Article(id=1321927695362011569, tenantId=1146029695717560320, journalId=1220038251117760515, issueId=1321926982078681131, articleNumber=null, orderNo=null, doi=10.11868/j.issn.1001-4381.2025.000306, pmid=null, cstr=32421.14.j.issn.1001-4381.2025.000306, oa=null, hot=null, price=null, onlineType=0, articleFormat=0, articleType=null, articleTypeStr=research-article, receivedDate=1748016000000, receivedDateStr=2025-05-24, revisedDate=null, revisedDateStr=null, acceptedDate=1750608000000, acceptedDateStr=2025-06-23, onlineDate=1793101722802, onlineDateStr=2026-10-27, pubDate=1771516800000, pubDateStr=2026-02-20, doiRegisterDate=null, doiRegisterDateStr=null, onlineIssueDate=1793101722802, onlineIssueDateStr=2026-10-27, onlineJustAcceptDate=null, onlineJustAcceptDateStr=null, onlineFirstDate=null, onlineFirstDateStr=null, sourceXml=null, magXml=null, createTime=1793101722802, creator=13701087609, updateTime=1793101722802, updator=13701087609, issue=Issue{id=1321926982078681131, tenantId=1146029695717560320, journalId=1220038251117760515, year='2026', volume='54', issue='2', pageStart='1', pageEnd='311', issueExtLink='null', onlineDate='null', pubDate='1771516800000', pubDateStr='2026-02-20', beforeIssueId=null, nextIssueId=null, price=null, status=1, issueComplete=1, articleOrder=1, issueType=-1, specialIssue=null, createTime=1793101552742, creator='13701087609', updateTime=1793101552742, updator='13701087609', preIssue=null, nextIssue=null, articleTotal=null, ext=null, issueFiles=null, downloadFileDto=null}, startPage=63, endPage=79, ext={EN=ArticleExt(id=1321927695580115378, articleId=1321927695362011569, tenantId=1146029695717560320, journalId=1220038251117760515, language=EN, title=Research progress in ceramic additive manufacturing technology in field of catalyst carriers, columnId=1321926982854627373, journalTitle=Journal of Materials Engineering, columnName=CERAMIC ADDITIVE MANUFACTURING AND ITS APPLICATIONS, runingTitle=null, highlight=null, articleAbstract=
Ceramic additive manufacturing technology, through high-precision structural design and multi-material integrated molding, provides a new approach for the field of catalysis, ranging from carrier customization to precise regulation of active sites. Catalyst carriers prepared based on ceramic additive manufacturing technology feature higher mass transfer efficiency, freely formed geometric shapes, and excellent thermal stability, demonstrating significant potential in reducing production costs and advancing green energy initiatives. This review systematically examines four principal additive manufacturing technologies applied to ceramic catalyst carriers: direct ink writing, stereolithography, digital light processing, and fused deposition modeling. The review summarizes four major kinds of ceramics applied as catalyst carriers, and outlines the current research landscape of additive manufacturing in fabricating diverse ceramic catalyst carriers, with a focused analysis on their applications in automotive exhaust purification, denitrification processes, chemical synthesis, solid oxide fuel cells, and solar thermochemical cycle reactions. Finally, the key challenges and future development directions of additively manufactured ceramic catalyst supports are discussed. Future research should focus on the development of novel multifunctional ceramic material systems, the synergistic design of high-precision and multiscale architectures, the coupled regulation of active sites and mass transfer behavior, as well as green, low-energy fabrication and post-processing strategies, to promote the large-scale application of additively manufactured ceramic catalyst supports in energy conversion and environmental catalysis.
