly V. Ordomsky , Xiulian Pan","doi":"10.1016/j.cattod.2025.115583","DOIUrl":"10.1016/j.cattod.2025.115583","url":null,"abstract":"","PeriodicalId":264,"journal":{"name":"Catalysis Today","volume":"463 ","pages":"Article 115583"},"PeriodicalIF":5.3,"publicationDate":"2025-10-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145463335","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}
Pub Date : 2025-09-30DOI: 10.1016/j.cattod.2025.115580
Oleksiy V. Shvets , Mykhailo M. Kurmach , Michal Mazur , Petr Golis , Pavlo S. Yaremov , Oleg Petrov , Nataliya D. Shcherban , Jiři Čejka , Mariya V. Shamzhy
Nanolayered zeolites are at the forefront of research as efficient catalysts for reactions involving bulky molecules. To date, various zeolites have been synthesized in nanolayered form via direct hydrothermal crystallization using Gemini-type surfactants, and their enhanced catalytic performance has been demonstrated in acid-catalyzed transformations of bulky substrates. However, the influence of zeolite topology on the strength and coordination environment of surface acid sites and its effect on catalytic behavior remains insufficiently understood. This study explores topology-acidity-activity relationships using a series of nanolayered aluminosilicate zeolites with FER, MFI, MOR, and BEA topologies in the alkylation of mesitylene with benzyl alcohol as a surface-acid-site-sensitive model reaction. In situ FTIR-monitored thermodesorption of substituted pyridines showed comparable surface Brønsted acid strength across the zeolites, while 27Al MAS NMR spectroscopy revealed a topology-dependent increase in fraction of distorted tetrahedral Al sites: MFI (21 %) < FER (30 %) < MOR (57 %) < BEA (64 %). Catalytic activity increased with surface-accessible Brønsted acid site concentration (mmol/g) or density (mmol/m2) in nanolayered MFI, FER, and MOR, with FER showing the highest yield (37 %) and selectivity (84 %). This trend was disrupted in BEA, which, despite the reasonably high surface Brønsted acid site concentration, showed lower activity. The findings of this study highlight the impact of topology-dependent structural features on catalytic performance of nanolayered zeolites.
纳米层沸石作为大分子反应的高效催化剂,处于研究的前沿。迄今为止,各种沸石已经通过使用gemini型表面活性剂通过直接水热结晶以纳米层形式合成,并且它们的增强催化性能已经在酸催化转化大块底物中得到证明。然而,沸石拓扑结构对表面酸位强度和配位环境的影响及其对催化行为的影响尚不清楚。本研究使用一系列具有FER、MFI、MOR和BEA拓扑结构的纳米层铝硅酸盐沸石作为表面酸位敏感模型反应,探索了拓扑-酸-活性关系。原位红外监测取代吡啶的热脱附显示沸石表面Brønsted酸强度相当,而27Al MAS NMR显示扭曲四面体Al位点的拓扑依赖性增加:MFI (21%) <; FER (30%) <; MOR (57%) <; BEA(64%)。纳米层MFI、FER和MOR的催化活性随表面可达Brønsted酸位浓度(mmol/g)或密度(mmol/m2)的增加而增加,其中FER的产率最高(37%),选择性最高(84%)。这一趋势在BEA中被打破,尽管表面Brønsted酸位点浓度相当高,但活性较低。本研究结果强调了拓扑依赖的结构特征对纳米层沸石催化性能的影响。
{"title":"Topology-acidity-catalytic activity interplay in hierarchical nanolayered aluminosilicate zeolites for Friedel-Crafts alkylation","authors":"Oleksiy V. Shvets , Mykhailo M. Kurmach , Michal Mazur , Petr Golis , Pavlo S. Yaremov , Oleg Petrov , Nataliya D. Shcherban , Jiři Čejka , Mariya V. Shamzhy","doi":"10.1016/j.cattod.2025.115580","DOIUrl":"10.1016/j.cattod.2025.115580","url":null,"abstract":"<div><div>Nanolayered zeolites are at the forefront of research as efficient catalysts for reactions involving bulky molecules. To date, various zeolites have been synthesized in nanolayered form <em>via</em> direct hydrothermal crystallization using Gemini-type surfactants, and their enhanced catalytic performance has been demonstrated in acid-catalyzed transformations of bulky substrates. However, the influence of zeolite topology on the strength and coordination environment of surface acid sites and its effect on catalytic behavior remains insufficiently understood. This study explores topology-acidity-activity relationships using a series of nanolayered aluminosilicate zeolites with FER, MFI, MOR, and BEA topologies in the alkylation of mesitylene with benzyl alcohol as a surface-acid-site-sensitive model reaction. <em>In situ</em> FTIR-monitored thermodesorption of substituted pyridines showed comparable surface Brønsted acid strength across the zeolites, while <sup>27</sup>Al MAS NMR spectroscopy revealed a topology-dependent increase in fraction of distorted tetrahedral Al sites: MFI (21 %) < FER (30 %) < MOR (57 %) < BEA (64 %). Catalytic activity increased with surface-accessible Brønsted acid site concentration (mmol/g) or density (mmol/m<sup>2</sup>) in nanolayered MFI, FER, and MOR, with FER showing the highest yield (37 %) and selectivity (84 %). This trend was disrupted in BEA, which, despite the reasonably high surface Brønsted acid site concentration, showed lower activity. The findings of this study highlight the impact of topology-dependent structural features on catalytic performance of nanolayered zeolites.</div></div>","PeriodicalId":264,"journal":{"name":"Catalysis Today","volume":"463 ","pages":"Article 115580"},"PeriodicalIF":5.3,"publicationDate":"2025-09-30","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145219086","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}
