Fuel Processing Technology最新文献

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A cation-exchange membrane direct formate-CO2 fuel cell: Enabling simultaneous hydrogen production and CO2 utilization 一种阳离子交换膜直接甲酸-二氧化碳燃料电池:能够同时生产氢气和利用二氧化碳
IF 7.7 2区 工程技术
Fuel Processing Technology Pub Date : 2025-11-15 Epub Date: 2025-09-30 DOI: 10.1016/j.fuproc.2025.108346
Jinxu Hao , Xianda Sun , Baibin Ma , Wanzhen Huang , Yuandong Yang , Xiaohan Ren
{"title":"A cation-exchange membrane direct formate-CO2 fuel cell: Enabling simultaneous hydrogen production and CO2 utilization","authors":"Jinxu Hao ,&nbsp;Xianda Sun ,&nbsp;Baibin Ma ,&nbsp;Wanzhen Huang ,&nbsp;Yuandong Yang ,&nbsp;Xiaohan Ren","doi":"10.1016/j.fuproc.2025.108346","DOIUrl":"10.1016/j.fuproc.2025.108346","url":null,"abstract":"<div><div>The carbon-neutral and carbon-negative energy utilization technologies have long been people pursued to realize the strategic objective of carbon neutrality. Herein, we propose a cation-exchange membrane (CEM) direct formate-CO<sub>2</sub> fuel cell that possesses the capability of simultaneously generating electricity and producing hydrogen, as well as continuously transforming carbon dioxide into pure sodium bicarbonate. Using the CO<sub>2</sub>-derived formate fuel, the roof-of-concept CEM direct formate-CO<sub>2</sub> fuel cell exhibits a peak power density of 38 mW cm<sup>−2</sup> at 80 °C without the assistance of additional electrolyte. The fairly stable constant-current discharge curve along with the detected hydrogen and pure sodium bicarbonate prove the conceptual feasibility of this electricity‑hydrogen-bicarbonate co-production device. By adding alkaline electrolyte to the anode, we achieved a higher peak power density of 63 mW cm<sup>−2</sup> at the corresponding hydrogen production rate of 0.57 mL min<sup>−1</sup> cm<sup>−2</sup>. More interestingly, the concentrations of pure NaHCO<sub>3</sub> solution can be controlled by adjusting the cathode water flow rate and fuel cell discharge current density. This work presents a theoretically feasible avenue for coupling hydrogen production and CO<sub>2</sub> utilization.</div></div>","PeriodicalId":326,"journal":{"name":"Fuel Processing Technology","volume":"278 ","pages":"Article 108346"},"PeriodicalIF":7.7,"publicationDate":"2025-11-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145227249","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
Catalytic methanol reforming process intensification for integration with proton-exchange membrane fuel cells (PEMFC) - Review 与质子交换膜燃料电池(PEMFC)集成的催化甲醇重整过程强化——综述
IF 7.7 2区 工程技术
Fuel Processing Technology Pub Date : 2025-11-15 Epub Date: 2025-10-17 DOI: 10.1016/j.fuproc.2025.108350
Emilija Todorovski , Filip Todorovski , Andrej Lotrič , Mitja Mori , Blaž Likozar , Søren Juhl Andreasen , Mihael Sekavčnik
{"title":"Catalytic methanol reforming process intensification for integration with proton-exchange membrane fuel cells (PEMFC) - Review","authors":"Emilija Todorovski ,&nbsp;Filip Todorovski ,&nbsp;Andrej Lotrič ,&nbsp;Mitja Mori ,&nbsp;Blaž Likozar ,&nbsp;Søren Juhl Andreasen ,&nbsp;Mihael Sekavčnik","doi":"10.1016/j.fuproc.2025.108350","DOIUrl":"10.1016/j.fuproc.2025.108350","url":null,"abstract":"<div><div>The Net Zero Scenario, driven by the imperative of carbon neutrality, demands a major reduction in reliance on fossil fuel-based hydrogen production. Another challenge is hydrogen's storage and transport due to its low volumetric energy density. These issues have elevated hydrogen carriers—particularly methanol—to a prominent position. Methanol's favorable H/C ratio, liquid state under ambient conditions, and renewable production potential establish it as a compelling hydrogen carrier. Already essential in vehicle fuels and chemical production, methanol's role is poised to expand further. Among conversion routes, methanol