Pub Date : 2025-12-15DOI: 10.1016/j.fuel.2025.138018
Feng Chen , Pan Deng , Jing-Ping Zhao , Zhi-Yang Ren , Tianlong Liu , Xiao-Bo Feng , Jing-Pei Cao
The design and synthesis of directly shaped zeolites via one-step hydrothermal method are attractive for industrial applications. However, realizing zeolites with millimeter level and sufficient mechanical strength remains a formidable challenge. Herein, the mechanically robust FER, MOR, and FER/MOR composite zeolite monoliths about 2 mm spherical monoliths were synthesized by one-setp without bindeless. These millimeter-sized spherical monoliths, assembled from nanosheets and nanorods, combine superior acidity and mass transfer efficiency. The differences in pore structure and acid site distribution between monolithic and conventional binder-based zeolites is elucidate. Over these millimeter-sized spherical monoliths, the DME catalytic performance is surpasses commercial shaped catalysts by 2–3 times. Moreover, regeneration under a low-oxygen atmosphere stabilizes the framework Al and ensures outstanding structural integrity and catalytic durability under cyclic operation. In addition, the influence of pyridine poison the acid site of shanped MOR zeolite is expounded. By finely adjusted the pyridine poison procedure over the MOR millimeter-sized MOR zeolite, the catalyst life can be significantly improved. Our findings provide novel and valuable insights for the design of industrial catalysts in syngas/CO2 to ethanol technology.
{"title":"Millimeter-scale zeolite monoliths via one-step hydrothermal synthesis for enhancing dimethyl ether carbonylation","authors":"Feng Chen , Pan Deng , Jing-Ping Zhao , Zhi-Yang Ren , Tianlong Liu , Xiao-Bo Feng , Jing-Pei Cao","doi":"10.1016/j.fuel.2025.138018","DOIUrl":"10.1016/j.fuel.2025.138018","url":null,"abstract":"<div><div>The design and synthesis of directly shaped zeolites via one-step hydrothermal method are attractive for industrial applications. However, realizing zeolites with millimeter level and sufficient mechanical strength remains a formidable challenge. Herein, the mechanically robust FER, MOR, and FER/MOR composite zeolite monoliths about 2 mm spherical monoliths were synthesized by one-setp without bindeless. These millimeter-sized spherical monoliths, assembled from nanosheets and nanorods, combine superior acidity and mass transfer efficiency. The differences in pore structure and acid site distribution between monolithic and conventional binder-based zeolites is elucidate. Over these millimeter-sized spherical monoliths, the DME catalytic performance is surpasses commercial shaped catalysts by 2–3 times. Moreover, regeneration under a low-oxygen atmosphere stabilizes the framework Al and ensures outstanding structural integrity and catalytic durability under cyclic operation. In addition, the influence of pyridine poison the acid site of shanped MOR zeolite is expounded. By finely adjusted the pyridine poison procedure over the MOR millimeter-sized MOR zeolite, the catalyst life can be significantly improved. Our findings provide novel and valuable insights for the design of industrial catalysts in syngas/CO<sub>2</sub> to ethanol technology.</div></div>","PeriodicalId":325,"journal":{"name":"Fuel","volume":"411 ","pages":"Article 138018"},"PeriodicalIF":7.5,"publicationDate":"2025-12-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145750040","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Improving the catalytic efficiency and catalyst life of Pt/Al2O3 catalyst for methylcyclohexane dehydrogenation is of great significance for the study of organic liquid hydrogen storage. In this work, the promotion effects of Ga and Ce on the substantial improvement of catalytic stability and activity over the Pt/Al2O3 during the methylcyclohexane dehydrogenation were investigated. The catalyst with optimizing Ga and Ce loading (1.5 wt%) exhibits ∼99.76 % selectivity and H2 evolution rate of 2102 mol/gPt/min at 300 °C. In 100 h long-time reaction, the conversion of methylcyclohexane remains around 75 % with no significant decrease. The characterization results show that introducing proper amount of Ga and Ce helps Ga3+ cations incorporate into the lattice structure of CeO2 that increase concentration of oxygen vacancies and CeO2 reducibility in the catalyst, which boost the capability of methylcyclohexane dehydrogenation and tolerance for coke formation. Thus, the excellent stability and activity are achieved over the GaCe-modified catalyst. This study may share new light on the rational construction of highly efficient Pt-based catalysts for methylcyclohexane dehydrogenation.