, authors=Xintong XU
1, Xuezhi LI
1, Xiaoyan ZHANG
1, Huihui KONG
2, authorsList=Xintong XU, Xuezhi LI, Xiaoyan ZHANG, Huihui KONG, authorCompany=null, correspAuthors=Xiaoyan ZHANG, authorNote=null, correspAuthorsNote=null, copyrightStatement=null, copyrightOwner=null, extLink=null, articleAbsUrl=null, sourceXml=null, magXml=null, pdfUrl=null, pdf=null, pdfFileSize=null, pdfExtLink=null, richHtmlUrl=null, mobilePdfUrl=null, reviewReport=null, pdfFirstPage=null, abstractGraph=null, abstractGraphContent=null, abstractVideo=null, citation=null, cebUrl=null, magXmlContent=null, mapNumber=null, fund=null), CN=ArticleExt(id=1321927699191411141, articleId=1321927695362011569, tenantId=1146029695717560320, journalId=1220038251117760515, language=CN, title=陶瓷增材制造技术在催化剂载体领域的研究进展, columnId=1321926983152422959, journalTitle=材料工程, columnName=陶瓷增材制造及其应用, runingTitle=null, highlight=null, articleAbstract=
陶瓷增材制造技术通过高精度结构设计与多材料一体化成型,为催化领域提供了从载体定制到活性位点精准调控的新方法。基于陶瓷增材制造技术制备的催化剂载体具有更高的传质效率、自由成型的几何形态、优异的热稳定性,在降低成本的同时,推动了绿色能源发展。本文综述了应用于陶瓷催化剂载体的四种主要增材制造技术,包括墨水书写成型技术、立体光固化成型技术、数字光投影技术和熔融沉积技术,概述了四种常见的催化剂载体陶瓷体系,总结了陶瓷增材制造技术制备不同类型陶瓷催化剂载体的研究现状,着重讨论了在汽车尾气处理、脱硝处理、化学合成、固体氧化物燃料电池、太阳能热化学循环反应等不同应用场景下催化剂载体的研究进展,最后,对陶瓷增材制造催化剂载体所面临的关键挑战与未来发展方向进行了展望。未来研究应重点围绕新型多功能陶瓷材料体系开发、高精度与多尺度结构协同设计、活性位点与传质行为的耦合调控以及绿色低能耗成型与后处理工艺展开,以推动陶瓷增材制造催化剂载体在能源转化与环境催化等领域的规模化应用。
, authors=徐欣彤
1, 李学智
1, 张笑妍
1, 孔慧慧
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2 catalyst for hydrogen photoproduction, refAbstract=null)], funds=[Fund(id=1321928030713397607, tenantId=1146029695717560320, journalId=1220038251117760515, articleId=1321927695362011569, awardId=2242046, language=CN, fundingSource=北京市自然科学基金面上项目(2242046), fundOrder=null, country=null), Fund(id=1321928032336593256, tenantId=1146029695717560320, journalId=1220038251117760515, articleId=1321927695362011569, awardId=FRF-IDRY-24-020, language=CN, fundingSource=北京科技大学青年教师学科交叉研究项目(中央高校基本科研业务费专项资金)(FRF-IDRY-24-020), fundOrder=null, country=null)], companyList=[AuthorCompany(id=1321928020072448306, tenantId=1146029695717560320, journalId=1220038251117760515, articleId=1321927695362011569, xref=1., ext=[AuthorCompanyExt(id=1321928020085031219, tenantId=1146029695717560320, journalId=1220038251117760515, articleId=1321927695362011569, companyId=1321928020072448306, language=EN, country=null, province=null, city=null, postcode=null, companyName=null, departmentName=null, remark=
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Schematic diagram of DIW process(a)[21],storage modulus (G') and loss modulus (G'') as function of shear stress for different ceramic inks studied(b)[28],high magnification SEM micrograph showing the interconnection among channels inside the rectilinear geometry(c)[28],and gas velocity passing through the DIW printed catalyst with a rectilinear geometry(d)[28], figureFileSmall=5E0fqLVrb0syxJA39GX8jQ==, figureFileBig=P5amnanmW4UDei49vklvjw==, tableContent=null), ArticleFig(id=1321928028482027862, tenantId=1146029695717560320, journalId=1220038251117760515, articleId=1321927695362011569, language=CN, label=图1, caption=
