Fuel Processing Technology最新文献

{"title":"Time-dependent evolution of morphologies and lattice defects in hydrothermal synthesized ceria-zirconia solid solutions for catalytic combustion of diesel soot","authors":"Zhengzheng Yang ,&nbsp;Zhi Chen ,&nbsp;Na Zhang ,&nbsp;Yang Zhou ,&nbsp;Dezhou Luo ,&nbsp;Tai Jin ,&nbsp;Huangwei Zhang","doi":"10.1016/j.fuproc.2025.108294","DOIUrl":"10.1016/j.fuproc.2025.108294","url":null,"abstract":"<div><div>In this work, the physical-chemical and morphological evolution of CeO₂-ZrO₂ solid solutions caused by hydrothermal processing time, and its effects on catalytic diesel soot elimination were studied. SEM and TEM results show that the CeO₂-ZrO₂ nanocrystal particles gradually aggregate with the extension of hydrothermal processing time. A moderate hydrothermal processing time can facilitate the engineering of catalyst morphology at micronmeter scale, however, excessive hydrothermal synthesis time would contrarily destroy the micrometer scaled catalyst morphological structure. The result of XPS, O₂-TPD and H₂-TPR analysis indicates that the hydrothermal synthesis process is conducive to generating lattice defects (oxygen vacancies) of CeO₂-ZrO₂ solid solution. This is a key factor for enhancing the concentration of surface-active oxygen species. The CeO₂-ZrO₂ catalyst prepared by 48 h of hydrothermal processing time (CZ-48 h) exhibits the highest concentration of surface-active oxygen species and oxygen vacancies. Interestingly, the CeO₂-ZrO₂ catalyst synthesized by 6 h of hydrothermal processing time (CZ-6 h) exhibits oxygen vacancy and surface-active oxygen levels that are close to the CZ-48 h, which is obviously more than the traditional co-precipitation CeO₂-ZrO₂ catalyst (CZ-0 h). The soot catalytic elimination performance of the CZ-6 h is also significantly superior to that of the CZ-0 h catalyst. Therefore, this study suggests that the short-time hydrothermal processing is an effective and low-cost strategy to create more oxygen vacancies and improve catalytic performance of CeO₂-ZrO₂ solid solution.</div></div>","PeriodicalId":326,"journal":{"name":"Fuel Processing Technology","volume":"276 ","pages":"Article 108294"},"PeriodicalIF":7.2,"publicationDate":"2025-07-23","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"144686155","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}

{"title":"Analysis of unburned hydrocarbon species for air and oxy-fuel flames in a semi-industrial combustion chamber using Fourier Transform Infrared Spectroscopy","authors":"D. König,&nbsp;J. Ströhle,&nbsp;B. Epple","doi":"10.1016/j.fuproc.2025.108283","DOIUrl":"10.1016/j.fuproc.2025.108283","url":null,"abstract":"<div><div>The combustion of biomass in an oxy-fuel atmosphere shows significant differences compared to air combustion, primarily due to the changes in gas properties caused by CO₂. While multiple studies have analyzed aspects such as flow field, temperature distribution, and CO occurrence in the flame, this study provides a comprehensive analysis of the occurrence of short unburned hydrocarbons ( <figure><img></figure> ) and aromatic compounds like benzene in both oxy-fuel and air flames. Short chained hydrocarbons are known as a significant group of molecules for cracking longer hydrocarbons and thus influencing the reaction rate. Simultaneously those species have also a big influence on the formation of aromatic compounds, whereas aromatic structures favor the formation of soot and tar. For this purpose, three different oxygen contents in the oxidizer, ranging from 27% to 33%, are compared with an air flame in a semi-industrial combustion chamber equipped with flue gas recirculation and a thermal power of up to 670<!--> <!-->k<span><math><mrow><mi>W</mi><mtext>th</mtext></mrow></math></span>. The gas species are analyzed using a Fourier Transform Infrared Spectroscopy analyzer (FTIR) and a suction probe to extract the measurement gas from different radial positions in the flame. The results show that the upper part of the flame along the center line in the oxy-fuel case reveals an extended volatile release and pyrolysis due to the availability of CO₂ and partially higher temperatures, leading to an increase in CO and shorter hydrocarbons. As the radial distance from the center line extends, the occurrence of hydrocarbons is mainly dominated by lean combustion reactions. This trend is consistent across all oxygen concentrations in the oxidizer stream during oxy-fuel combustion. At greater distances from the burner plane, the air case and the oxy-fuel condition with 33% oxygen concentration show the highest similarities in the concentrations of unburned hydrocarbons. The analysis of aromatic compounds reveals significant changes in the upper part of the flame, which can be attributed to the influence of CO₂ on the formation of shorter hydrocarbons and the enhanced tar cracking mechanism in the oxy-fuel case.</div></div>","PeriodicalId":326,"journal":{"name":"Fuel Processing Technology","volume":"276 ","pages":"Article 108283"},"PeriodicalIF":7.2,"publicationDate":"2025-07-23","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"144687406","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}

