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Optimal operation of multi-plant steam district heating systems for enhanced efficiency and sustainability
IF 9.9 1区 工程技术 Q1 ENERGY & FUELS Pub Date : 2025-02-01 DOI: 10.1016/j.enconman.2024.119298
Saranya Anbarasu , Kathryn Hinkelman , Wangda Zuo , Victor Mendez Ferreira
Despite their crucial role in supplying heat and power to universities, industries, and healthcare facilities, many steam-based district heating systems rely on outdated control methods. Among these, multi-central plant districts are particularly challenging due to the complexities of coordinating multiple plants, optimizing load distributions, and managing system downtime. In response, new operational strategies are developed to enhance the efficiency and sustainability of steam districts while utilizing existing resources. These strategies include reducing plant operational pressure without compromising the reliable supply to buildings and optimizing load allocation across multiple plants. The load allocation considers boiler part-load efficiency, runtime, network losses, and building pressure set points, and is compared with traditional multi-boiler controls. To support this exploration, new dynamic Modelica models are developed. In addition, methods to reduce modeling complexities are incorporated, enhancing their suitability for practical applications. A holistic district-wide analysis using a real university case study demonstrates a 4.7% fuel savings by lowering boiler operational pressure from 900 kPa to 600 kPa, along with a 13.3% reduction in condensation losses across the distribution network. Furthermore, the load allocation approach results in a 13.1% reduction in fuel consumption during peak winter periods and 15.3% during shoulder periods, with corresponding decreases in carbon emissions and fuel costs. This approach can also save maintenance costs by reducing the boiler runtime by 49.6%. This research underscores the benefits of retrofitting aging steam district heating systems, offering immediate operational improvements by enhancing efficiency, meeting regulatory compliance, and extending infrastructure lifespans while delaying costly overhauls.
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引用次数: 0
Flow-driven directional freeze-casting of graphene aerogels on tubular components for enhanced thermal energy management
IF 9.9 1区 工程技术 Q1 ENERGY & FUELS Pub Date : 2025-02-01 DOI: 10.1016/j.enconman.2024.119389
Subhani Shaik, Vandana Kumari Jha, Ganghyeon Bae, Duckjong Kim
In the rapidly advancing field of energy storage technologies, achieving efficiency and sustainability has become paramount, with adsorption playing a crucial role. This adsorption process benefits significantly from aerogel-based structures due to their inherent porosity and customizable architectures, which facilitate exceptional heat- and mass-transfer capabilities. However, despite extensive research on optimizing aerogel microstructures for enhanced adsorption, integrating these materials into practical energy storage systems remains challenging. To overcome this, we present a flow-driven directional freeze-casting technique that integrates aerogels with radially oriented pore networks onto tubular components, forming well-aligned, fin-like structures. This innovative method increases the practical applicability of aerogels in real-world energy storage systems. By adjusting process conditions, we achieve a further improved alignment similar to longitudinal finned structures, significantly enhancing mass transfer. This improved alignment results in ∼ 35 % reductions in both adsorption and desorption times compared to the lowest alignment sample. Based on the measured adsorption characteristics, the performance estimation for thermal energy storage systems integrating the tailored aerogel structure showed a 61 % increase in power density compared to the highest recently reported value for sorption-based thermal battery. When applied to adsorption heat pump systems, the estimated specific cooling power improved by 68–98 % compared to other reported adsorbent composites. These results highlight the potential of our novel aerogel integration technique to enhance thermal management solutions and significantly advance adsorption-based energy systems.