{"title":"Enhancing the efficiency of methylcyclohexane dehydrogenation of Pt/Al2O3 catalyst doped by Ga and Ce adding: Unraveling the role of oxygen vacancy","authors":"Chen-Xu Chen , Jing-Pei Cao , Nai-Yu Yao , Wen Tang , Wei Jiang , Chuang Zhang , Xiao-Yan Zhao , Xiao-Yu Qiao , Tungalagtamir Bold","doi":"10.1016/j.fuel.2025.137981","DOIUrl":"10.1016/j.fuel.2025.137981","url":null,"abstract":"<div><div>Improving the catalytic efficiency and catalyst life of Pt/Al<sub>2</sub>O<sub>3</sub> catalyst for methylcyclohexane dehydrogenation is of great significance for the study of organic liquid hydrogen storage. In this work, the promotion effects of Ga and Ce on the substantial improvement of catalytic stability and activity over the Pt<strong>/</strong>Al<sub>2</sub>O<sub>3</sub> during the methylcyclohexane dehydrogenation were investigated. The catalyst with optimizing Ga and Ce loading (1.5 wt%) exhibits ∼99.76 % selectivity and H<sub>2</sub> evolution rate of 2102 mol/g<sub>Pt</sub>/min at 300 °C. In 100 h long-time reaction, the conversion of methylcyclohexane remains around 75 % with no significant decrease. The characterization results show that introducing proper amount of Ga and Ce helps Ga<sup>3+</sup> cations incorporate into the lattice structure of CeO<sub>2</sub> that increase concentration of oxygen vacancies and CeO<sub>2</sub> reducibility in the catalyst, which boost the capability of methylcyclohexane dehydrogenation and tolerance for coke formation. Thus, the excellent stability and activity are achieved over the GaCe-modified catalyst. This study may share new light on the rational construction of highly efficient Pt-based catalysts for methylcyclohexane dehydrogenation.</div></div>","PeriodicalId":325,"journal":{"name":"Fuel","volume":"410 ","pages":"Article 137981"},"PeriodicalIF":7.5,"publicationDate":"2025-12-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145788180","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-12-15DOI: 10.1016/j.fuel.2025.138016
Rongjing Wang , Xiaolong Xu , Guangxuan Chen , Yunkun Zhao , Yibo Guo , Shuting Min , Tingting Xu , Xun Wang
This study systematically evaluated the reactivity of four iron-based oxygen carriers (OCs) in a pilot-scale methane reforming coupled with thermochemical water-splitting system for hydrogen and syngas co-production. The oxygen carriers were synthesized with a kilogram-scale mechanical method. Two high-entropy OCs, (Ni0.2Co0.2Mg0.2Cu0.2Ca0.2)Fe2O4 (HEO1) and (Ni0.2Co0.2Mg0.2Cr0.2Mn0.2)Fe2O4 (HEO2), showed good cycling stability during a 50-hour test. HEO1 showed a higher oxygen transfer capacity (OTC) of 24.6 % and better carbon-resistance performance. It reached the highest hydrogen yield of 10.40 mmol/g-OC and a hydrogen purity of 98.75 %. HEO2 showed slight carbon deposition during methane reforming in the fuel reactor (FR), which led to a lower hydrogen purity of 93.37 % and a hydrogen yield of 9.52 mmol/g-OC. The composite OC 0.3NiFe2O4/0.7SrFe12O19 (Sr-Ni-Fe-O) showed a high hydrogen purity of 98.60 % but a lower hydrogen yield of 6.90 mmol/g-OC. This was attributed to its low lattice oxygen activity, which hindered deep reduction during the FR stage. Ca2Ni0.75Fe1.25O5 (Ca-Ni-Fe-O) tended to produce carbon deposition in the FR and was more suitable for syngas production. It reached the highest syngas yield of 1.97 L/LCH4 because of its low lattice oxygen activity and low OTC. Overall, HEO1 showed superior cyclic stability and sintering resistance, providing a strong foundation for the scalable application of high-entropy oxides in thermochemical hydrogen production.
{"title":"Experimental study on methane reforming coupled with thermochemical water splitting using kilogram scale oxygen carriers for co-production of hydrogen and syngas","authors":"Rongjing Wang , Xiaolong Xu , Guangxuan Chen , Yunkun Zhao , Yibo Guo , Shuting Min , Tingting Xu , Xun Wang","doi":"10.1016/j.fuel.2025.138016","DOIUrl":"10.1016/j.fuel.2025.138016","url":null,"abstract":"<div><div>This study systematically evaluated the reactivity of four iron-based oxygen carriers (OCs) in a pilot-scale methane reforming coupled with thermochemical water-splitting system for hydrogen and syngas co-production. The oxygen carriers were synthesized with a kilogram-scale mechanical method. Two high-entropy OCs, (Ni<sub>0.2</sub>Co<sub>0.2</sub>Mg<sub>0.2</sub>Cu<sub>0.2</sub>Ca<sub>0.2</sub>)Fe<sub>2</sub>O<sub>4</sub> (HEO1) and (Ni<sub>0.2</sub>Co<sub>0.2</sub>Mg<sub>0.2</sub>Cr<sub>0.2</sub>Mn<sub>0.2</sub>)Fe<sub>2</sub>O<sub>4</sub> (HEO2), showed good cycling stability during a 50-hour test. HEO1 showed a higher oxygen transfer capacity (OTC) of 24.6 % and better carbon-resistance performance. It reached the highest hydrogen yield of 10.40 mmol/g-OC and a hydrogen purity of 98.75 %. HEO2 showed slight carbon deposition during methane reforming in the fuel reactor (FR), which led to a lower hydrogen purity of 93.37 % and a hydrogen yield of 9.52 mmol/g-OC. The composite OC 0.3NiFe<sub>2</sub>O<sub>4</sub>/0.7SrFe<sub>12</sub>O<sub>19</sub> (Sr-Ni-Fe-O) showed a high hydrogen purity of 98.60 % but a lower hydrogen yield of 6.90 mmol/g-OC. This was attributed to its low lattice oxygen activity, which hindered deep reduction during the FR stage. Ca<sub>2</sub>Ni<sub>0.75</sub>Fe<sub>1.25</sub>O<sub>5</sub> (Ca-Ni-Fe-O) tended to produce carbon deposition in the FR and was more suitable for syngas production. It reached the highest syngas yield of 1.97 L/L<sub>CH4</sub> because of its low lattice oxygen activity and low OTC. Overall, HEO1 showed superior cyclic stability and sintering resistance, providing a strong foundation for the scalable application of high-entropy oxides in thermochemical hydrogen production.