Pub Date : 2025-09-26DOI: 10.1016/j.cattod.2025.115578
Taeeun Kwon , Jaewoo Kim , Ki Hyuk Kang , Wangyun Won , Insoo Ro
The catalytic upcycling of polyethylene (PE) remains a major challenge in sustainable waste management. This study demonstrates that water promotes PE hydrocracking over Ru/zeolite catalysts only when the support framework is strongly hydrophilic, as in HY and HMOR. Systematic characterization reveals that this promotional effect is governed by surface wettability, rather than acidity or metal dispersion. Thermodynamic analysis confirms that water and PE are immiscible under reaction conditions, ruling out direct water–polymer interactions. Instead, water preferentially associates with hydrophilic catalyst surfaces, promoting Brønsted acid activity through confined hydration. Controlled experiments show that direct contact between water and the catalyst is essential for enhanced reactivity; spatial separation between the two leads to suppressed conversion, likely due to unfavorable interactions between water and the molten polymer. These findings highlight the mechanistic role of interfacial water–catalyst accessibility and establish catalyst hydrophilicity as a key design parameter for reliable and efficient water-assisted hydrocracking. The results have practical implications for processing moisture-containing plastic waste streams.
{"title":"Influence of zeolite hydrophilicity and hydrophobicity on water-assisted polyethylene hydrocracking","authors":"Taeeun Kwon , Jaewoo Kim , Ki Hyuk Kang , Wangyun Won , Insoo Ro","doi":"10.1016/j.cattod.2025.115578","DOIUrl":"10.1016/j.cattod.2025.115578","url":null,"abstract":"<div><div>The catalytic upcycling of polyethylene (PE) remains a major challenge in sustainable waste management. This study demonstrates that water promotes PE hydrocracking over Ru/zeolite catalysts only when the support framework is strongly hydrophilic, as in HY and HMOR. Systematic characterization reveals that this promotional effect is governed by surface wettability, rather than acidity or metal dispersion. Thermodynamic analysis confirms that water and PE are immiscible under reaction conditions, ruling out direct water–polymer interactions. Instead, water preferentially associates with hydrophilic catalyst surfaces, promoting Brønsted acid activity through confined hydration. Controlled experiments show that direct contact between water and the catalyst is essential for enhanced reactivity; spatial separation between the two leads to suppressed conversion, likely due to unfavorable interactions between water and the molten polymer. These findings highlight the mechanistic role of interfacial water–catalyst accessibility and establish catalyst hydrophilicity as a key design parameter for reliable and efficient water-assisted hydrocracking. The results have practical implications for processing moisture-containing plastic waste streams.</div></div>","PeriodicalId":264,"journal":{"name":"Catalysis Today","volume":"462 ","pages":"Article 115578"},"PeriodicalIF":5.3,"publicationDate":"2025-09-26","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145227246","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}
Pub Date : 2025-09-24DOI: 10.1016/j.cattod.2025.115579
Junya Omaki, Natsumi Yano, Yusuke Kataoka