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引用次数: 0
A multi-level optimization design and intelligent control framework for fuel cell-based combined heat and power systems
IF 9.9 1区 工程技术 Q1 ENERGY & FUELS Pub Date : 2025-02-01 DOI: 10.1016/j.enconman.2024.119397
Jiabao Cheng , Fubin Yang , Hongguang Zhang , Nanqiao Wang , Yinlian Yan , Yonghong Xu
Fuel cell systems have attracted significant attention in the field of residential energy due to their high efficiency and environmentally friendly characteristics. However, the inherent coupling of its thermoelectric output limits the flexibility of the system to meet diverse residential energy needs. This study proposes a combined heat and power system based on a proton exchange membrane fuel cell integrated with an organic Rankine cycle and heat pump, and builds a multi-level optimization design and intelligent control framework. Through this framework, current density and split ratio were identified as two key operational parameters affecting heat and power output. To enhance the precision and adaptability of system control, a neural network evaluation metric based on sensitivity weighting was introduced to optimize the hyperparameters of the Back Propagation neural network controller. This approach significantly improved the accuracy of the control model and system performance. Based on the optimized neural network controller, an intelligent control strategy oriented towards heat demand was realized, effectively meeting users’ dynamic needs. Results show that under typical demand conditions, the system achieved significant performance improvement: maximum thermal efficiency of 47.48 %, maximum electrical efficiency of 36.73 %, maximum hydrogen consumption rate of 1.3 g/s, and minimum levelized cost of energy of 0.4183 $/kW·h−1. This research provides valuable theoretical guidance for the optimization design and operations management of fuel cell-based combined heat and power systems.
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引用次数: 0
Waste eggshell derived CaO/metal-organic framework @LDH for microwave-assisted biodiesel synthesis: Thermodynamics, mechanistic insights and life-cycle cost analysis
IF 9.9 1区 工程技术 Q1 ENERGY & FUELS Pub Date : 2025-02-01 DOI: 10.1016/j.enconman.2024.119380
Saptarshi Roy, Md. Ahmaruzzaman
Designing an economical and environmentally friendly catalyst for production of biodiesel is crucial yet a challenging aspect for advancing renewable energy applications. To accomplish this, the present research elucidates the fabrication of a highly efficient novel heterogeneous catalyst by utilizing CaO derived from waste chicken eggshells and a metal–organic framework (MOF)@layered double hydroxide (LDH) (CLD-HK) for the sustainable microwave-assisted transesterification of soybean oil (SO), achieving a biodiesel yield of 99.78 ± 0.6 % within just 60 min. The remarkable catalytic performance is primarily ascribed to the strong basicity of CaO and LDH, along with the unsaturated sites contributed by the MOF, which create accessible active sites for effective substrate adsorption and effective coordination with triglycerides. This synergy results in excellent catalytic performance of the CLD-HK catalyst. Kinetic studies revealed an activation energy (Ea) of 29.50 kJ/mol, significantly lower than previous reported values, demonstrating high energy efficiency. Various parametric studies revealed that the reaction adhered to pseudo-first-order model with a rate constant of 0.07495 min−1. A plausible reaction mechanism for the transesterification of SO was proposed based on the various characterization results. Furthermore, 1HNMR, 13C NMR, FT-IR and GC–MS analyses validated the conversion of SO to fatty acid methyl esters (FAME), with the produced biodiesel meeting the ASTM standards. The life cycle cost analysis (LCCA) estimated the unit production cost at merely $0.42/kg, highlighting the commercial viability of this biowaste-based catalyst. This approach not only valorizes waste materials but also offers a sustainable and cost-effective alternative to petroleum-based diesel.
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引用次数: 0
Optimizing temperature and pressure in PEM electrolyzers: A model-based approach to enhanced efficiency in integrated energy systems 优化PEM电解槽的温度和压力:一种基于模型的方法来提高综合能源系统的效率
IF 9.9 1区 工程技术 Q1 ENERGY & FUELS Pub Date : 2025-02-01 DOI: 10.1016/j.enconman.2024.119338
Luka Bornemann, Jelto Lange, Martin Kaltschmitt
Hydrogen stands as a promising energy carrier within the ongoing energy supply transformation, yet its production via electrolyzers remains prohibitively costly. To address this challenge, this paper proposes an advanced equation-oriented process model for a PEM (Polymer-Electrolyte-Membrane) electrolysis system, including the electrolyzer and downstream hydrogen compression, aimed at optimizing the interaction of its operating parameters (i.e., current density, temperature, pressure). Initially, the model is utilized to analyze the isolated performance of the electrolysis system through operational flowsheet optimizations, followed by its integration into a broader energy system for operational planning optimization.