</div></div>","PeriodicalId":325,"journal":{"name":"Fuel","volume":"411 ","pages":"Article 138016"},"PeriodicalIF":7.5,"publicationDate":"2025-12-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145799513","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-12-15DOI: 10.1016/j.fuel.2025.137985
Xueling Wei , Youjun Huang , Qiguan Wang , Taotao Ai , Xiangyu Zou , Wenhu Li , Sumin Wang , Weiwei Bao , Jie Han
Direct seawater electrolysis represents a promising technology for large-scale green hydrogen production. In this study, a ruthenium-doped nickel phosphide with phosphorus vacancies (Ru/Ni2Pv/NF) was successfully synthesized through galvanic replacement reaction integrated with plasma-assisted phosphidation and vacancy engineering. The Ru/Ni2Pv/NF demonstrates exceptional oxygen evolution reaction (OER) and hydrogen evolution reaction (HER) performance in seawater splitting. The electrolyzer coupled with Ru/Ni2Pv/NF achieves an industrial current density of 1 A cm−2 at 2.0 V under 1 M KOH mixed seawater. The integration of theoretical calculations and experimental analyses reveals that the synergistic interaction between phosphorus vacancies and Ru effectively modulates the electronic structure of the electrocatalyst, thereby facilitating the formation of active NiOOH species and a protective PO43- anion layer. This study proposes a simple yet effective strategy for the rapid incorporation of dopants and defects to enhance electrocatalytic performance.
海水直接电解是一种很有前途的大规模绿色制氢技术。本研究通过电取代反应结合等离子体辅助磷化和空位工程,成功合成了含磷空位的钌掺杂磷化镍(Ru/Ni2Pv/NF)。Ru/Ni2Pv/NF在海水裂解中表现出优异的析氧反应(OER)和析氢反应(HER)性能。电解槽与Ru/Ni2Pv/NF耦合,在1 M KOH混合海水中,在2.0 V下可获得1 A cm−2的工业电流密度。理论计算和实验分析相结合表明,磷空位和Ru之间的协同作用有效地调节了电催化剂的电子结构,从而促进了活性NiOOH物质和PO43-阴离子保护层的形成。本研究提出了一种简单而有效的快速掺入掺杂剂和缺陷以提高电催化性能的策略。
{"title":"Doping Ru on Ni2P with phosphorus vacancies for overall seawater electrolysis","authors":"Xueling Wei , Youjun Huang , Qiguan Wang , Taotao Ai , Xiangyu Zou , Wenhu Li , Sumin Wang , Weiwei Bao , Jie Han","doi":"10.1016/j.fuel.2025.137985","DOIUrl":"10.1016/j.fuel.2025.137985","url":null,"abstract":"<div><div>Direct seawater electrolysis represents a promising technology for large-scale green hydrogen production. In this study, a ruthenium-doped nickel phosphide with phosphorus vacancies (Ru/Ni<sub>2</sub>P<sub>v</sub>/NF) was successfully synthesized through galvanic replacement reaction integrated with plasma-assisted phosphidation and vacancy engineering. The Ru/Ni<sub>2</sub>P<sub>v</sub>/NF demonstrates exceptional oxygen evolution reaction (OER) and hydrogen evolution reaction (HER) performance in seawater splitting. The electrolyzer coupled with Ru/Ni<sub>2</sub>P<sub>v</sub>/NF achieves an industrial current density of 1 A cm<sup>−2</sup> at 2.0 V under 1 M KOH mixed seawater. The integration of theoretical calculations and experimental analyses reveals that the synergistic interaction between phosphorus vacancies and Ru effectively modulates the electronic structure of the electrocatalyst, thereby facilitating the formation of active NiOOH species and a protective PO<sub>4</sub><sup>3-</sup> anion layer. This study proposes a simple yet effective strategy for the rapid incorporation of dopants and defects to enhance electrocatalytic performance.</div></div>","PeriodicalId":325,"journal":{"name":"Fuel","volume":"411 ","pages":"Article 137985"},"PeriodicalIF":7.5,"publicationDate":"2025-12-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145750037","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-12-15DOI: 10.1016/j.fuel.2025.137979
Yunqi Cao , Haonan Rong , Li Yang , Yifan Ding , Fang Liu , Cheng Zhai