DIW工艺示意图(a)[21]、不同陶瓷墨水的储能模量(G')和损耗模量(G'')随剪切应力变化曲线(b)[28]、高倍SEM图显示矩形通道内部的相互连接情况(c)[28]及DIW打印直线几何结构催化剂中的气体流速情况(d)[28], figureFileSmall=5E0fqLVrb0syxJA39GX8jQ==, figureFileBig=P5amnanmW4UDei49vklvjw==, tableContent=null), ArticleFig(id=1321928028612051287, tenantId=1146029695717560320, journalId=1220038251117760515, articleId=1321927695362011569, language=EN, label=Fig.2, caption=
Schematic diagram of Al2O3/Ce-TZP ceramics printed by stereolithography(a)[31],absorbance of different samples(b)[31],schematic diagram of EA bridging to KH560-modified Si3N4 powder(c)[36], figureFileSmall=0x+qkvyC4vKfUQprYAUz6w==, figureFileBig=9geBNYtApdHY1ixIncltkg==, tableContent=null), ArticleFig(id=1321928028884681048, tenantId=1146029695717560320, journalId=1220038251117760515, articleId=1321927695362011569, language=CN, label=图2, caption=
立体光固化成型Al2O3/Ce-TZP陶瓷示意图(a)[31]、不同样品吸光度(b)[31]、EA与KH560改性Si3N4粉末表面间的桥接机理示意图(c)[36], figureFileSmall=0x+qkvyC4vKfUQprYAUz6w==, figureFileBig=9geBNYtApdHY1ixIncltkg==, tableContent=null), ArticleFig(id=1321928028968567129, tenantId=1146029695717560320, journalId=1220038251117760515, articleId=1321927695362011569, language=EN, label=Fig.3, caption=
A typical apparatus for DLP system(a)[43],overall schematic flowchart for preparation of HPC loaded with Ni/Co based catalysts(b)[45],DLP printed green body(c)[46],and SEM images of WP scaffold at different magnifications(d)[46], figureFileSmall=Vc2tOUwX+nMR4bhHxKSkaQ==, figureFileBig=yKKIbqYbeiHSbt3sM1Uctw==, tableContent=null), ArticleFig(id=1321928029052453210, tenantId=1146029695717560320, journalId=1220038251117760515, articleId=1321927695362011569, language=CN, label=图3, caption=
DLP系统的典型设备示意图(a)[43]、制备负载Ni/Co基催化剂的HPC的总体示意图(b)[45]、DLP打印坯体(c)[46]及不同倍率下WP支架的SEM图(d)[46], figureFileSmall=Vc2tOUwX+nMR4bhHxKSkaQ==, figureFileBig=yKKIbqYbeiHSbt3sM1Uctw==, tableContent=null), ArticleFig(id=1321928029341860187, tenantId=1146029695717560320, journalId=1220038251117760515, articleId=1321927695362011569, language=EN, label=Fig.4, caption=
Processing workflow of the FDM method based upon screw extrusion(a)[49],and conceptual flow chart for the 3D printing gyroid for photocatalytic applications(b)[53], figureFileSmall=kVX8YtbBOEL6jaEnv0Wg1w==, figureFileBig=GuMZPaUI9uAHiiE/tkR+yg==, tableContent=null), ArticleFig(id=1321928029459300700, tenantId=1146029695717560320, journalId=1220038251117760515, articleId=1321927695362011569, language=CN, label=图4, caption=
基于螺杆挤出法的FDM工艺流程图(a)[49]及用于光催化的3D打印嵌入式gyroid结构的概念流程图(b)[53], figureFileSmall=kVX8YtbBOEL6jaEnv0Wg1w==, figureFileBig=GuMZPaUI9uAHiiE/tkR+yg==, tableContent=null), ArticleFig(id=1321928029715153245, tenantId=1146029695717560320, journalId=1220038251117760515, articleId=1321927695362011569, language=EN, label=Fig.5, caption=
Catalyst carriers coated with catalysts(a)[76],green parts(from left to right:U-lock,thread,and twist-lock)(b)[77],schematic illustration of fabrication procedure for 3D-Cu-SSZ-13@SiO2 monolithic catalysts(c)[78],schematic diagram and digital photograph of catalytic testing(d)[78],and NO conversion of 3D-Cu-SSZ-13 and 3D-Cu-SSZ-13@SiO2-50 at 300 ℃ with different WHSV(e)[78], figureFileSmall=T1mvklzuQCT/LdCOeeC6iw==, figureFileBig=Ks31zZ4YDSBuUSXNBJ5mRA==, tableContent=null), ArticleFig(id=1321928029815816542, tenantId=1146029695717560320, journalId=1220038251117760515, articleId=1321927695362011569, language=CN, label=图5, caption=