The study reveals several key findings: optimizing operational parameters, rather than using fixed values at the maximum, improves peak system efficiency by approximately 5 %pt. and shifts this peak to lower current densities, thus expanding the range of high-efficiency operation. Each current density has an optimal pair of temperature and pressure, with maximum temperatures only advantageous at loads above 40%, while maximum operating pressure is suboptimal across the entire load range. The analysis indicates that incorporating operating parameter optimization within the operational planning of the electrolysis system reduces energy consumption by 4% and operating costs by 7% in the evaluated energy system.
Additionally, the study distinguishes between optimizing the electrolyzer’s operating parameters for maximizing its own efficiency and for system efficiency (i.e., including hydrogen compression). It demonstrates that maximum system efficiency is achievable only when the electrolyzer considers hydrogen compression in its operation mode, accepting some efficiency losses individually but yielding greater efficiency gains in the context of hydrogen compression.
In summary, the findings of this paper suggest that continuously operating a PEM electrolyzer at maximum temperature and pressure may not be the most efficient approach. Instead, dynamic adjustments based on current density improve operational efficiency, thereby reducing electricity consumption and operating costs. Evaluating the electrolyzer within the broader energy system context – and accepting minor efficiency losses at the electrolyzer level – can yield significant overall benefits and savings. These results underscore the importance of comprehensive, context-aware strategies in advancing cost-effective green hydrogen production.
在正在进行的能源供应转型中,氢是一种很有前途的能源载体,但通过电解槽生产氢的成本仍然过高。为了解决这一挑战,本文提出了一个先进的面向方程的PEM(聚合物-电解质-膜)电解系统过程模型,包括电解槽和下游氢压缩,旨在优化其操作参数(即电流密度、温度、压力)的相互作用。首先,该模型通过操作流程优化来分析电解系统的孤立性能,然后将其集成到更广泛的能源系统中进行操作规划优化。
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引用次数: 0
Design and experimental testing of a novel skip-cycle mechanism for Wankel engine 一种新型万克尔发动机跳循环机构的设计与试验
IF 9.9 1区 工程技术 Q1 ENERGY & FUELS Pub Date : 2025-02-01 DOI: 10.1016/j.enconman.2024.119410
O.A. Kutlar , M. Üngör , Ö. Cihan
In this study a new skip-cycle mechanism which will be applied to the Wankel engine have been designed, analyzed and tested. With skip-cycle method application, after the four periods of power generation are completed, no more work is produced in the following cycle. To achieve this, the fuel and ignition are cut off during the cycle when power is not generated. Additionally, in this cycle the intake port is also closed. The aim of this application is to change the effective stroke volume of the engine according to load conditions thus reducing the pumping loss and increasing efficiency. Alternative mechanisms have been designed, analyzed and one of them with minimal modification is tested on the single rotor Mazda 13B test engine. In the designed system of skip-cycle, it has been intended to stop the intake operation with the aid of a rotary valve placed in the intake port thus providing cycle control. A correlation between the moving parts on the engine has been developed with the inclusion of the valve into the mechanism. Valve window angle, valve orientation and valve window geometry parameters were evaluated. The skip-cycle mechanism was installed in the test engine and measured data of the skip-cycle and normal cycle were compared. The result show that the Wankel engine with skip-cycle mechanism runs at low load conditions with higher pressure during combustion period and lower vacuum pressure at intake period compared at equal power generation at normal cycle conditions.