A new cyclometalated dinuclear iridium complex with a 1,2-bis(4′-methyl-2,2'-bipyridin-4-yl)ethane (bmbe) bridging ligand, [Ir2(ppy)4(bmbe)](PF6)2 (IrPS-D; ppy = 2-phenylpyridinate), which is anticipated to function as a highly efficient photosensitizer (PS) for the photochemical hydrogen evolution reaction, is synthesized and structurally characterized via 1H NMR, ESI-TOF-MS, ATR-FT-IR, elemental analysis, and single crystal X-ray diffraction analyses. The combination of spectroscopic analysis and time-dependent density functional theory calculations clarifies that (i) the visible-light absorption spectrum of IrPS-D exhibits a shape and excitation features almost identical to those of [Ir(ppy)2(dmbpy)]PF6 (IrPS-M; dmbpy = 4,4'-dimethyl-2,2′-bipyridine), which is a well-known promising PS for the photochemical hydrogen evolution reaction and mononuclear counterpart of IrPS-D, whereas the spectral intensity of IrPS-D is approximately twice as high as that of IrPS-M; (ii) the emission energies of IrPS-D and IrPS-M are nearly identical; however, IrPS-D exhibits a slightly shorter emission lifetime and higher quantum yield compared with those of IrPS-M, resulting in relatively faster radiative and non-radiative rate constants for IrPS-D compared with those of IrPS-M; and (iii) the excited state of IrPS-D is quenched by triethylamine (TEA) faster than that of IrPS-M. Upon visible-light irradiation, IrPS-D serves as a highly efficient PS for the photochemical hydrogen evolution reaction in the presence of K2PtCl4 and TEA, which function as the hydrogen evolution catalyst and sacrificial electron donor, respectively. The maximum turnover number (TONPS) of IrPS-D for hydrogen evolution is 2672, which is approximately 4.75 times greater than that of IrPS-M (TONPS = 563) under the same reaction conditions.
{"title":"Cyclometalated dinuclear iridium(III) complex with 2,2'-bipyridyl-based bridging ligand as a photosensitizer for photochemical hydrogen evolution reaction","authors":"Junya Omaki, Natsumi Yano, Yusuke Kataoka","doi":"10.1016/j.cattod.2025.115579","DOIUrl":"10.1016/j.cattod.2025.115579","url":null,"abstract":"<div><div>A new cyclometalated dinuclear iridium complex with a 1,2-bis(4′-methyl-2,2'-bipyridin-4-yl)ethane (bmbe) bridging ligand, [Ir<sub>2</sub>(ppy)<sub>4</sub>(bmbe)](PF<sub>6</sub>)<sub>2</sub> (<strong>IrPS-D</strong>; ppy = 2-phenylpyridinate), which is anticipated to function as a highly efficient photosensitizer (PS) for the photochemical hydrogen evolution reaction, is synthesized and structurally characterized via <sup>1</sup>H NMR, ESI-TOF-MS, ATR-FT-IR, elemental analysis, and single crystal X-ray diffraction analyses. The combination of spectroscopic analysis and time-dependent density functional theory calculations clarifies that (i) the visible-light absorption spectrum of <strong>IrPS-D</strong> exhibits a shape and excitation features almost identical to those of [Ir(ppy)<sub>2</sub>(dmbpy)]PF<sub>6</sub> (<strong>IrPS-M</strong>; dmbpy = 4,4<em>'</em>-dimethyl-2<em>,2′</em>-bipyridine), which is a well-known promising PS for the photochemical hydrogen evolution reaction and mononuclear counterpart of <strong>IrPS-D</strong>, whereas the spectral intensity of <strong>IrPS-D</strong> is approximately twice as high as that of <strong>IrPS-M</strong>; (ii) the emission energies of <strong>IrPS-D</strong> and <strong>IrPS-M</strong> are nearly identical; however, <strong>IrPS-D</strong> exhibits a slightly shorter emission lifetime and higher quantum yield compared with those of <strong>IrPS-M</strong>, resulting in relatively faster radiative and non-radiative rate constants for <strong>IrPS-D</strong> compared with those of <strong>IrPS-M</strong>; and (iii) the excited state of <strong>IrPS-D</strong> is quenched by triethylamine (TEA) faster than that of <strong>IrPS-M</strong>. Upon visible-light irradiation, <strong>IrPS-D</strong> serves as a highly efficient PS for the photochemical hydrogen evolution reaction in the presence of K<sub>2</sub>PtCl<sub>4</sub> and TEA, which function as the hydrogen evolution catalyst and sacrificial electron donor, respectively. The maximum turnover number (TON<sub>PS</sub>) of <strong>IrPS-D</strong> for hydrogen evolution is 2672, which is approximately 4.75 times greater than that of <strong>IrPS-M</strong> (TON<sub>PS</sub> = 563) under the same reaction conditions.</div></div>","PeriodicalId":264,"journal":{"name":"Catalysis Today","volume":"462 ","pages":"Article 115579"},"PeriodicalIF":5.3,"publicationDate":"2025-09-24","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145227248","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}