{"title":"Performance evaluation of inexpensive composite copper/iron ore oxygen carriers produced by industrial granulation in chemical looping combustion of coke oven gas","authors":"Xinghe Liu ,&nbsp;Xinhua Lai ,&nbsp;Yandong Li ,&nbsp;Cao Kuang ,&nbsp;Haiying Zhao ,&nbsp;Mengshuang Li ,&nbsp;Rongchao Li ,&nbsp;Panlei Wang ,&nbsp;Jinchen Ma ,&nbsp;Chaohe Zheng ,&nbsp;Haibo Zhao","doi":"10.1016/j.fuproc.2025.108293","DOIUrl":"10.1016/j.fuproc.2025.108293","url":null,"abstract":"<div><div>Chemical looping combustion (CLC) is a promising technology with the potential to achieve dual objectives of coke oven gas (COG) efficient utilization and reduction of CO₂ emissions in the steel industry. In this work, two inexpensive composite oxygen carriers, CuFe20M (16 wt% copper ore, 64 wt% iron ore, 20 wt% montmorillonite) and CuFe20C (16 wt% copper ore, 64 wt% iron ore, 20 wt% cement), are prepared at a large scale by the extrusion-spheronization and hydroforming methods, respectively. Its combustion performance is comprehensively evaluated using coke oven gas as the fuel in a fixed-bed reactor. The results show that the selection of an appropriate reaction temperature significantly influences the performance of the oxygen carriers. The CH₄ conversion of CuFe20M and CuFe20C reaches the maximum of 95.90 % and 96.72 % at 900 °C, respectively. The CO conversion is not sensitive to temperature change. Excessively high reaction temperatures (&gt;900 °C) lead to a noticeable increase in carbon deposition, resulting in a decline in carbon capture efficiency. Increasing the fuel gas flow rate will suppress the carbon deposition and improve the carbon capture efficiency. Correspondingly, shortening the reaction time will lead to the decrease of CO₂ yield. Long-period CLC tests of COG reveal that the hydroforming-derived CuFe20C oxygen carrier exhibits excellent stability and reactivity compared to the extrusion-spheronization-derived CuFe20M oxygen carrier. Under the optimal operating conditions, the average CH₄ conversion and CO conversion of the CuFe20C are 98.24 % and 95.35 %, respectively. Moreover, CuFe20C exhibits higher CO₂ yield, carbon capture efficiency, and lower carbon deposition. This work provides support for the application of inexpensive composite oxygen carriers (preferably, CuFe20C) in the CLC of COG.</div></div>","PeriodicalId":326,"journal":{"name":"Fuel Processing Technology","volume":"276 ","pages":"Article 108293"},"PeriodicalIF":7.2,"publicationDate":"2025-07-23","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"144686154","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}