Low calorific value and fluctuation of low-concentration methane (LCM) from coal mines pose awkward challenges for stable combustion and utilization. A gradient catalytic porous media (PM) burner by loading Fe2O3 on the surface of Al2O3 foam ceramics was designed to validate the enhanced combustion stability. The cold startup and combustion characteristics were investigated with different equivalence ratio (φ) and inlet velocity (v), and the heat transfer and reaction mechanisms were revealed based on experimental results. The results indicated that porous media catalytic combustion achieved rapid preheating response (<150 s) in the cold-startup process. The flame variation from surface combustion to submerged combustion reflected the combustion integrity. Fe2O3/Al2O3 had robust mid-to-high temperature reactivity, achieving greater than 98 % CH4 conversion and lower than 5 ppm NOx emissions under all conditions. Flame stabilization occurred optimally at the interface of 20/30 PPI region under φ = 0.40 and v = 11 cm/s, leveraging thermal feedback and flame buffering effects of the gradient porous media structure. Long-term combustion testing verified the system’s stability with high combustion efficiency and low emissions. Mechanistic analysis revealed that oxygen vacancies facilitated efficient activation of CH bonds, FeOAl bonds could inhibit carbon deposition and improved mechanical strength, with the Vickers hardness decreased by less than 50 % compared to fresh catalyst. The synergy between the gradient structure and catalytic reaction improved the combustion stability of LCM, providing a viable solution for the utilization of coal mine methane.
{"title":"Valorization of catalytically improved combustion stability for low-concentration methane in a gradient pore-density porous media burner","authors":"Yunqi Cao , Haonan Rong , Li Yang , Yifan Ding , Fang Liu , Cheng Zhai","doi":"10.1016/j.fuel.2025.137979","DOIUrl":"10.1016/j.fuel.2025.137979","url":null,"abstract":"<div><div>Low calorific value and fluctuation of low-concentration methane (LCM) from coal mines pose awkward challenges for stable combustion and utilization. A gradient catalytic porous media (PM) burner by loading Fe<sub>2</sub>O<sub>3</sub> on the surface of Al<sub>2</sub>O<sub>3</sub> foam ceramics was designed to validate the enhanced combustion stability. The cold startup and combustion characteristics were investigated with different equivalence ratio (<em>φ</em>) and inlet velocity (<em>v</em>), and the heat transfer and reaction mechanisms were revealed based on experimental results. The results indicated that porous media catalytic combustion achieved rapid preheating response (<150 s) in the cold-startup process. The flame variation from surface combustion to submerged combustion reflected the combustion integrity. Fe<sub>2</sub>O<sub>3</sub>/Al<sub>2</sub>O<sub>3</sub> had robust mid-to-high temperature reactivity, achieving greater than 98 % CH<sub>4</sub> conversion and lower than 5 ppm NO<sub>x</sub> emissions under all conditions. Flame stabilization occurred optimally at the interface of 20/30 PPI region under <em>φ</em> = 0.40 and <em>v</em> = 11 cm/s, leveraging thermal feedback and flame buffering effects of the gradient porous media structure. Long-term combustion testing verified the system’s stability with high combustion efficiency and low emissions. Mechanistic analysis revealed that oxygen vacancies facilitated efficient activation of C<img>H bonds, Fe<img>O<img>Al bonds could inhibit carbon deposition and improved mechanical strength, with the Vickers hardness decreased by less than 50 % compared to fresh catalyst. The synergy between the gradient structure and catalytic reaction improved the combustion stability of LCM, providing a viable solution for the utilization of coal mine methane.</div></div>","PeriodicalId":325,"journal":{"name":"Fuel","volume":"411 ","pages":"Article 137979"},"PeriodicalIF":7.5,"publicationDate":"2025-12-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145750038","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
The optimization of an innovative process consisting of chemical absorption–desorption at ambient pressure and temperature with EDTA-Fe/carbonate solutions devoted to biogas upgrading was conducted. The influence of parameters such as the initial pH (9–10), inorganic carbon concentration (IC) (4000–8000 mg/L), biogas flowrate (BF) (30–90 L/d), air flowrate (AF) (300–1500 L/d), L/G ratio (0.7–3) and EDTA-Fe concentration (Fe) (0–30 mM) on biomethane composition was evaluated. In addition, the effect of carbon-coated iron nanoparticles on CO2 absorption performance was investigated. The L/G ratio governed the O2 concentration in the biomethane. Interestingly, the addition of EDTA-Fe was not necessary for the complete removal of H2S from the biogas. BF, AF and IC exerted a significant influence on the biomethane CO2 concentration (BF > AF > IC), while the initial pH induced no effect. On the other hand, the supplementation of iron nanoparticles did not significantly influence on the CO2 absorption performance. The optimal conditions in a 7 L absorption-7 L desorption system were: BF = 90 L/d, AF = 1500 L/d, L/G = 0.7, IC = 8000 mg C/L, initial pH = 9.5 and Fe = 0 mM. Under these operational conditions, the biomethane obtained was free of H2S and average concentrations of CO2, O2, N2 and CH4 of 1.7 ± 0.1 %, 0.7 ± 0.1 %, 2.7 ± 0.5 % and 94.9 ± 0.6 %, respectively, were recorded for 3 weeks of continuous operation. This biomethane complied with the European standard EN 16273 on the biomethane use for injection into natural gas networks.