Formic acid is a promising hydrogen carrier because of its high hydrogen content and small enthalpy of dehydrogenation. Hydrogen is generally produced from formic acid via liquid-phase decomposition over catalysts. Catalysts consisting of noble metals that are stable in acidic solutions and carbon supports without acidic sites causing side reactions have several advantages, such as the high activity and ease of separation. To enhance catalytic activity, the surface area of the active metal should be increased. However, conventional impregnation methods are not completely suitable for this purpose because of the weak metal–carbon interactions. To solve this problem, a preparation method using an ion-exchange resin as a precursor for the carbon support was employed. In this study, we investigated the effect of the preparation method of carbon-supported Pt catalysts on their catalytic activity for the liquid-phase decomposition of formic acid. The catalysts prepared from ion-exchange resins exhibited Pt loadings of approximately 26–28 wt% and Pt particle sizes of 2–3 nm; therefore, this method can realize a higher dispersion degree of Pt nanoparticles than an impregnation method. Moreover, the produced catalysts demonstrated a higher activity for the dehydrogenation of formic acid than those of the catalysts prepared by the impregnation method. Additionally, the carbonization temperature strongly affected the catalyst properties, such as the pore size and metal accessibility. Consequently, the catalyst activity for the decomposition of formic acid varied depending on the carbonization temperature. We also formulated a new reaction model considering hydrogen adsorption.
{"title":"Hydrogen production from aqueous formic acid solution using Pt/Cs with different preparation methods","authors":"Shuka Murakami, Hiroyasu Fujitsuka, Motoaki Kawase","doi":"10.1016/j.cattod.2025.115575","DOIUrl":"10.1016/j.cattod.2025.115575","url":null,"abstract":"<div><div>Formic acid is a promising hydrogen carrier because of its high hydrogen content and small enthalpy of dehydrogenation. Hydrogen is generally produced from formic acid via liquid-phase decomposition over catalysts. Catalysts consisting of noble metals that are stable in acidic solutions and carbon supports without acidic sites causing side reactions have several advantages, such as the high activity and ease of separation. To enhance catalytic activity, the surface area of the active metal should be increased. However, conventional impregnation methods are not completely suitable for this purpose because of the weak metal–carbon interactions. To solve this problem, a preparation method using an ion-exchange resin as a precursor for the carbon support was employed. In this study, we investigated the effect of the preparation method of carbon-supported Pt catalysts on their catalytic activity for the liquid-phase decomposition of formic acid. The catalysts prepared from ion-exchange resins exhibited Pt loadings of approximately 26–28 wt% and Pt particle sizes of 2–3 nm; therefore, this method can realize a higher dispersion degree of Pt nanoparticles than an impregnation method. Moreover, the produced catalysts demonstrated a higher activity for the dehydrogenation of formic acid than those of the catalysts prepared by the impregnation method. Additionally, the carbonization temperature strongly affected the catalyst properties, such as the pore size and metal accessibility. Consequently, the catalyst activity for the decomposition of formic acid varied depending on the carbonization temperature. We also formulated a new reaction model considering hydrogen adsorption.</div></div>","PeriodicalId":264,"journal":{"name":"Catalysis Today","volume":"462 ","pages":"Article 115575"},"PeriodicalIF":5.3,"publicationDate":"2025-09-23","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145155984","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}
Pub Date : 2025-09-23DOI: 10.1016/j.cattod.2025.115574
Hyeonji Yeom, Yongseok Kim, Hanbit Jang, Jongmin Park, Seongeun Kim, Kyungsu Na
The direct CO2 hydrogenation into liquid-phase hydrocarbons offers a sustainable route for carbon recycling, yet achieving high selectivity toward sustainable aviation fuel-range aromatic compounds remains challenging. Here, we report a bifunctional catalyst system composed of FeK-loaded CuAl2O4-based catalyst (FeK/CAO) and a nanosheet MFI-type zeolite (NS-HMFI) with hierarchical porosity for the selective production of C8–10 aromatic hydrocarbons. Structural and compositional characterizations confirmed the mesoporous architecture and strong acidity of NS-HMFI and the multifunctional activity of FeK/CAO in CO2 activation and C–C coupling. By engineering the spatial proximity between the two catalysts through four integration methods such as physical mixture (PM), granule