基于Pd-Pt双金属催化剂的燃料电池尾排消氢器研究与试验OA
Development and performance evaluation of a palladium-platinum bimetallic-catalyst-based hydrogen eliminator for fuel cell exhaust
随着氢能作为清洁能源的快速发展,其安全隐患尤其是氢气泄漏引发的燃烧爆炸风险已成为制约其规模化应用的关键挑战.文章针对现有消氢技术在催化效率、响应速度和结构集成性方面的不足,设计了一种基于钯-铂(Pd-Pt)双金属催化剂的新型消氢器.该装置采用蜂窝陶瓷载体与催化剂颗粒的复合结构,优化了催化活性、气体流动和热管理.通过搭建试验平台,在100~400 SLPM气体流量和1%~4%氢气浓度条件下进行性能测试.结果显示,最高消氢效率可达93%以上,稳态响应时间(160~300 s)随流量增加而延长,但转化率保持一致,证明了系统的适应性和稳定性.同时,温度监测揭示了氢气浓度对稳态温度(70~110℃)的显著影响,强调了热管理的重要性.该设计具有轻量化、模块化和低成本优势,适用于车载及分布式氢能系统,为提升氢能燃料电池的安全性和工程可行性提供了有效解决方案.
[Objective]Existing hydrogen-elimination technologies suffer from low catalytic efficiency and slow response speed,as well as poor structural integration,which limit their application in fuel cell systems.The high leakage propensity,low ignition energy,and wide combustion range of hydrogen pose critical safety risks that constrain the scalability of hydrogen energy.To address these challenges and achieve high catalytic performance,rapid response,and lightweight,modular integration,this study develops a novel palladium-platinum(Pd-Pt)bimetallic-catalyst-based hydrogen eliminator.By optimizing the catalyst formulation and structural design,the device enhances hydrogen recombination efficiency and operational safety for vehicular and distributed energy systems.[Methods]The hydrogen eliminator was designed using a Pd-Pt bimetallic catalyst supported on an integrated system comprising a honeycomb ceramic carrier and catalyst particles to maximize catalytic activity and gas-flow efficiency.The catalyst employs an alumina(Al2O3)framework with Pd-Pt nanoparticles at a loading of 300 g/m3,integrated into a 400-mesh porous honeycomb carrier(outer diameter:80 mm;height:2 cm).Spherical catalyst particles(diameter:5.0±0.1 mm)were packed between the honeycomb layers,forming a uniform pore network that minimizes flow resistance and enhances contact efficiency.The eliminator shell,constructed from 45 steel,features a three-segment modular design with flared inlet and outlet channels and fluororubber seals to ensure airtightness.Performance evaluation was conducted on a custom test platform across gas-flow rates and hydrogen concentrations of 100-400 SLPM and 1%-4%,respectively.Real-time monitoring of inlet and outlet hydrogen concentrations and reaction temperatures enabled calculation of the elimination efficiency using X=(H2_in-H2_out)/H2_in×100%.Nine test conditions were evaluated,covering various flow-rate and concentration combinations.Each test was conducted for 10 minutes to assess steady-state response time,elimination efficiency,and temperature variation.[Results]Experimental results revealed the following:at 100 SLPM,hydrogen-elimination efficiencies reached 93%,90%,and 88%for hydrogen concentrations of 1%,2%,and 4%,respectively,with a steady-state response time of approximately 160 s;at 200 SLPM,elimination efficiencies remained within 1%of those recorded at 100 SLPM,although the response time increased to approximately 200 s;at 400 SLPM,elimination efficiencies remained consistent,whereas the response time increased to approximately 300 s,indicating that higher gas-flow rates prolonged the response time without significantly affecting steady-state efficiency;thermal analysis at 200 SLPM revealed steady-state temperatures of 70℃,90℃,and 110℃for hydrogen concentrations of 1%,2%,and 4%,respectively,highlighting the influence of hydrogen concentration on exothermic heat release.The system demonstrated robust catalytic stability and adaptability,with the modular design reducing noble metal loading and enhancing integration flexibility.Furthermore,flow-resistance and pressure-drop tests confirmed the enhanced hydrodynamic efficiency of the structure.[Conclusions]Pd-Pt bimetallic catalysts were integrated with a honeycomb ceramic carrier to achieve hydrogen-elimination efficiencies and response times of 88%-93%and 160-300 s,respectively,effectively meeting the dynamic requirements of fuel cell systems.The modular design and optimized flow channels reduced manufacturing costs,flow resistance,and maintenance complexity,significantly enhancing system integration and scalability.The experimental results elucidate the synergistic effects of gas-flow rate and hydrogen concentration on response time and thermal behavior,providing critical data for engineering scale-up and operational optimization.This design provides a reliable solution for safe hydrogen management in vehicular and distributed energy systems,ultimately supporting the broader adoption of hydrogen fuel cells and sustainable energy transitions.
徐磊;王学亮;盛文;胡煜;任潇宇;曹圣
中车青岛四方机车车辆股份有限公司,山东 青岛 266111中车青岛四方机车车辆股份有限公司,山东 青岛 266111同济大学 汽车学院,上海 201804同济大学 汽车学院,上海 201804同济大学 汽车学院,上海 201804同济大学 汽车学院,上海 201804
能源科技
催化燃烧Pd-Pt催化剂消氢效率燃料电池尾排
catalytic combustionPd-Pt catalysthydrogen-elimination efficiencyfuel cell exhaust
《实验技术与管理》 2026 (3)
60-65,6
工业和信息化部装备工业一司课题项目(CEIEC-2024-ZM02-0044)
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