本文设计、分析和试验了一种应用于万克尔发动机的新型跳循环机构。采用跳循环法,四个周期发电完成后,下一个周期不再产生功。为了达到这个目的,在不产生动力的循环过程中,燃料和点火被切断。此外,在这个循环中,进气口也是关闭的。该应用程序的目的是根据负载条件改变发动机的有效冲程量,从而减少泵送损失并提高效率。对备选机构进行了设计和分析,并在单转子马自达13B试验发动机上对其中一种修改最小的机构进行了试验。在设计的跳过循环系统中,它旨在通过放置在进气口的旋转阀的帮助来停止进气操作,从而提供循环控制。发动机上运动部件之间的相关性随着气门的加入而发展起来。评估了阀窗角、阀窗方位和阀窗几何参数。在试验发动机上安装了跳循环机构,并对跳循环和正常循环的测量数据进行了比较。结果表明,与正常循环等功率工况相比,采用跳循环机构的万克尔发动机在燃烧期压力较高、进气期真空压力较低的低负荷工况下运行。
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引用次数: 0
Biogenic hydrogen production from oil hydrocarbons at geological carbon storage conditions 地质储碳条件下石油烃类生物制氢
IF 9.9 1区 工程技术 Q1 ENERGY & FUELS Pub Date : 2025-02-01 DOI: 10.1016/j.enconman.2024.119438
Javier Vilcáez, Emranul Chowdhury
We found that supercritical CO2 and the availability of protein-rich matter in depleted oil reservoirs can result in the biogenic production of H2 from oil hydrocarbons by indigenous microbial communities. Our experimental results support the hypothesis that a decrease in pH to acidic levels due to the dissolution of supercritical CO2 into the formation water and availability of protein-rich matter favors the activity of H2-producing microbial communities over the activity of H2-using microbial communities. To determine where, when, and how much H2 could be produced in a depleted oil reservoir injected with CO2 and produced water (PW) supplied with protein-rich matter, we simulated the biogenic production of H2 for the Morrow B sandstone reservoir. Simulations were conducted using CO2Bio, a program developed to simulate the multiphase bio-geochemical reactive transport of CO2-CH4-H2-H2S gases in geological carbon storage (GCS) sites. The microbiological capabilities of CO2Bio are validated against batch reaction experimental results. Our field-scale simulation results indicate that 154 – 1673 kg of H2 could be produced after 100 days of CO2 and PW co-injection into a single well of radial flow, and that sandstone reservoirs are more suitable than carbonate reservoirs to produce H2 from dissolved hydrocarbons. Based on the obtained experimental and simulation results, we propose a new H2 production method that couples GCS and PW disposal in depleted oil reservoirs to attenuate environmental and energy issues related to global warming derived from atmospheric pollution with CO2, risk of freshwater resources contamination with PW, and depletion of energy resources.
我们发现,超临界CO2和枯竭油藏中富含蛋白质物质的可用性可以导致本地微生物群落从石油碳氢化合物中生物生产H2。我们的实验结果支持这样的假设,即由于超临界CO2溶解到地层水中,pH值降低到酸性水平,并且富含蛋白质的物质的可用性有利于产生h2的微生物群落的活性,而不是利用h2的微生物群落的活性。为了确定在注入富含蛋白质物质的CO2和采出水(PW)的枯竭油藏中,在何时何地可以生产氢气,以及可以生产多少氢气,我们模拟了Morrow B砂岩油藏的生物产氢。利用CO2Bio软件模拟地质碳库(GCS)中CO2-CH4-H2-H2S气体多相生物地球化学反应输运过程。通过批反应实验结果验证了CO2Bio的微生物学性能。现场模拟结果表明,单井径向流注入CO2和PW 100天后,H2产量可达154 ~ 1673 kg,砂岩储层比碳酸盐岩储层更适合从溶解烃中生产H2。基于已获得的实验和模拟结果,我们提出了一种新的制氢方法,将GCS和PW处理结合在枯竭油藏中,以减轻二氧化碳污染大气、PW污染淡水资源和能源枯竭带来的全球变暖相关环境和能源问题。
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引用次数: 0
Synergistic intensification of palladium-based membrane reactors for hydrogen production: A review 钯基膜反应器协同强化制氢研究进展
IF 9.9 1区 工程技术 Q1 ENERGY & FUELS Pub Date : 2025-02-01 DOI: 10.1016/j.enconman.2024.119424
Wei-Wei Yang , Xin-Yuan Tang , Xu Ma , Xiangkun Elvis Cao , Ya-Ling He
Hydrogen is a clean, zero-carbon energy carrier that is critical in the transition to a renewable energy system. Hydrogen production membrane reactors are based on membrane technology for process intensification, allowing simultaneous reaction enhancement and hydrogen purification. However, concentration polarization creates mismatch between reaction and separation processes, limiting the performance. To further develop and increase the hydrogen production efficiency in membrane reactors, this review first provides advances in membrane reactor research from several perspectives, including membrane materials, performance metrics, and evaluation tools. Subsequently, the effects of operating conditions and structural design on the performance enhancement of membrane reactors are organized and analyzed. The review focuses on summarizing the mechanisms for improving membrane reactor design performance, proposing four methods: shortening distance, increasing routes, smoothing paths, and multi-product removal. Additionally, it is suggested to draw on membrane surface pattern designs to guide the disruption of concentration boundary layers. The review finds that enhancement ways primarily revolve around mitigating concentration polarization. Various ways have the potential to achieve low-cost and higher performance by complementing each other’s strengths, such as minimizing the use of precious metals and employing low-cost multi-product separation. Moreover, there is a lack of corresponding evaluation standards for membrane reactors, which hinders the subsequent commercialization development. Finally, this review combines existing challenges and research progress to provide perspectives for the future development of membrane reactors. The major goal is to introduce new research methods to further promote the application of membrane reactors in greater depth.