{"title":"Analysis of a methanol synthesis reactor operating in non-isothermal cooling conditions","authors":"Grazia Leonzio ,&nbsp;Giovanni Manenti ,&nbsp;Marcello Maria Bozzini ,&nbsp;Roberto Baratti ,&nbsp;Flavio Manenti","doi":"10.1016/j.fuproc.2025.108288","DOIUrl":"10.1016/j.fuproc.2025.108288","url":null,"abstract":"<div><div>Productivity and energy efficiency of industrial units for methanol synthesis strongly depend on adopted configuration for the synthesis reactor(s). Several configurations are described in literature and are commercially available.</div><div>In this work, a reactor configuration of shell-and-tube type, with catalyst on tube-side and coolant on shell-side, and with the shell-side split into two zones (double-zone methanol reactor - DZMR) is described. Such a DZMR allows installing shell-side cooling conditions that are overall non-isothermal; specifically, one shell-side zone operates in isothermal conditions whereas the other shell-side zone operates in non-isothermal conditions. Accordingly, the present work analyzes and compares the DZMR productivity under different shell-side operating conditions, with the thermal oil used as shell-side coolant. Analysis and comparison are carried out by modelling a small-scale DZMR: productivity, yield and carbon conversion are evaluated by means of process modelling in Aspen Plus software.</div><div>Results show that a DZMR with overall non-isothermal shell-side cooling conditions has a high efficiency: methanol productivity (328 tons of MeOH per year), yield and conversion (41 %) are the highest, energy consumption is the lowest and required coolant flowrate is the smallest. The DZMR here described realizes to be operationally flexible and more efficient than conventional shell-and-tube type isothermal reactors.</div></div>","PeriodicalId":326,"journal":{"name":"Fuel Processing Technology","volume":"276 ","pages":"Article 108288"},"PeriodicalIF":7.2,"publicationDate":"2025-07-18","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"144654750","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}

{"title":"Optimal design of catalytic reactors for direct biogas methanation through thermodynamic analysis and 2-D reactor modeling","authors":"Emanuele Giglio ,&nbsp;Paolo Bruno ,&nbsp;Enrico Catizzone ,&nbsp;Girolamo Giordano ,&nbsp;Massimo Migliori","doi":"10.1016/j.fuproc.2025.108287","DOIUrl":"10.1016/j.fuproc.2025.108287","url":null,"abstract":"<div><div>Catalytic methanation upgrades biogas by reacting it with hydrogen. Thermodynamic analysis of a two-step adiabatic process explored temperature control (below 550 °C for catalyst stability). Reactant staging proved insufficient for hot spot management. Product recycling in the first reactor effectively controlled temperature and produced synthetic natural gas (SNG) approaching grid quality. A two-dimensional model of cooled multi-tubular reactors revealed significant radial thermal gradients. A once-through configuration exceeded the temperature limit despite cooling. Reactant staging failed to simultaneously control temperature and achieve targeted conversion. Conversely, product recycling successfully addressed both constraints. Two configurations were proposed: stoichiometric hydrogen (STOIC) and hydrogen-deficient (H-DEF). Optimized reactor designs, employing a 0.30–0.35 recirculation ratio, were developed for both. The STOIC configuration required 18 parallel tubes for the first reactor and 33 for the second. The H-DEF unit utilized 22 tubes in both reactors. These findings highlight product recycling as a viable strategy for efficient and controlled biogas upgrading via catalytic methanation in multi-tubular reactors.</div></div>","PeriodicalId":326,"journal":{"name":"Fuel Processing Technology","volume":"276 ","pages":"Article 108287"},"PeriodicalIF":7.2,"publicationDate":"2025-07-17","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"144654751","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}