以EDTA-Fe/碳酸盐溶液为原料,对常压常温化学吸附-解吸工艺进行了优化。考察了初始pH(9 ~ 10)、无机碳浓度(IC) (4000 ~ 8000 mg/L)、沼气流量(BF) (30 ~ 90 L/d)、空气流量(AF) (300 ~ 1500 L/d)、L/G比(0.7 ~ 3)、EDTA-Fe浓度(Fe) (0 ~ 30 mM)等参数对生物甲烷组成的影响。此外,还研究了碳包覆铁纳米颗粒对CO2吸收性能的影响。L/G比值决定了生物甲烷中O2的浓度。有趣的是,EDTA-Fe的加入并不是完全去除沼气中H2S的必要条件。BF、AF和IC对生物甲烷CO2浓度(BF > AF >; IC)有显著影响,而初始pH对生物甲烷CO2浓度没有影响。另一方面,铁纳米颗粒的添加对CO2吸收性能没有显著影响。最优条件7 L absorption-7 L解吸系统:男朋友= 90 L / d,房颤= 1500 L / d, L / G = 0.7, IC C / L = 8000毫克,初始pH = 9.5和铁= 0毫米。在这些操作条件下,获得免费硫化氢和甲烷,平均浓度的二氧化碳,氧气,氮气和CH4 1.7±0.1%,0.7±0.1%,2.7±0.5%和94.9±0.6%,分别记录3周的连续操作。这种生物甲烷符合欧洲标准EN 16273关于生物甲烷用于注入天然气网络。
{"title":"Pilot-scale optimization of a physical–chemical biogas upgrading system based on a high alkalinity absorbent at ambient pressure and temperature","authors":"Edwin G. Hoyos , Saeed Rasekhi , Rogelio Mazaeda , Raúl Muñoz","doi":"10.1016/j.fuel.2025.138010","DOIUrl":"10.1016/j.fuel.2025.138010","url":null,"abstract":"<div><div>The optimization of an innovative process consisting of chemical absorption–desorption at ambient pressure and temperature with EDTA-Fe/carbonate solutions devoted to biogas upgrading was conducted. The influence of parameters such as the initial pH (9–10), inorganic carbon concentration (IC) (4000–8000 mg/L), biogas flowrate (BF) (30–90 L/d), air flowrate (AF) (300–1500 L/d), L/G ratio (0.7–3) and EDTA-Fe concentration (Fe) (0–30 mM) on biomethane composition was evaluated. In addition, the effect of carbon-coated iron nanoparticles on CO<sub>2</sub> absorption performance was investigated. The L/G ratio governed the O<sub>2</sub> concentration in the biomethane. Interestingly, the addition of EDTA-Fe was not necessary for the complete removal of H<sub>2</sub>S from the biogas. BF, AF and IC exerted a significant influence on the biomethane CO<sub>2</sub> concentration (BF > AF > IC), while the initial pH induced no effect. On the other hand, the supplementation of iron nanoparticles did not significantly influence on the CO<sub>2</sub> absorption performance. The optimal conditions in a 7 L absorption-7 L desorption system were: BF = 90 L/d, AF = 1500 L/d, L/G = 0.7, IC = 8000 mg C/L, initial pH = 9.5 and Fe = 0 mM. Under these operational conditions, the biomethane obtained was free of H<sub>2</sub>S and average concentrations of CO<sub>2</sub>, O<sub>2</sub>, N<sub>2</sub> and CH<sub>4</sub> of 1.7 ± 0.1 %, 0.7 ± 0.1 %, 2.7 ± 0.5 % and 94.9 ± 0.6 %, respectively, were recorded for 3 weeks of continuous operation. This biomethane complied with the European standard EN 16273 on the biomethane use for injection into natural gas networks.</div></div>","PeriodicalId":325,"journal":{"name":"Fuel","volume":"411 ","pages":"Article 138010"},"PeriodicalIF":7.5,"publicationDate":"2025-12-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145799510","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-12-15DOI: 10.1016/j.fuel.2025.137926
Weize Chen , Jingchen Cui , Zhenxian Zhang , Qingyang Wang , Pengbo Dong , Xiangyu Meng , Jiangping Tian , Hua Tian , Wuqiang Long , Shiying Liu
Ammonia stands as a pivotal carbon-free energy vector with the potential to decarbonize hard-to-abate sectors like heavy industry and maritime transport. However, its widespread adoption in internal combustion engines is critically challenged by the dual emissions of unburned NH3, a toxic gas, and N2O, a potent greenhouse gas. This study demonstrates a novel diesel multiple injection strategy (first injection and second injection), based on the Jet Controlled Compression Ignition (JCCI) concept, to achieve near-zero emissions in a two-stroke ammonia-diesel engine. The results elucidate that the first injection creates a high-temperature reaction zone and elevates the in-cylinder thermal state, which is essential for robustly igniting the subsequent liquid ammonia spray. The timing and mass of this first injection, coupled with an optimised injection interval, are critical for stabilizing the flame and forming a pervasive high-temperature environment. This environment is key to minimizing incomplete combustion products. Compared to a conventional single-injection strategy, the optimised multi-injection approach enhanced the dominance of diffusion combustion, leading to a marginal improvement in indicated thermal efficiency while achieving drastic emission reductions: unburned NH3 and N2O were reduced by 90 % (to 62 ppm) and 83 % (to 7 ppm), respectively. This work provides a practical and effective combustion management strategy, transforming a fundamental combustion concept (JCCI) into a viable solution for enabling clean ammonia combustion. It thus presents a significant step towards the application of ammonia as a sustainable fuel for high-power energy systems and contributes directly to the goals of the green energy transition.