氢是一种清洁、零碳的能源载体,在向可再生能源系统过渡的过程中至关重要。制氢膜反应器是基于膜技术的过程强化,允许同时反应增强和氢气净化。然而,浓度极化造成反应和分离过程之间的不匹配,限制了性能。为了进一步发展和提高膜反应器的产氢效率,本文首先从膜材料、性能指标和评价工具等几个方面综述了膜反应器的研究进展。在此基础上,组织分析了操作条件和结构设计对膜反应器性能提高的影响。综述了提高膜反应器设计性能的机制,提出了缩短距离、增加路径、平滑路径和去除多产物的四种方法。此外,建议绘制膜表面图案设计来指导浓度边界层的破坏。审查发现,增强途径主要围绕减轻集中极化。通过相互补充优势,各种方法都有可能实现低成本和更高的性能,例如尽量减少贵金属的使用和采用低成本的多产品分离。此外,膜反应器缺乏相应的评价标准,阻碍了后续的商业化发展。最后,结合膜反应器存在的挑战和研究进展,对膜反应器的未来发展进行展望。主要目标是引入新的研究方法,进一步推动膜反应器在更大程度上的应用。
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引用次数: 0
Enabling large-scale enhanced hydrogen production in deep underground coal gasification in the context of a hydrogen economy 在氢经济背景下,实现深层地下煤气化大规模强化制氢
IF 9.9 1区 工程技术 Q1 ENERGY & FUELS Pub Date : 2025-02-01 DOI: 10.1016/j.enconman.2024.119449
Zixiang Wei , Liangliang Jiang , Aliakbar Hassanpouryouzband , Shanshan Chen , Yanpeng Chen , Yiwen Ju , Lele Feng , Kouqi Liu , Jiansheng Zhang , Zhangxin Chen , S.M. Farouq Ali
Underground coal gasification (UCG) is an emerging clean energy technology with significant potential for enhanced hydrogen production, especially when coupled with water injection. Previous lab-scale studies have explored this potential, but the mechanisms driving water-assisted hydrogen enhancement in large-scale, deep UCG settings remain unclear. This study addresses this gap using numerical simulations of a large-scale deep coal model designed for hydrogen-oriented UCG. We investigated single-point and multipoint water injection strategies to optimize hydrogen production. Additionally, we developed a retractable water injection technique to ensure sustained hydrogen output and effective cavity control. Our results indicate that the water–gas shift reaction is crucial for increasing hydrogen production. Multipoint injection has been proven to be more effective than single-point injection, increasing hydrogen production by 11% with an equal amount of steam. The introduction of retractable injection allows for continuous and efficient hydrogen generation, with daily hydrogen production rates of approximately five times that of a conventional injection scheme, and an increase in cumulative hydrogen production of approximately 105% over the same time period. Importantly, the multipoint injection method also helped limit vertical cavity growth, mitigating the risk of aquifer contamination. These findings support the potential of UCG as a low-carbon energy source in the transition to a hydrogen economy.
