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Comprehensive study on performance improvement of flat plate solar collectors integrated with thermal energy storage through porous media and nano-additives 利用多孔介质和纳米添加剂提高蓄热平板太阳能集热器性能的综合研究
IF 6.9 2区 工程技术 Q2 ENERGY & FUELS Pub Date : 2026-01-07 DOI: 10.1016/j.applthermaleng.2026.129717
Mohammed Y. Nawaf , Abdulrazzak Akroot , Hasanain A. Abdul Wahhab
Sustainable energy development is one of the most continuous, as it is an available, environmentally friendly energy used to meet demand for heat. Due to their simple design, solar collectors are the most widely used technology for solar thermal energy. Also, a major drawback faced by solar thermal collectors operating at low and medium temperature levels is their low thermal performance. This study examines the thermal performance enhancement of solar collectors through the integration of porous media absorbers, TiO₂–water nanofluids, and thermal energy storage (TES) systems. Four porous absorber configurations, C65, C93, A60, and A80 (copper and aluminum materials), were experimentally examined and validated using computational fluid dynamics (CFD) simulations under varying porosities, flow rates, and nanoparticle concentrations (0.1–0.3 wt%). Results revealed that the copper foam with 65 % porosity (C65) delivered the highest temperature difference and thermal efficiency among all configurations, with outlet temperature increases of up to 6.8 °C and a 14.5 % improvement in thermal efficiency compared to the baseline. In contrast, the A60 aluminum model exhibited more modest gains. The addition of TiO₂ nanoparticles enhanced heat transfer due to increased effective thermal conductivity, while TES integration reduced outlet temperature fluctuations by nearly 20 %, ensuring more stable operation. Although these findings highlight the promise of hybrid solar collector designs, challenges such as maintaining nanofluid stability, increased pumping power requirements, and ensuring economic feasibility remain critical for real-world applications. This study provides the first systematic comparative insights into the coupled effects of absorbed unit design, nanoparticle integration, and TES operation, offering a practical framework for optimizing solar thermal systems.
可持续能源发展是最持续的能源之一,因为它是一种可用的、环保的能源,用于满足供热需求。由于其设计简单,太阳能集热器是应用最广泛的太阳能热技术。此外,太阳能集热器在低温度和中温度水平下工作面临的一个主要缺点是它们的低热性能。本研究考察了通过集成多孔介质吸收器、二氧化钛-水纳米流体和热能储存(TES)系统来增强太阳能集热器的热性能。在不同孔隙率、流速和纳米颗粒浓度(0.1-0.3 wt%)的条件下,采用计算流体动力学(CFD)模拟对C65、C93、A60和A80(铜和铝材料)四种多孔吸收体结构进行了实验研究和验证。结果表明,65%孔隙率(C65)的泡沫铜在所有配置中提供了最高的温差和热效率,出口温度比基线提高了6.8°C,热效率提高了14.5%。相比之下,A60铝制车型表现出更温和的增长。由于增加了有效导热系数,tio2纳米颗粒的加入增强了传热,而TES集成减少了近20%的出口温度波动,确保了更稳定的运行。尽管这些发现强调了混合太阳能集热器设计的前景,但保持纳米流体稳定性、增加泵送功率需求以及确保经济可行性等挑战对实际应用仍然至关重要。本研究首次对吸收单元设计、纳米颗粒集成和TES运行的耦合效应进行了系统的比较研究,为优化太阳能热系统提供了一个实用的框架。
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引用次数: 0
Enhanced thermal performance of glass dual-stage wedge-shaped manifold microchannel heat sinks 提高玻璃双级楔形流形微通道散热器的热性能
IF 6.9 2区 工程技术 Q2 ENERGY & FUELS Pub Date : 2026-01-07 DOI: 10.1016/j.applthermaleng.2026.129706