{"title":"Near-Zero NH3/N2O emissions enabled in two-stroke ammonia-diesel dual-direct-injection engines: an experimental study via synergistic diesel multiple injection strategy","authors":"Weize Chen , Jingchen Cui , Zhenxian Zhang , Qingyang Wang , Pengbo Dong , Xiangyu Meng , Jiangping Tian , Hua Tian , Wuqiang Long , Shiying Liu","doi":"10.1016/j.fuel.2025.137926","DOIUrl":"10.1016/j.fuel.2025.137926","url":null,"abstract":"<div><div>Ammonia stands as a pivotal carbon-free energy vector with the potential to decarbonize hard-to-abate sectors like heavy industry and maritime transport. However, its widespread adoption in internal combustion engines is critically challenged by the dual emissions of unburned NH<sub>3</sub>, a toxic gas, and N<sub>2</sub>O, a potent greenhouse gas. This study demonstrates a novel diesel multiple injection strategy (first injection and second injection), based on the Jet Controlled Compression Ignition (JCCI) concept, to achieve near-zero emissions in a two-stroke ammonia-diesel engine. The results elucidate that the first injection creates a high-temperature reaction zone and elevates the in-cylinder thermal state, which is essential for robustly igniting the subsequent liquid ammonia spray. The timing and mass of this first injection, coupled with an optimised injection interval, are critical for stabilizing the flame and forming a pervasive high-temperature environment. This environment is key to minimizing incomplete combustion products. Compared to a conventional single-injection strategy, the optimised multi-injection approach enhanced the dominance of diffusion combustion, leading to a marginal improvement in indicated thermal efficiency while achieving drastic emission reductions: unburned NH<sub>3</sub> and N<sub>2</sub>O were reduced by 90 % (to 62 ppm) and 83 % (to 7 ppm), respectively. This work provides a practical and effective combustion management strategy, transforming a fundamental combustion concept (JCCI) into a viable solution for enabling clean ammonia combustion. It thus presents a significant step towards the application of ammonia as a sustainable fuel for high-power energy systems and contributes directly to the goals of the green energy transition.</div></div>","PeriodicalId":325,"journal":{"name":"Fuel","volume":"411 ","pages":"Article 137926"},"PeriodicalIF":7.5,"publicationDate":"2025-12-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145799514","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-12-15DOI: 10.1016/j.fuel.2025.138044
Xiaodong You , Zhenjie Sun , Chen Yang , Songtao Wu , Zhenming Li , Jialong Chen , Mingjie Xiong , Guanshuai Zhang , Yuan Liu , Yunpu Wang , Chunlei Gao , Feiqiang Guo
To address the dual challenges of coal gasification fine slag (CGFS) disposal and the demand for efficient catalysts for bio-oil upgrading, this study aimed to synthesize metal-modified Na-X zeolite/carbon composites from CGFS and evaluate their performance in biomass catalytic pyrolysis. The composites were prepared via acid leaching, alkali fusion, and hydrothermal crystallization, followed by impregnation with different metals (Ni, Co, Fe, Ca). Characterization revealed that metal modification dramatically reconstructed the acid properties, eliminating weak/medium sites while generating abundant strong Lewis acid sites, with the total strong acid amount increasing from 0.289 mmol/g (parent support) to 0.563 mmol/g (GZ-Co). In the catalytic fast pyrolysis of pine wood at 600 °C, metal modification significantly enhanced deoxygenation. Notably, the optimal GZ-Ni catalyst increased the gas yield from 37.23 wt% (non-catalytic) to 53.16 wt%, while the relative hydrocarbon content in bio-oil rose substantially from 15 % to 38 %. The strong Lewis acidity introduced by the metals was identified as the key factor promoting decarbonylation, decarboxylation, and aromatization reactions. Although reversible deactivation occurred due to coking, regeneration effectively restored catalytic activity. This work provides not only a sustainable “waste-to-catalyst” strategy for CGFS valorization but also elucidates the critical role of tailored strong Lewis acidity in designing efficient catalysts for bio-oil upgrading.