涂覆过催化剂的催化剂载体(a)[76],坯体部件(从左到右:U型锁、螺纹、旋锁)(b)[77],3D-Cu-SSZ-13@SiO2整体式催化剂的制备过程示意图(c)[78],催化试验原理图及照片(d)[78]及不同WHSV下3D-Cu-SSZ-13和3D-Cu-SSZ-13@SiO2-50在300 ℃下NO的转换率(e)[78], figureFileSmall=T1mvklzuQCT/LdCOeeC6iw==, figureFileBig=Ks31zZ4YDSBuUSXNBJ5mRA==, tableContent=null), ArticleFig(id=1321928029916479839, tenantId=1146029695717560320, journalId=1220038251117760515, articleId=1321927695362011569, language=EN, label=Fig.6, caption=
NH3-SCR process(a)[82],3D-printed closed-walls lattice (left),and 3D-printed and sintered closed-walls lattice in its final configuration (right)(b)[84],and schematic diagram of printed Mn-Ce-Fe/ATP monolithic woodpile structure(c)[85], figureFileSmall=KvZ96FL0Y5nBzSgeBBUa0Q==, figureFileBig=C/zbkxbb9Yh9qNF2np8ACw==, tableContent=null), ArticleFig(id=1321928030012948832, tenantId=1146029695717560320, journalId=1220038251117760515, articleId=1321927695362011569, language=CN, label=图6, caption=
NH3-SCR反应过程(a)[82]、3D打印闭合壁晶格(左图)和3D打印烧结闭合壁晶格的最终形态(右图)(b)[84]、打印的木堆结构Mn-Ce-Fe/ATP示意图(c)[85], figureFileSmall=KvZ96FL0Y5nBzSgeBBUa0Q==, figureFileBig=C/zbkxbb9Yh9qNF2np8ACw==, tableContent=null), ArticleFig(id=1321928030101029217, tenantId=1146029695717560320, journalId=1220038251117760515, articleId=1321927695362011569, language=EN, label=Fig.7, caption=
The topological structured Al2O3 carrier printed by SLA(a)[86],conversion of CH4 and CO2(b)[86],digital design of the catalyst architectures and optical microscope micrographs of the catalyst architectures(c)[87],BCC structure as printed (top view)(d)[89],optical microscope image of a calcined BCC structure(cross-sectional view)(e)[89],FCC structure,as printed(top view)(f)[89],and optical microscope image of a calcined FCC structure(cross-sectional view)(g)[89], figureFileSmall=PlgK3MjnfJupSEPi8GVWFg==, figureFileBig=uIRBSYsnYQpzZhUcodLRTA==, tableContent=null), ArticleFig(id=1321928030201692514, tenantId=1146029695717560320, journalId=1220038251117760515, articleId=1321927695362011569, language=CN, label=图7, caption=
SLA打印的拓扑结构Al2O3载体(a)[86]、CH4和CO2的转化率(b)[86]、催化剂结构的数字化设计及其光学显微镜照片(c)[87]、打印BCC结构的俯视图(d)[89]、BCC结构烧结后的光学显微镜图像(横截面)(e)[89]、打印FCC结构的俯视图(f)[89]及FCC结构烧结后的光学显微镜图像(横截面)(g)[89], figureFileSmall=PlgK3MjnfJupSEPi8GVWFg==, figureFileBig=uIRBSYsnYQpzZhUcodLRTA==, tableContent=null), ArticleFig(id=1321928030285578595, tenantId=1146029695717560320, journalId=1220038251117760515, articleId=1321927695362011569, language=EN, label=Fig.8, caption=
Current density-voltage-power characteristics of the 3D-printed anode-supported cell MS-3DC and 3DC at 700-800 °C with the supply of humidified H2=0.4 L·min-1 and air 1.2 L·min-1, respectively(a)[93],procedure of forming multi-cylindrical objects and stacking layers(b)[94],DLP-printed honeycomb structure(c)[95],and a cross-sectional microstructure of honeycomb structure printed by DLP(d)[95], figureFileSmall=1J/oOkA7Lb9tv7D58bqv2w==, figureFileBig=56fttj2FtJSPrWs4vl/XVg==, tableContent=null), ArticleFig(id=1321928030377853284, tenantId=1146029695717560320, journalId=1220038251117760515, articleId=1321927695362011569, language=CN, label=图8, caption=