{"title":"Unraveling the pivotal role of amylopectin in enhancing hydrothermal stability and filtration control of native corn starch-based drilling fluids for decarbonization","authors":"Fuchang You ,&nbsp;Lei Pu ,&nbsp;Yu Wu ,&nbsp;Yancheng Zheng","doi":"10.1016/j.fuproc.2025.108289","DOIUrl":"10.1016/j.fuproc.2025.108289","url":null,"abstract":"<div><div>Enhanced utilization of native starch offers a promising approach to improving energy efficiency and advancing decarbonization, thereby fostering sustainable and eco-friendly practices in petroleum extraction. However, previous studies suggest limited high-temperature potential of native starch in water-based drilling fluids (WBDFs), mainly due to insufficient research on amylose-to-amylopectin ratios. This study investigates the hydrothermal stability and filtration control performance of corn starches with different amylose-to-amylopectin ratios in WBDFs to address this issue. The results demonstrate that amylopectin content significantly influences the hydrothermal stability and filtration control performance of WBDFs. Waxy corn starch, with 100 % amylopectin content, exhibits excellent performance, achieving a filtration loss of only 7.2 mL even at 160 °C. In contrast, as the amylopectin content decreases, the temperature resistance of normal corn starch declines below 140 °C, while high-amylose corn starch shows poor filtration control even at 120 °C. The key factor contributing to these differences is the amylopectin content. The “clustered or chrysanthemum-like” structure and multi-branched chains of amylopectin enhance bentonite interactions, improving colloidal stability and particle distribution. Slower degradation of amylopectin also boosts hydrothermal stability and dense mud cake formation. The findings of this study provide a theoretical framework for utilizing native starch in WBDFs.</div></div>","PeriodicalId":326,"journal":{"name":"Fuel Processing Technology","volume":"276 ","pages":"Article 108289"},"PeriodicalIF":7.2,"publicationDate":"2025-07-14","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"144613999","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}

{"title":"Hollow carbon spheres as catalyst support for Fischer-Tropsch synthesis: synthesis techniques, optimization strategies, and future research","authors":"Tshepo Molefe ,&nbsp;Yao Jiang ,&nbsp;Alice Magubane ,&nbsp;Liberty Mguni ,&nbsp;Ludwe Sikeyi ,&nbsp;Cairong Jiang ,&nbsp;Xinying Liu ,&nbsp;Yali Yao","doi":"10.1016/j.fuproc.2025.108285","DOIUrl":"10.1016/j.fuproc.2025.108285","url":null,"abstract":"<div><div>The potential of hollow carbon spheres (HCS) as catalyst supports, particularly in the Fischer-Tropsch synthesis (FTS) process, is examined in this review. These materials are presently attracting great attention due to their unique properties such as encapsulation ability, controllable permeability, surface functionality, high surface-to-volume ratios, and excellent chemical and thermal stabilities. FTS is a pivotal technology for converting carbon monoxide and hydrogen into synthetic fuels and chemicals, but it requires the creation of effective catalyst supports. This review describes the structural benefits and chemical stability of HCS by looking at a wide range of research, emphasizing its effectiveness in comparison to conventional catalyst supports. A critical analysis of the synthesis techniques, optimization plans, and future research avenues sheds light on how HCS can improve catalytic effectiveness and reaction results in FTS. The primary objective of this effort is to stimulate additional research and development in catalyst support materials, paving a path for more sustainable and economically viable processes in the energy sector.</div></div>","PeriodicalId":326,"journal":{"name":"Fuel Processing Technology","volume":"276 ","pages":"Article 108285"},"PeriodicalIF":7.2,"publicationDate":"2025-07-11","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"144596580","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}

{"title":"Study on optimization of exhaust gas purification device and CO catalytic elimination of industrial transport vehicles","authors":"Xiaoyu Chen ,&nbsp;Yating Liu ,&nbsp;Jiaxin Shi ,&nbsp;Le Li ,&nbsp;Shuo Gao ,&nbsp;Junyi Li ,&nbsp;Jia Li ,&nbsp;Yu Zhang ,&nbsp;Yichao Lin","doi":"10.1016/j.fuproc.2025.108286","DOIUrl":"10.1016/j.fuproc.2025.108286","url":null,"abstract":"<div><div>To address the issue of excessive CO emissions in the exhaust of explosion-proof diesel vehicles used in mining operations, this study developed and optimized an exhaust CO purification device featuring a Co₃O₄ monolithic catalyst core. The internal structure and external water-cooling system of the device were refined through numerical simulation. Field tests demonstrated that when the vehicle was equipped with the exhaust gas purification device, the maximum CO removal efficiency reached 97.7 %. During underground operations, the highest CO purification efficiency reached 64 %, while during coal shoveling activities, the average CO purification efficiency was 52.2 %. The device is of great significance for improving the underground working environment and ensuring the life, health and safety of personnel.</div></div>","PeriodicalId":326,"journal":{"name":"Fuel Processing Technology","volume":"276 ","pages":"Article 108286"},"PeriodicalIF":7.2,"publicationDate":"2025-07-09","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"144579739","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}