{"title":"Metal-modified Na-X zeolite/carbon composites derived from coal gasification fine slag for enhanced catalytic pyrolysis of biomass","authors":"Xiaodong You , Zhenjie Sun , Chen Yang , Songtao Wu , Zhenming Li , Jialong Chen , Mingjie Xiong , Guanshuai Zhang , Yuan Liu , Yunpu Wang , Chunlei Gao , Feiqiang Guo","doi":"10.1016/j.fuel.2025.138044","DOIUrl":"10.1016/j.fuel.2025.138044","url":null,"abstract":"<div><div>To address the dual challenges of coal gasification fine slag (CGFS) disposal and the demand for efficient catalysts for bio-oil upgrading, this study aimed to synthesize metal-modified Na-X zeolite/carbon composites from CGFS and evaluate their performance in biomass catalytic pyrolysis. The composites were prepared via acid leaching, alkali fusion, and hydrothermal crystallization, followed by impregnation with different metals (Ni, Co, Fe, Ca). Characterization revealed that metal modification dramatically reconstructed the acid properties, eliminating weak/medium sites while generating abundant strong Lewis acid sites, with the total strong acid amount increasing from 0.289 mmol/g (parent support) to 0.563 mmol/g (GZ-Co). In the catalytic fast pyrolysis of pine wood at 600 °C, metal modification significantly enhanced deoxygenation. Notably, the optimal GZ-Ni catalyst increased the gas yield from 37.23 wt% (non-catalytic) to 53.16 wt%, while the relative hydrocarbon content in bio-oil rose substantially from 15 % to 38 %. The strong Lewis acidity introduced by the metals was identified as the key factor promoting decarbonylation, decarboxylation, and aromatization reactions. Although reversible deactivation occurred due to coking, regeneration effectively restored catalytic activity. This work provides not only a sustainable “waste-to-catalyst” strategy for CGFS valorization but also elucidates the critical role of tailored strong Lewis acidity in designing efficient catalysts for bio-oil upgrading.</div></div>","PeriodicalId":325,"journal":{"name":"Fuel","volume":"411 ","pages":"Article 138044"},"PeriodicalIF":7.5,"publicationDate":"2025-12-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145799451","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-12-15DOI: 10.1016/j.fuel.2025.138009
Suleyman I. Allakhverdiev
The growing demand for low-carbon energy carriers has renewed interest in photocatalytic hydrogen production as a viable solar-to-fuel route. Natural photosynthesis offers an elegant blueprint for coupling light harvesting, charge separation and catalysis, but its direct exploitation for hydrogen evolution is limited by low efficiency and restricted control over the underlying interfaces. Semi-artificial and artificial photosynthetic platforms address these limitations by combining biological or bio-inspired catalysts with engineered inorganic light harvesters and support architectures. This review focuses on artificial photosynthetic interfaces for photocatalytic hydrogen production, using semi-artificial systems as a conceptual and experimental bridge. We first outline the continuum from natural to semi-artificial and fully artificial photosynthesis, highlighting how the degree and nature of interface control evolve across these platforms. We then analyse semi-artificial architectures to extract design principles for soft bio–inorganic interfaces that wire inorganic photocatalysts to microbial cells, sub-cellular compartments and isolated enzymes. Building on these insights, we discuss artificial photosynthetic systems in terms of their key interfacial motifs, including semiconductor–semiconductor and semiconductor–metal junctions, cocatalyst-semiconductor contacts and solid–liquid boundaries that govern charge separation, redox selectivity and mass transport. Finally, we identify cross-cutting challenges related to reproducibility, operational durability, scalability and the use of earth-abundant components. By framing recent progress through the lens of interface engineering, this review provides a unified basis for the rational design of next-generation hydrogen-producing photosystems.