3D打印阳极支撑电池MS-3DC和3DC在700~800 ℃条件下的电流密度、电压、功率特性(供给条件分别为加湿H2=0.4 L/min,空气=1.2 L/min)(a)[93]、形成多圆柱形物体和堆叠层的过程(b)[94]、DLP打印的蜂窝结构(c)[95]及DLP打印蜂窝结构的横截面微观结构(d)[95], figureFileSmall=1J/oOkA7Lb9tv7D58bqv2w==, figureFileBig=56fttj2FtJSPrWs4vl/XVg==, tableContent=null), ArticleFig(id=1321928030457545061, tenantId=1146029695717560320, journalId=1220038251117760515, articleId=1321927695362011569, language=EN, label=Fig.9, caption=
Photograph of DIW-printed CeO2 scaffolds(a)[97],morphology comparison of CeO2 structures with different gradient channels the two pore structures with different effective density gradients are presented in one image(b)[98],steady-state temperature profiles across the sample during the reduction step for the 10 structures(insert:volume-specific fuel yield (mLn CO generated per unit volume) during the oxidation step of the CO2-splitting cycle)(c)[98],3D printed Au/TiO2 monoliths,photographs of a post-impregnated(left) and a pre-impregnated (right) Au/TiO2 monoliths(d)[100],micro-CT 3D visualization of the internal section of an Au/TiO2 monolith(e),SEM images of the Au/TiO2 monoliths printed with nozzle diameters of 580 μm(f),410 μm(g),and 200 μm(h)[100],and effect of microfilament thickness on photocatalytic hydrogen production using post-impregnated Au/TiO2 monoliths calcined at 400 ℃ containing 4 layers and a mass fraction of 0.005% Au loading (X-axis corresponds to the ratio between geometric exposed surface and monolith weight for each microfilament thickness,Y-axis corresponds to the normalized activity on an Au mass basis)(i)[100], figureFileSmall=CzJexSawjZeDfncwwO2h4w==, figureFileBig=m+8xWFs8tCVh0aPTTzIt2Q==, tableContent=null), ArticleFig(id=1321928030541431142, tenantId=1146029695717560320, journalId=1220038251117760515, articleId=1321927695362011569, language=CN, label=图9, caption=
DIW打印的CeO2支架照片(a)[97],不同梯度通道CeO2结构的形态比较(梯度孔隙结构由一张图片表示)(b)[98],10种结构在还原过程中样品的稳态温度分布(插入图:在CO2分解循环的氧化步骤中,体积比燃料产量(单位体积产生的百万CO))(c)[98],3D打印的Au/TiO2单体,浸渍后(左)和预浸渍(右)Au/TiO2单体的照片(d)[100],Au/TiO2整体式催化剂内部结构的三维可视化图(micro-CT)(e)[100],不同喷嘴直径580 μm(f)、410 μm(g)、200 μm(h)打印的Au/TiO2 SEM图像[100],微丝厚度对400 ℃煅烧后浸渍Au/TiO2单体光催化制氢的影响(含4层,Au质量分数为0.005%)(X轴对应于每个微丝厚度的几何暴露面与整体重量之比,Y轴对应于以Au质量为基础的标准化活度)(i)[100], figureFileSmall=CzJexSawjZeDfncwwO2h4w==, figureFileBig=m+8xWFs8tCVh0aPTTzIt2Q==, tableContent=null)], attaches=null, journal=Journal(id=1220037122615103490, delFlag=0, nameCn=材料工程, nameEn=Journal of Materials Engineering, nameHistory1=null, nameHistory2=null, issn=1001-4381, eissn=, cn=11-1800/TB, coden=null, periodic=0, language=CN, oaType=null, ccby=null, superviseOffice=null, ownerOffice=null, pubOffice=null, editorOffice=null, officeType=null, aims=null, clcCode=null, officeProv=null, officeCity=null, officeAddr=null, officeZip=null, officeEmail=null, officePhone=null, editDirector=null, 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