{"title":"A techno-economic assessment of power-to-gas to produce hydrogen by TALOS","authors":"Matthew Hawkins ,&nbsp;Daniel Mills ,&nbsp;Muzaffar Bandarkar ,&nbsp;Peter Ackroyd ,&nbsp;Farouq Saifudin ,&nbsp;George Aggidis ,&nbsp;Giuseppe Bagnato","doi":"10.1016/j.fuproc.2025.108282","DOIUrl":"10.1016/j.fuproc.2025.108282","url":null,"abstract":"<div><div>The transition toward a low-carbon energy system encourages academicians to research innovative energy solutions. Diversifying renewable energy sources ensures the effort to fulfil market demand comes into being. This study presents a comprehensive techno-economic assessment of Power-to-Gas technology to produce hydrogen using TALOS-WEC as energy converter from wave energy to electricity. Power-to-Gas is a technology that converts electrical energy into gaseous fuel and TALOS-WEC is a novel multiple degree of freedom wave energy converter developed by Lancaster University, UK. The system in the study utilises a decommissioned offshore oil platform and uses seawater as a raw material, which brings forward the advantage of abundance. The study considers separation, electrolysis, compression or liquefaction, and a transportation system. An economic analysis and economic potential study has been done for each system and then a levelized cost of energy analysis has been calculated. A process flow diagram of the plant can be seen for the purpose of visualising the system setup. The LCOE of the suggested technology is at 123.19 $/MWh and the cost breakdown shows that the decommissioned oil platform will cost the most at 32.5 M $/yr followed by hydrogen compression technology and TALOS at 1.6 M$/yr and 1.5 M$/yr respectively for the stated operating period. This study has shown optimistic results for the Power-to-gas technology, but further research and development needed for TALOS-WEC to become feasible for the system.</div></div>","PeriodicalId":326,"journal":{"name":"Fuel Processing Technology","volume":"276 ","pages":"Article 108282"},"PeriodicalIF":7.2,"publicationDate":"2025-07-07","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"144570428","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}

{"title":"Biomass char gasification for hydrogen production: A thermodynamic equilibrium analysis","authors":"Shaolin Liu,&nbsp;Amine Ben-Abdelwahed,&nbsp;Cécile Gaborieau,&nbsp;Jean Lachaud","doi":"10.1016/j.fuproc.2025.108279","DOIUrl":"10.1016/j.fuproc.2025.108279","url":null,"abstract":"<div><div>Hydrogen can be produced from biomass via thermochemical conversion, either through direct gasification of raw biomass or a two-step process involving pyrolysis to generate char, followed by char gasification. The latter process reduces tar contamination in syngas and improves gasification efficiency. Chemical equilibrium modeling of char gasification provides valuable estimates of ideal operating conditions, serving as an effective tool for gasifier design and optimization. The analysis focuses on the effects of process parameters on hydrogen yield and efficiency, as well as the determination of optimal thermodynamic conditions for hydrogen production. The chemical composition of wood char at different pyrolysis temperatures was examined using literature data. Char gasification in steam was predicted using Gibbs energy minimization, identifying up to 122 product species. The optimal conditions were identified within a temperature range of 900–1300 °C and a steam-to-char molar ratio (<span><math><mi>m</mi></math></span>) of 0.6–0.9, yielding a hydrogen molar fraction of 0.53 ± 0.01. Under these conditions, the primary gases produced were <span><math><msub><mrow><mi>H</mi></mrow><mrow><mn>2</mn></mrow></msub></math></span> (0.53) and <span><math><mi>CO</mi></math></span> (0.45). Further optimization of process efficiency suggested that setting the gasification temperature to 800 °C and the steam-to-char molar ratio to 1.3 could achieve a hydrogen molar fraction of 0.5 while maintaining a process efficiency of 55%.</div></div>","PeriodicalId":326,"journal":{"name":"Fuel Processing Technology","volume":"276 ","pages":"Article 108279"},"PeriodicalIF":7.2,"publicationDate":"2025-07-06","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"144563093","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}