mixture (GM), dual-bed system (DB), and multi-bed system (MB), we elucidated the relationship between proximity and catalytic performance. Among the systems tested, the GM system achieved the highest CO2 conversion (39.2 %) with the lowest CO selectivity (13.0 %) due to enhanced CO2 adsorption and dissociation facilitated by potassium migration and increased surface basicity. Conversely, the DB system, with minimal catalyst proximity, promoted the highest aromatic distribution and enabled selective conversion of light olefins into C8–10 aromatics. All systems integrating NS-HMFI showed >95 % distribution for C8–10 aromatics among total aromatics, highlighting the critical role of external acid sites in mesoporous zeolites. This work demonstrates a proximity-controlled catalytic approach for efficient CO2 hydrogenation to SAF-range aromatics and provides mechanistic insights into the design of multifunctional hybrid catalysts.
{"title":"Enhancing CO2 hydrogenation via spatially engineered bifunctional catalysts: Toward selective C8–10 aromatics for sustainable aviation fuel","authors":"Hyeonji Yeom, Yongseok Kim, Hanbit Jang, Jongmin Park, Seongeun Kim, Kyungsu Na","doi":"10.1016/j.cattod.2025.115574","DOIUrl":"10.1016/j.cattod.2025.115574","url":null,"abstract":"<div><div>The direct CO<sub>2</sub> hydrogenation into liquid-phase hydrocarbons offers a sustainable route for carbon recycling, yet achieving high selectivity toward sustainable aviation fuel-range aromatic compounds remains challenging. Here, we report a bifunctional catalyst system composed of FeK-loaded CuAl<sub>2</sub>O<sub>4</sub>-based catalyst (FeK/CAO) and a nanosheet MFI-type zeolite (NS-HMFI) with hierarchical porosity for the selective production of C<sub>8–10</sub> aromatic hydrocarbons. Structural and compositional characterizations confirmed the mesoporous architecture and strong acidity of NS-HMFI and the multifunctional activity of FeK/CAO in CO<sub>2</sub> activation and C–C coupling. By engineering the spatial proximity between the two catalysts through four integration methods such as physical mixture (PM), granule mixture (GM), dual-bed system (DB), and multi-bed system (MB), we elucidated the relationship between proximity and catalytic performance. Among the systems tested, the GM system achieved the highest CO<sub>2</sub> conversion (39.2 %) with the lowest CO selectivity (13.0 %) due to enhanced CO<sub>2</sub> adsorption and dissociation facilitated by potassium migration and increased surface basicity. Conversely, the DB system, with minimal catalyst proximity, promoted the highest aromatic distribution and enabled selective conversion of light olefins into C<sub>8–10</sub> aromatics. All systems integrating NS-HMFI showed >95 % distribution for C<sub>8–10</sub> aromatics among total aromatics, highlighting the critical role of external acid sites in mesoporous zeolites. This work demonstrates a proximity-controlled catalytic approach for efficient CO<sub>2</sub> hydrogenation to SAF-range aromatics and provides mechanistic insights into the design of multifunctional hybrid catalysts.</div></div>","PeriodicalId":264,"journal":{"name":"Catalysis Today","volume":"462 ","pages":"Article 115574"},"PeriodicalIF":5.3,"publicationDate":"2025-09-23","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145154914","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}
Pub Date : 2025-09-22DOI: 10.1016/j.cattod.2025.115577
Zihuai Xu , Jiasheng Wang , Xiujuan Feng , Sheng Zhang , Xiaoqiang Yu , Xuan Zhang , Ming Bao
A film-like MgO-supported trimetallic catalysts CuZnCo/MgO/CNFs were prepared for selective hydrogenation of furfural into furfuryl alcohol for the first time. The hydrogenation reaction of furfural proceeded smoothly in the presence of the optimal catalyst CuZn0.125Co0.5/MgO/CNFs under mild conditions to provide the desired product furfuryl alcohol in quantitative yield with nearly 100 % selectivity. The catalyst CuZn0.125Co0.5/MgO/CNFs could be easily recycled by a magnet due to its magnetic property and reused for several times without deactivation. The structure of the catalyst CuZn0.125Co0.5/MgO/CNFs was characterized by using various techniques such as scanning electron microscopy, transmission electron microscopy, X-ray diffraction, and X-ray photoelectron spectroscopy. The high catalytic activity of CuZn0.125Co0.5/MgO/CNFs is attributed to the synergistic effect of the three metals (Cu, Zn, and Co).