{"title":"Artificial photosynthetic interfaces for enhanced photocatalytic hydrogen generation","authors":"Suleyman I. Allakhverdiev","doi":"10.1016/j.fuel.2025.138009","DOIUrl":"10.1016/j.fuel.2025.138009","url":null,"abstract":"<div><div>The growing demand for low-carbon energy carriers has renewed interest in photocatalytic hydrogen production as a viable solar-to-fuel route. Natural photosynthesis offers an elegant blueprint for coupling light harvesting, charge separation and catalysis, but its direct exploitation for hydrogen evolution is limited by low efficiency and restricted control over the underlying interfaces. Semi-artificial and artificial photosynthetic platforms address these limitations by combining biological or bio-inspired catalysts with engineered inorganic light harvesters and support architectures. This review focuses on artificial photosynthetic interfaces for photocatalytic hydrogen production, using semi-artificial systems as a conceptual and experimental bridge. We first outline the continuum from natural to semi-artificial and fully artificial photosynthesis, highlighting how the degree and nature of interface control evolve across these platforms. We then analyse semi-artificial architectures to extract design principles for soft bio–inorganic interfaces that wire inorganic photocatalysts to microbial cells, sub-cellular compartments and isolated enzymes. Building on these insights, we discuss artificial photosynthetic systems in terms of their key interfacial motifs, including semiconductor–semiconductor and semiconductor–metal junctions, cocatalyst-semiconductor contacts and solid–liquid boundaries that govern charge separation, redox selectivity and mass transport. Finally, we identify cross-cutting challenges related to reproducibility, operational durability, scalability and the use of earth-abundant components. By framing recent progress through the lens of interface engineering, this review provides a unified basis for the rational design of next-generation hydrogen-producing photosystems.</div></div>","PeriodicalId":325,"journal":{"name":"Fuel","volume":"411 ","pages":"Article 138009"},"PeriodicalIF":7.5,"publicationDate":"2025-12-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145799503","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-12-15DOI: 10.1016/j.fuel.2025.137971
Amir Abdolhosseinnejad , Sajad Rezazadeh , H. Rostamnejad Takleh , Milad Razbin
While solid oxide fuel cells (SOFCs) offer strong performance, the selection of appropriate subsystems for waste-heat recovery and the reliable prediction of overall system behavior remain insufficiently addressed in the literature. Therefore, a novel CH4-fueled, SOFC-based hybrid power and cooling system, integrating an organic flash cycle and an ejector refrigeration unit to simultaneously generate electricity and dual-level cooling, is proposed. The configuration harnesses high-grade exhaust energy from the SOFC without relying on mechanical compressors, thereby improving energy recovery and operational efficiency. A comprehensive framework combining thermodynamic, economic, and environmental analyses is applied to evaluate system performance. Artificial neural networks trained on response surface methodology data are employed to predict system outputs, while genetic algorithms are used to optimize key design parameters under multi-objective scenarios. The main objectives are to maximize thermal efficiency, minimize levelized cost of system (), and reduce emitted rate of CO2. Numerical results show that thermal efficiency improves to 83.1 % and exergy efficiency reaches 44.9 %. The decreases by more than 15 %, while emitted rate of CO2 is reduced by 11.4 %. Exergy analysis reveals that the SOFC and thermoelectric generator are the dominant sources of irreversibility. From an economic perspective, optimization enhances net present value by 39.5 % and shortens the payback period from 7.48 to 6.39 years.
{"title":"Performance prediction and multi-objective optimization of a CH4-fueled SOFC power/cooling system using ANN–GA: thermodynamic, economic, and environmental evaluation","authors":"Amir Abdolhosseinnejad , Sajad Rezazadeh , H. Rostamnejad Takleh , Milad Razbin","doi":"10.1016/j.fuel.2025.137971","DOIUrl":"10.1016/j.fuel.2025.137971","url":null,"abstract":"<div><div>While solid oxide fuel cells (SOFCs) offer strong performance, the selection of appropriate subsystems for waste-heat recovery and the reliable prediction of overall system behavior remain insufficiently addressed in the literature. Therefore, a novel CH<sub>4</sub>-fueled, SOFC-based hybrid power and cooling system, integrating an organic flash cycle and an ejector refrigeration unit to simultaneously generate electricity and dual-level cooling, is proposed. The configuration harnesses high-grade exhaust energy from the SOFC without relying on mechanical compressors, thereby improving energy recovery and operational efficiency. A comprehensive framework combining thermodynamic, economic, and environmental analyses is applied to evaluate system performance. Artificial neural networks trained on response surface methodology data are employed to predict system outputs, while genetic algorithms are used to optimize key design parameters under multi-objective scenarios. The main objectives are to maximize thermal efficiency, minimize levelized cost of system (<span><math><mrow><mi>L</mi><mi>C</mi><mi>O</mi><mi>S</mi></mrow></math></span>), and reduce emitted rate of CO<sub>2</sub>. Numerical results show that thermal efficiency improves to 83.1 % and exergy efficiency reaches 44.9 %. The <span><math><mrow><mi>L</mi><mi>C</mi><mi>O</mi><mi>S</mi></mrow></math></span> decreases by more than 15 %, while emitted rate of CO<sub>2</sub> is reduced by 11.4 %. Exergy analysis reveals that the SOFC and thermoelectric generator are the dominant sources of irreversibility. From an economic perspective, optimization enhances net present value by 39.5 % and shortens the payback period from 7.48 to 6.39 years.</div></div>","PeriodicalId":325,"journal":{"name":"Fuel","volume":"411 ","pages":"Article 137971"},"PeriodicalIF":7.5,"publicationDate":"2025-12-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145750026","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":1,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}