steam reforming (MSR) stands out for its high hydrogen yield and low CO production. This review outlines strategies for lowering the MSR reaction temperature, enabling integration with proton exchange membrane fuel cells (PEMFC), and leveraging the thermal synergy between the two systems. The review highlights the critical roles of catalysts and reactor design in optimizing MSR–PEMFC integration. A detailed evaluation of Cu-based and group 8–10 metal catalysts provides insight into their suitability for PEMFC applications. Reactor configurations, including conventional, membrane, and micro-channeled designs, are assessed for their integration potential. Finally, the review synthesizes these findings into design-oriented insights for optimizing MSR–PEMFC systems, emphasizing catalyst selection, reactor configuration, and system-level integration, offering practical pathways for implementation.</div></div>","PeriodicalId":326,"journal":{"name":"Fuel Processing Technology","volume":"278 ","pages":"Article 108350"},"PeriodicalIF":7.7,"publicationDate":"2025-11-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145333147","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
Machine learning-driven modeling framework for steam co-gasification applications 蒸汽共气化应用的机器学习驱动建模框架
IF 7.7 2区 工程技术
Fuel Processing Technology Pub Date : 2025-11-15 Epub Date: 2025-09-19 DOI: 10.1016/j.fuproc.2025.108340
Usman Khan Jadoon, Ismael Díaz, Manuel Rodríguez
{"title":"Machine learning-driven modeling framework for steam co-gasification applications","authors":"Usman Khan Jadoon,&nbsp;Ismael Díaz,&nbsp;Manuel Rodríguez","doi":"10.1016/j.fuproc.2025.108340","DOIUrl":"10.1016/j.fuproc.2025.108340","url":null,"abstract":"<div><div>Steam co-gasification of biomass and plastic waste is a promising route for syngas production and waste valorization. However, accurately predicting syngas composition remains challenging due to inherent complexity and nonlinearity of the process. This study presents a comprehensive comparative analysis between conventional process simulators-based models (Aspen Plus), namely the thermodynamic equilibrium (TEM), restricted thermodynamic (RTM), and kinetic (KM) modeling approaches, and machine learning (ML) models for the prediction of the syngas composition. Using 208 experimental data points compiled from 20 published studies covering various feedstocks and gasification conditions in bubbling fluidized bed gasifiers (BFBG), the performance of the models was evaluated after extensive data preprocessing. Among several ML algorithms evaluated, the neural network (NN) delivered the lowest average root mean square error in syngas mol fraction predictions (0.0174), outperforming RTM (0.0966), KM (0.1378), and TEM (0.1470). To explore input–output relationships beyond interpolation, a conditional generative adversarial network (cGAN) generated synthetic data, which served as the basis for sensitivity and interpretability analyses. The NN, acting as a surrogate model, was paired with SHapley Additive exPlanations (SHAP) and Partial Dependence Plots (PDP) to quantify the effects and nonlinear interactions of key features on syngas yields providing actionable insights for process optimization.</div></div>","PeriodicalId":326,"journal":{"name":"Fuel Processing Technology","volume":"278 ","pages":"Article 108340"},"PeriodicalIF":7.7,"publicationDate":"2025-11-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145106654","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
Emulsified fuel stabilized by comb-type ternary block copolymers for drag reduction and heat transfer enhancement 用梳型三元嵌段共聚物稳定乳化燃料,以减少阻力和增强传热
IF 7.7 2区 工程技术
Fuel Processing Technology Pub Date : 2025-11-15 Epub Date: 2025-09-17 DOI: 10.1016/j.fuproc.2025.108335
Bin Sun , Xiwei Ye , Yongsheng Guo , Shu Yan , Wenjun Fang