{"title":"Preparation and application of film-like mesoporous MgO-supported Cu-Zn-Co trimetallic catalyst for selective hydrogenation of furfural to furfuryl alcohol","authors":"Zihuai Xu , Jiasheng Wang , Xiujuan Feng , Sheng Zhang , Xiaoqiang Yu , Xuan Zhang , Ming Bao","doi":"10.1016/j.cattod.2025.115577","DOIUrl":"10.1016/j.cattod.2025.115577","url":null,"abstract":"<div><div>A film-like MgO-supported trimetallic catalysts CuZnCo/MgO/CNFs were prepared for selective hydrogenation of furfural into furfuryl alcohol for the first time. The hydrogenation reaction of furfural proceeded smoothly in the presence of the optimal catalyst CuZn<sub>0.125</sub>Co<sub>0.5</sub>/MgO/CNFs under mild conditions to provide the desired product furfuryl alcohol in quantitative yield with nearly 100 % selectivity. The catalyst CuZn<sub>0.125</sub>Co<sub>0.5</sub>/MgO/CNFs could be easily recycled by a magnet due to its magnetic property and reused for several times without deactivation. The structure of the catalyst CuZn<sub>0.125</sub>Co<sub>0.5</sub>/MgO/CNFs was characterized by using various techniques such as scanning electron microscopy, transmission electron microscopy, X-ray diffraction, and X-ray photoelectron spectroscopy. The high catalytic activity of CuZn<sub>0.125</sub>Co<sub>0.5</sub>/MgO/CNFs is attributed to the synergistic effect of the three metals (Cu, Zn, and Co).</div></div>","PeriodicalId":264,"journal":{"name":"Catalysis Today","volume":"462 ","pages":"Article 115577"},"PeriodicalIF":5.3,"publicationDate":"2025-09-22","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145154916","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}
CO2 hydrogenation to methanol is one of the most promising routes for CO2 utilization. In CO2 hydrogenation, low temperatures and high pressures are thermodynamically favorable for high CO2 conversion and methanol selectivity. However, owing to the difficulty in activating CO₂ at low temperatures, developing catalysts that function under mild conditions is a significant challenge. In this study, we demonstrate that ZrO₂-supported Au nanoparticles promote the hydrogenation of CO₂ to produce CH₃OH under mild conditions (160 °C, 4 MPa, H₂/CO₂ molar ratio = 3), whereas the conventional Cu-based catalyst shows no activity. Methanol selectivity improved by adding a trace amount of Cu (based on ≤0.3 wt%) to Au/ZrO₂. Compared with Au/ZrO₂, Au–Cu/ZrO₂ maintained a high methanol production rate and suppressed CO production, resulting in improved methanol selectivity. Based on kinetic analysis, in situ infrared spectroscopy, structural characterization, and OH–D2 exchange, we propose that the addition of a trace amount of Cu to Au/ZrO2 suppresses CO production via formate decomposition owing to the decrease in the spillover rate of hydrogen from the Au nanoparticles to ZrO2, resulting in improved methanol selectivity.