煤地下气化(UCG)是一种新兴的清洁能源技术,具有提高氢气产量的巨大潜力,特别是与注水相结合时。以前的实验室规模的研究已经探索了这种潜力,但是在大尺度、深UCG环境中驱动水辅助氢增强的机制仍然不清楚。本研究通过为面向氢的UCG设计的大型深部煤模型的数值模拟来解决这一差距。我们研究了单点和多点注水策略,以优化氢气产量。此外,我们开发了一种可伸缩注水技术,以确保持续的氢气输出和有效的空腔控制。我们的研究结果表明,水气转换反应对提高氢气产量至关重要。多点注入已被证明比单点注入更有效,在等量蒸汽的情况下,氢气产量可提高11%。引入可伸缩注氢系统后,可实现连续高效制氢,日制氢速率约为常规注氢方案的5倍,同期累计制氢量增加约105%。重要的是,多点注入方法还有助于限制垂直空腔的生长,降低含水层污染的风险。这些发现支持了UCG作为向氢经济过渡的低碳能源的潜力。
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引用次数: 0
Comprehensive experimental analysis of performance parameters and inductive process to determinate dynamic voltage characteristics for proton exchange membrane fuel cell 综合实验分析性能参数和感应过程确定质子交换膜燃料电池的动态电压特性
IF 9.9 1区 工程技术 Q1 ENERGY & FUELS Pub Date : 2025-02-01 DOI: 10.1016/j.enconman.2024.119426
Lei Huang , Xuexia Zhang , Yu Jiang , Shuangxi Tang , Hongbo Liao , Ruike Huang , Sidi Dong
Determining the dynamic characteristics is crucial for enhancing the efficiency and reliability of proton exchange membrane fuel cells (PEMFCs) system in hydrogen vehicle application. However, existing research lacks a comprehensive analysis of internal polarization processes and performance parameters, with an overemphasis on external voltage output signals. To address this gap, firstly, a practical polarization curve model integrated with dynamics of platinum oxidation and gas diffusion is established to obtain performance parameters. This model, in contrast to the traditional Butler-Volmer equation, can reproduce the doubling of Tafel slope. Then, this study introduces, for the first time, the ultra-low frequency inductive impedance of electrochemical impedance spectroscopy (EIS) to reveal the internal mechanism of dynamic response. After analyzing the relationship between dynamic voltage and impedance characteristics, an extended distribution of relaxation times (DRT) method is introduced, alongside an improved distributed transmission line model (TLM), enabling the quantitative analysis of inductive processes. Finally, the study evaluates the impact of operating conditions and degradation on dynamic characteristics from the perspectives of voltage signals, polarization decomposition, performance parameters, inductive process resistance, and current distribution heterogeneity, revealing the underlying mechanisms. The results indicate that dynamic responses primarily depend on the transient resistances associated with platinum oxidation and oxygen diffusion, which affect the transition in activation and concentration overpotentials. Additionally, diffusion resistance is related to oxide coverage. The internal humidity is a key factor as higher water activity facilitates intermediate reactions involving platinum. This study provides valuable insight into PEMFCs dynamic performance and guidance for system control optimization.
确定质子交换膜燃料电池(pemfc)系统的动态特性是提高氢燃料汽车应用效率和可靠性的关键。然而,现有的研究缺乏对内部极化过程和性能参数的全面分析,过于强调外部电压输出信号。为了解决这一问题,首先建立了结合铂氧化和气体扩散动力学的实用极化曲线模型,获得了性能参数;与传统的Butler-Volmer方程相比,该模型可以再现塔菲尔斜率的加倍。然后,本研究首次引入了电化学阻抗谱(EIS)的超低频感应阻抗,揭示了动态响应的内在机理。在分析了动态电压和阻抗特性之间的关系后,引入了一种扩展的松弛时间分布(DRT)方法,以及改进的分布式传输线模型(TLM),使感应过程的定量分析成为可能。最后,从电压信号、极化分解、性能参数、感应过程电阻、电流分布不均一性等方面评价了工况和劣化对动态特性的影响,揭示了影响机理。结果表明,动态响应主要取决于与铂氧化和氧扩散相关的瞬态电阻,这影响了活化和浓度过电位的转变。此外,扩散阻力与氧化物覆盖有关。内部湿度是一个关键因素,因为较高的水活度有利于涉及铂的中间反应。该研究为pemfc的动态性能提供了有价值的见解,并为系统控制优化提供了指导。
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引用次数: 0
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Energy Conversion and Management
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