{"title":"Emulsified fuel stabilized by comb-type ternary block copolymers for drag reduction and heat transfer enhancement","authors":"Bin Sun ,&nbsp;Xiwei Ye ,&nbsp;Yongsheng Guo ,&nbsp;Shu Yan ,&nbsp;Wenjun Fang","doi":"10.1016/j.fuproc.2025.108335","DOIUrl":"10.1016/j.fuproc.2025.108335","url":null,"abstract":"<div><div>Turbulent flow in high-speed hydrocarbon fuels increases engine resistance and pump load, leading to higher power demands and reduced reliability. Current drag reduction agents often worsen heat transfer performance. To overcome the contradiction between drag reduction and heat transfer deterioration, comb-type ternary block copolymers, hexadecyl methacrylate-co-dimethylaminoethyl methacrylate-co-methacrylic acid, have been designed and synthesized through photoinitiated polymerization and used as emulsifiers to prepare emulsified fuels. The emulsions with different compositions of JP-10 to water as 9.5:0.5, 9:1, 8.5:1.5, and 8:2, respectively, were characterized using creaming index analysis, dynamic light scattering and zeta potential measurements, rheological analysis, laser scanning confocal microscopy and polarized optical microscopy measurements, interfacial tension and interfacial film rheology measurements. A significant enhancement in heat sink and heat transfer coefficients of the emulsified fuel compared to pure JP-10 is observed within the temperature range from 100 to 225 °C. Simultaneous enhancements in drag reduction rate and heat transfer coefficient for the emulsified fuel in a distributed flow calorimeter can reach 19.5 % and 6.09 %, respectively. Emulsified fuels show great prospects in improving the stable and highly efficient operation of advanced aircraft.</div></div>","PeriodicalId":326,"journal":{"name":"Fuel Processing Technology","volume":"278 ","pages":"Article 108335"},"PeriodicalIF":7.7,"publicationDate":"2025-11-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145106197","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
Comparative chemiluminescence investigation of OH* radicals in laminar and turbulent multi-fuel air- and oxy-fuel flames on semi-industrial and laboratory scale including NOX-formation 层流和湍流多燃料空气和全氧燃料火焰中OH*自由基在半工业和实验室规模下的化学发光对比研究,包括nox的形成
IF 7.7 2区 工程技术
Fuel Processing Technology Pub Date : 2025-11-15 Epub Date: 2025-09-26 DOI: 10.1016/j.fuproc.2025.108342
Stefan Schwarz , Georg Daurer , Joshua Slawatycki , Matthias Urban , René Prieler , Christian Gaber , Martin Demuth , Christoph Hochenauer
{"title":"Comparative chemiluminescence investigation of OH* radicals in laminar and turbulent multi-fuel air- and oxy-fuel flames on semi-industrial and laboratory scale including NOX-formation","authors":"Stefan Schwarz ,&nbsp;Georg Daurer ,&nbsp;Joshua Slawatycki ,&nbsp;Matthias Urban ,&nbsp;René Prieler ,&nbsp;Christian Gaber ,&nbsp;Martin Demuth ,&nbsp;Christoph Hochenauer","doi":"10.1016/j.fuproc.2025.108342","DOIUrl":"10.1016/j.fuproc.2025.108342","url":null,"abstract":"<div><div>Chemiluminescence emitted by the de-excitation of excited hydroxyl radicals (OH*), allows for several insights into combustion processes. The presented study investigates air- and oxy-fuel combustion of natural gas with hydrogen enrichment up to 100%, using both small-scale laminar flames and turbulent high-impulse flames (50–100 kW). The obtained results from the laminar 1 kW flames from the laboratory burner are then used, to interpret the influence of turbulence and chemistry influence from an industrial scale multi-fuel multi-oxidizer burner. The measurements performed for the laboratory burner were also compared to simulations. Experimental data were compared to 1D simulations, showing good agreement in trends. However, in turbulent flames, turbulence effects far exceeded those of combustion chemistry. While laminar flames exhibited the highest chemiluminescence intensity in CH<sub>4</sub>-air combustion in both experiments and simulations, the maximum in turbulent combustion experiments occurred in oxy-fuel combustion, with hydrogen and natural gas performing similarly. Oxy-fuel flames showed similar chemiluminescence intensities, increased by 2 orders of magnitude, compared to turbulent air-fuel combustion. Additionally, the changes in flame shape and reaction zone size for hydrogen-enrichment in air-fuel combustion were investigated in terms of NO<sub>X</sub> formation, where OH* imaging proved its potential for emission reduction.