CO2加氢制甲醇是CO2利用最有前途的途径之一。在CO2加氢过程中,低温和高压在热力学上有利于CO2的高转化率和甲醇的选择性。但是,由于很难在低温条件下活化CO₂,因此开发在温和条件下也能发挥作用的催化剂是一个巨大的挑战。在这项研究中,我们证明了负载ZrO₂的Au纳米颗粒在温和的条件下(160 °C, 4 MPa, H₂/CO₂摩尔比= 3)促进CO₂加氢生成CH₃OH,而传统的cu基催化剂没有表现出活性。在Au/ZrO₂中加入微量Cu(基于≤0.3 wt%),提高了甲醇的选择性。与Au/ZrO₂相比,Au - cu /ZrO₂保持了较高的甲醇收率,抑制了CO的产生,从而提高了甲醇的选择性。基于动力学分析、原位红外光谱、结构表征和OH-D2交换,我们提出在Au/ZrO2中添加微量Cu可以抑制甲酸分解产生CO,这是由于Au纳米颗粒向ZrO2中氢的溢出速率降低,从而提高了甲醇的选择性。
{"title":"Low-temperature CO2 hydrogenation to methanol on Cu-doped Au/ZrO2: Effect of Cu doping on hydrogen activation","authors":"Katsutoshi Nomoto , Yuichiro Okuzumi , Takumi Nakagawa , Hiroki Miura , Tetsuya Shishido","doi":"10.1016/j.cattod.2025.115573","DOIUrl":"10.1016/j.cattod.2025.115573","url":null,"abstract":"<div><div>CO<sub>2</sub> hydrogenation to methanol is one of the most promising routes for CO<sub>2</sub> utilization. In CO<sub>2</sub> hydrogenation, low temperatures and high pressures are thermodynamically favorable for high CO<sub>2</sub> conversion and methanol selectivity. However, owing to the difficulty in activating CO₂ at low temperatures, developing catalysts that function under mild conditions is a significant challenge. In this study, we demonstrate that ZrO₂-supported Au nanoparticles promote the hydrogenation of CO₂ to produce CH₃OH under mild conditions (160 °C, 4 MPa, H₂/CO₂ molar ratio = 3), whereas the conventional Cu-based catalyst shows no activity. Methanol selectivity improved by adding a trace amount of Cu (based on ≤0.3 wt%) to Au/ZrO₂. Compared with Au/ZrO₂, Au–Cu/ZrO₂ maintained a high methanol production rate and suppressed CO production, resulting in improved methanol selectivity. Based on kinetic analysis, <em>in situ</em> infrared spectroscopy, structural characterization, and OH–D<sub>2</sub> exchange, we propose that the addition of a trace amount of Cu to Au/ZrO<sub>2</sub> suppresses CO production via formate decomposition owing to the decrease in the spillover rate of hydrogen from the Au nanoparticles to ZrO<sub>2</sub>, resulting in improved methanol selectivity.</div></div>","PeriodicalId":264,"journal":{"name":"Catalysis Today","volume":"462 ","pages":"Article 115573"},"PeriodicalIF":5.3,"publicationDate":"2025-09-20","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145154912","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}
Pub Date : 2025-09-20DOI: 10.1016/j.cattod.2025.115576
Hankyeul Kang, Tae Hoon Lee, Jong Hun Kang
Plastic waste, particularly from polyolefins such as polyethylene (PE), poses an escalating environmental burden due to its chemical inertness and volume. Pyrolysis is commercialized process that offers a practical solution for recycling plastic waste, but it is limited by high temperature requirements, substantial energy consumption, and high proportion of olefinic products. Hydrocracking with bifunctional catalysts under optimized conditions presents a promising alternative.
Here, we developed a property-optimized Ru/Beta catalyst system combined with a pressurized open batch distillation reactor for the selective hydrocracking of waste PE into C5–C30 hydrocarbons. Zeolite Beta supports with varied Si/Al ratios and crystal sizes were synthesized to control Brønsted acid site distribution and external surface area. The controlled properties influenced Ru nanoparticle dispersion, hydrogen activation, and overall catalytic activity. Nano-sized zeolite Beta supports exhibited the highest Ru dispersion and facilitated efficient hydrocracking. The open batch reactor configuration enabled real-time vapor-phase separation of volatile products, minimizing secondary cracking. Under optimized conditions (280 °C, 40 H2 bar), Ru/nanosized Beta with (Si/Al=10) achieved over an 80 % PE conversion and a 50 % selectivity toward C5–C30 liquid hydrocarbons. Product analysis using GC-FID, GPC, and ¹H NMR confirmed the formation of branched alkanes with a narrow molecular weight distribution in the C5–C15 range. This work underscores the critical role of metal–acid site balance, nanoscale catalyst engineering, and dynamic reactor operation in achieving selective and efficient polyolefin hydrocracking.