</div></div>","PeriodicalId":326,"journal":{"name":"Fuel Processing Technology","volume":"278 ","pages":"Article 108342"},"PeriodicalIF":7.7,"publicationDate":"2025-11-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145155932","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
Analysis of configurations for coupling an active magnetic regenerator with heat exchangers for hydrogen liquefaction 氢液化用主动磁蓄热器与热交换器耦合结构分析
IF 7.7 2区 工程技术
Fuel Processing Technology Pub Date : 2025-11-15 Epub Date: 2025-09-25 DOI: 10.1016/j.fuproc.2025.108337
Angelica Liponi , Mathieu Tenda , Rasmus Bjørk , Umberto Desideri
{"title":"Analysis of configurations for coupling an active magnetic regenerator with heat exchangers for hydrogen liquefaction","authors":"Angelica Liponi ,&nbsp;Mathieu Tenda ,&nbsp;Rasmus Bjørk ,&nbsp;Umberto Desideri","doi":"10.1016/j.fuproc.2025.108337","DOIUrl":"10.1016/j.fuproc.2025.108337","url":null,"abstract":"<div><div>This paper presents a study of four different configurations for performing the heat exchange between helium—supplied by an active magnetic regenerator (AMR)—and hydrogen in the 82–20 K range for hydrogen liquefaction. We evaluate helium mass flow requirements and analyse the configurations considering both technical and exergetic aspects. Results show a strong influence of the temperature difference of helium at the AMR cold end on the required helium mass flow rate, which ranges from 35 to over 75 times the liquid hydrogen mass flow rate. The exergy efficiency of the cooling stage, not including AMR losses, ranges between 33 % and 49 %. The use of a single AMR causes significant temperature differences between helium and hydrogen in the heat exchangers leading to large exergy losses (representing over 95 % of the overall losses). We finally show that this issue can be overcome using multiple AMR in parallel with increasing cold-end temperatures.</div></div>","PeriodicalId":326,"journal":{"name":"Fuel Processing Technology","volume":"278 ","pages":"Article 108337"},"PeriodicalIF":7.7,"publicationDate":"2025-11-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145155934","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
Stepwise Fe introduction tailors Rh-CeO2 active sites for selective CO2 hydrogenation to ethanol Fe的逐步引入调整了Rh-CeO2的活性位点,以选择性地将CO2加氢成乙醇
IF 7.7 2区 工程技术
Fuel Processing Technology Pub Date : 2025-11-15 Epub Date: 2025-10-06 DOI: 10.1016/j.fuproc.2025.108347
Jun Yu , Rui Xu , Yong Guo , Dongsen Mao , Tao Meng , Xiang Zheng , Haifang Mao
{"title":"Stepwise Fe introduction tailors Rh-CeO2 active sites for selective CO2 hydrogenation to ethanol","authors":"Jun Yu ,&nbsp;Rui Xu ,&nbsp;Yong Guo ,&nbsp;Dongsen Mao ,&nbsp;Tao Meng ,&nbsp;Xiang Zheng ,&nbsp;Haifang Mao","doi":"10.1016/j.fuproc.2025.108347","DOIUrl":"10.1016/j.fuproc.2025.108347","url":null,"abstract":"<div><div>CO<sub>2</sub> hydrogenation to produce high-value fuels like ethanol represents a cutting-edge research frontier, yet overcoming the low ethanol productivity remains a challenge. Herein, a series of Fe-promoted Rh/CeO<sub>2</sub> catalysts were prepared by varying the impregnation sequences, and investigated their catalytic performance of ethanol synthesis via CO<sub>2</sub> hydrogenation. The Fe/Rh/CeO₂ catalyst, fabricated through sequential Rh impregnation followed by Fe deposition, demonstrated remarkable performance, achieving 19.8 % ethanol selectivity at 10.8 % CO₂ conversion, with a notable one-pass ethanol productivity of 25.3 mmol·g<sub>Rh</sub><sup>−1</sup>·h<sup>−1</sup>. Characterization results revealed that sequential Rh impregnation prior to Fe can promote the Rh dispersion and metal-support interaction, enhancing CO₂ adsorption and dissociation capability. This interface also facilitates the transformation of absorbed b-CO<sub>3</sub><sup>2−</sup> into CO(l), provides high concentrations of CO(l) and HCOO* intermediates simultaneously, and finally boosting the ethanol formation by the C − C coupling reaction.</div></div>","PeriodicalId":326,"journal":{"name":"Fuel Processing Technology","volume":"278 ","pages":"Article 108347"},"PeriodicalIF":7.7,"publicationDate":"2025-11-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145263019","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
Pore structure evolution of semi-coke under steam atmosphere in the context of deep underground coal gasification 煤深埋地下气化条件下蒸汽气氛下半焦孔隙结构演化
IF 7.7 2区 工程技术
Fuel Processing Technology Pub Date : 2025-11-15 Epub Date: 2025-09-12 DOI: 10.1016/j.fuproc.2025.108329
Yueming Liu, Shuqin Liu, Zihe Liu, Xuan Li, Jiahong Cao, Chuan Qi, Weibin Wang
{"title":"Pore structure evolution of semi-coke under steam atmosphere in the context of deep underground coal gasification","authors":"Yueming Liu,&nbsp;Shuqin Liu,&nbsp;Zihe Liu,&nbsp;Xuan Li,&nbsp;Jiahong Cao,&nbsp;Chuan Qi,&nbsp;Weibin Wang","doi":"10.1016/j.fuproc.2025.108329","DOIUrl":"10.1016/j.fuproc.2025.108329","url":null,"abstract":"<div><div>Underground coal gasification (UCG) is one of the important ways for in-situ clean conversion of deep coal resources. Affected by groundwater influx, steam gasification becomes the dominant reaction for syngas production in the UCG process. This paper investigates the pressurized gas production characteristics of semi-coke under steam atmosphere range from atmospheric to 3 MPa. The gasified residual coke is characterized by N<sub>2</sub> adsorption-desorption, SEM, AFM, and Raman spectroscopy to analyze the evolution of pore structure and functional groups of semi-coke with changes in pressure and carbon conversion rate. The results show that the action of steam leads to the development of abundant microporous structures below 1 nm on the semi-coke surface. Under 3 MPa, the specific surface area of micropores increases from 17.64 m<sup>2</sup>/g to 435.46 m<sup>2</sup>/g, which is 4 times that under CO₂ atmosphere. Micropores serve as the main site for the initial reaction of steam gasification. Evolution of semi-coke structure based on functional groups is the result of competition between pressure-dominated chain scission and H radical-dominated polycondensation. The research results provide a theoretical basis for strengthening the hydrogen production process of deep underground coal gasification affected by groundwater.</div></div>","PeriodicalId":326,"journal":{"name":"Fuel Processing Technology","volume":"278 ","pages":"Article 108329"},"PeriodicalIF":7.7,"publicationDate":"2025-11-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145044873","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
Hydrothermal hydrodenitrogenation and hydrodesulfurization over nickel-based catalysts in sub/supercritical water 亚/超临界水中镍基催化剂的水热加氢脱氮和加氢脱硫
IF 7.7 2区 工程技术
Fuel Processing Technology Pub Date : 2025-11-15 Epub Date: 2025-09-16 DOI: 10.1016/j.fuproc.2025.108332
Jie Zhang , Hulin Li , Hao Chen , Hong Zhang , Chuang Yang , Haobo Li