塑料废物,特别是来自聚乙烯(PE)等聚烯烃的塑料废物,由于其化学惰性和体积,造成了日益严重的环境负担。热解是一种商业化的工艺,为塑料废弃物的回收利用提供了切实可行的解决方案,但存在温度要求高、能耗大、烯烃产物比例高等限制。在优化条件下,双功能催化剂加氢裂化是一种很有前景的选择。在这里,我们开发了一种性能优化的Ru/Beta催化剂体系,结合加压开放式蒸馏反应器,用于将废PE选择性加氢裂化成C5-C30烃。合成了不同Si/Al比和晶体尺寸的沸石β载体,以控制Brønsted酸位分布和外表面积。受控制的性质影响钌纳米颗粒的分散、氢活化和整体催化活性。纳米沸石β载体表现出最高的Ru分散性,促进了高效的加氢裂化。开放式间歇反应器配置实现了挥发性产物的实时气相分离,最大限度地减少了二次裂解。在优化条件下(280 °C, 40 H2 bar), Ru/纳米尺寸β (Si/Al=10)的PE转化率超过80%,对C5-C30液态烃的选择性超过50%。通过GC-FID、GPC和¹H NMR对产物进行分析,证实在C5-C15范围内形成了分子量分布较窄的支链烷烃。这项工作强调了金属-酸位点平衡、纳米级催化剂工程和动态反应器操作在实现选择性和高效聚烯烃加氢裂化中的关键作用。
{"title":"Coupling property-optimized Ru/Beta catalysts with advanced open batch distillation reactors for waste polyethylene hydrocracking","authors":"Hankyeul Kang, Tae Hoon Lee, Jong Hun Kang","doi":"10.1016/j.cattod.2025.115576","DOIUrl":"10.1016/j.cattod.2025.115576","url":null,"abstract":"<div><div>Plastic waste, particularly from polyolefins such as polyethylene (PE), poses an escalating environmental burden due to its chemical inertness and volume. Pyrolysis is commercialized process that offers a practical solution for recycling plastic waste, but it is limited by high temperature requirements, substantial energy consumption, and high proportion of olefinic products. Hydrocracking with bifunctional catalysts under optimized conditions presents a promising alternative.</div><div>Here, we developed a property-optimized Ru/Beta catalyst system combined with a pressurized open batch distillation reactor for the selective hydrocracking of waste PE into C<sub>5</sub>–C<sub>30</sub> hydrocarbons. Zeolite Beta supports with varied Si/Al ratios and crystal sizes were synthesized to control Brønsted acid site distribution and external surface area. The controlled properties influenced Ru nanoparticle dispersion, hydrogen activation, and overall catalytic activity. Nano-sized zeolite Beta supports exhibited the highest Ru dispersion and facilitated efficient hydrocracking. The open batch reactor configuration enabled real-time vapor-phase separation of volatile products, minimizing secondary cracking. Under optimized conditions (280 °C, 40 H<sub>2</sub> bar), Ru/nanosized Beta with (Si/Al=10) achieved over an 80 % PE conversion and a 50 % selectivity toward C<sub>5</sub>–C<sub>30</sub> liquid hydrocarbons. Product analysis using GC-FID, GPC, and ¹H NMR confirmed the formation of branched alkanes with a narrow molecular weight distribution in the C<sub>5</sub>–C<sub>15</sub> range. This work underscores the critical role of metal–acid site balance, nanoscale catalyst engineering, and dynamic reactor operation in achieving selective and efficient polyolefin hydrocracking.</div></div>","PeriodicalId":264,"journal":{"name":"Catalysis Today","volume":"462 ","pages":"Article 115576"},"PeriodicalIF":5.3,"publicationDate":"2025-09-20","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145154911","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}