{"title":"Hydrothermal hydrodenitrogenation and hydrodesulfurization over nickel-based catalysts in sub/supercritical water","authors":"Jie Zhang ,&nbsp;Hulin Li ,&nbsp;Hao Chen ,&nbsp;Hong Zhang ,&nbsp;Chuang Yang ,&nbsp;Haobo Li","doi":"10.1016/j.fuproc.2025.108332","DOIUrl":"10.1016/j.fuproc.2025.108332","url":null,"abstract":"<div><div>As an inherent by-product of the petroleum industry, oily sludge has substantial potential as energy resource due to its high oil content and calorific value. The hydrodenitrogenation/hydrodesulfurization of nitrogen/sulfur compounds quinoline and thiophene in oily sludge at sub/supercritical hydrothermal conditions was studied, along with its catalytic properties and reaction mechanism. The effects of nickel-based catalysts, hydrogen sources, and reaction conditions on hydrodenitrogenation (HDN) of quinoline were examined. A reaction kinetic model for quinoline in supercritical water was developed. An experimental investigation on hydrodesulfurization (HDS) of sulfur-containing thiophene was conducted, and the catalytic properties of nickel-based catalysts for simultaneous HDN and HDS of quinoline and thiophene were evaluated. Within 400–440 °C, ethanol was superior to formic acid as hydrogen source. Ni-Co/γ-Al<sub>2</sub>O<sub>3</sub> had the most effective catalytic impact on denitrogenation of quinoline. The conversion efficiency of 5 wt% quinoline reached 94.67 %, while denitrogenation efficiency was 57.08 % at 24 MPa, 440 °C, and 60 min. The hydrogenation and ring-opening steps had significant effects on the overall denitrogenation process. The hydrodesulfurization catalysis from Ni-Mo/γ-Al<sub>2</sub>O<sub>3</sub> was the most prominent for thiophene. At 24 MPa, 440 °C, and 60 min, the desulfurization efficiency of thiophene reached 57.34 %. Desulfurization of thiophene mainly followed the hydrogenation route, with thiophene rings being saturated before desulfurization occurred.</div></div>","PeriodicalId":326,"journal":{"name":"Fuel Processing Technology","volume":"278 ","pages":"Article 108332"},"PeriodicalIF":7.7,"publicationDate":"2025-11-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145106198","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
A comprehensive review of the catalytic transformation for biomass derivatives into high-value fuels and chemicals over bimetallic Ni-Re catalysts 综述了双金属Ni-Re催化剂催化生物质衍生物转化为高价值燃料和化学品的研究进展
IF 7.7 2区 工程技术
Fuel Processing Technology Pub Date : 2025-11-15 Epub Date: 2025-09-04 DOI: 10.1016/j.fuproc.2025.108326
Pratikkumar Lakhani, Atthapon Srifa
{"title":"A comprehensive review of the catalytic transformation for biomass derivatives into high-value fuels and chemicals over bimetallic Ni-Re catalysts","authors":"Pratikkumar Lakhani,&nbsp;Atthapon Srifa","doi":"10.1016/j.fuproc.2025.108326","DOIUrl":"10.1016/j.fuproc.2025.108326","url":null,"abstract":"<div><div>Ni-Re bimetallic catalysts provide an excellent synergy of hydrogenation activity from Ni and oxophilic acidity from ReO<sub>X</sub>, allowing for effective conversion of biomass-derived molecules into fuels and chemicals. This review highlights recent developments in Ni-Re catalyst synthesis, structure-performance relationships, and applications in key transformations such as furfural, 5-hydroxymethylfurfural, and levulinic acid upgrading, and hydrodeoxygenation of fatty acid esters. The discussion highlights bifunctional mechanisms, hydrogen spillover, and metal-support interactions in controlling selectivity. Catalyst deactivation challenges and regeneration strategies are also addressed. Finally, future research directions are suggested with emphasis on atomic-scale catalyst design, integration of green hydrogen, and industrial use in sustainable biorefineries.</div></div>","PeriodicalId":326,"journal":{"name":"Fuel Processing Technology","volume":"278 ","pages":"Article 108326"},"PeriodicalIF":7.7,"publicationDate":"2025-11-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"144988771","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
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