Guanghan Huang , Yi Zhang , Shuang Liu , Wenjie Miao , Jiawei Liao , Mengnan Jiang , Chengqiang Cui , Yu Zhang , Guannan Yang , Shidong Xue
With the increase in heat flux in Integrated Circuit (IC) chips and the trend of utilizing low-thermal-conductivity glass substrates for microelectronic packaging, thermal management has become a significant challenge. Dual-sided cooling with an embedded microchannel on a glass substrate to achieve near-source cooling is a promising solution. Manifold Microchannels (MMCs) with a more uniform temperature distribution demonstrates potential prospects in IC substrate-embedded cooling technologies. However, current MMCs are mainly single-stage and often experience uneven flow distributions. In addition, there are few reports on MMCs fabricated using glass. To address these gaps, this study proposes a novel Dual-stage Wedge-shaped Manifold Microchannel (DWMMC) with glass as a material. The main objective is to mitigate flow inhomogeneity and improve temperature uniformity. A glass-based Single-stage Wedge-shaped Manifold Microchannel (SWMMC) was used as the control group. The hydrodynamic and thermal performances of single-phase convective heat transfer were experimentally and numerically analyzed. The experimental results show that the DWMMC exhibits superior thermal performance compared to the SWMMC. Compared with SWMMC, DWMMC reduces the glass-bottom wall temperature by 17.3 °C at 6.7 W·cm−2, and significantly improves the temperature uniformity. In addition, the DWMMC increased the convective heat transfer coefficient (heff) by 58.5 %, achieving a maximum heff of 6976 W·m−2·K−1. The comprehensive performance evaluation parameter COP was also enhanced by 35.8 %. This enhancement is attributed to the double-bending baffle flow of the DWMMC, which effectively suppresses flow maldistribution and alleviates the large-area low-velocity or stagnation zone. This hydraulic improvement reduces the thickness of the velocity boundary layer and strengthens fluid mixing. Finally, the application demonstration of DWMMC revealed that the thermal resistance of dual-sided cooling with glass substrate-embedded microchannels was remarkably decreased by 57.5 % compared with conventional single-sided cooling.
随着集成电路(IC)芯片中热流通量的增加以及采用低导热玻璃基板进行微电子封装的趋势,热管理已成为一个重大挑战。在玻璃基板上嵌入微通道实现近源冷却的双面冷却是一种很有前途的解决方案。温度分布更为均匀的流形微通道(MMCs)在集成电路衬底嵌入式冷却技术中具有广阔的应用前景。然而,目前的mmc主要是单级的,并且经常出现流量分布不均匀的情况。此外,用玻璃制造mmc的报道很少。为了解决这些差距,本研究提出了一种新型的双级楔形流形微通道(DWMMC),以玻璃为材料。主要目的是减轻流动不均匀性,提高温度均匀性。采用玻璃基单级楔形流形微通道(SWMMC)作为对照组。对单相对流换热的水动力和热性能进行了实验和数值分析。实验结果表明,与SWMMC相比,DWMMC具有更好的热性能。与SWMMC相比,DWMMC在6.7 W·cm−2下使玻璃底壁温度降低了17.3℃,并显著提高了温度均匀性。此外,DWMMC使对流换热系数(heff)提高了58.5%,最大heff为6976 W·m−2·K−1。综合性能评价参数COP也提高了35.8%。这种增强归因于DWMMC的双弯折流,有效地抑制了流动的不均匀分布,缓解了大面积的低速或停滞区。这种水力改进减小了速度边界层的厚度,加强了流体的混合。最后,DWMMC的应用演示表明,与传统的单面冷却相比,玻璃衬底嵌入微通道的双面冷却的热阻显著降低了57.5%。
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引用次数: 0
Thermal-mechanical analysis on foundation schemes of molten salt storage tanks 熔盐储罐基础方案的热-力学分析
IF 6.9 2区 工程技术 Q2 ENERGY & FUELS Pub Date : 2026-01-07 DOI: 10.1016/j.applthermaleng.2026.129749
Zhiyi Tang , Liang Hu , Yufan Cao , Fan Bai , Yifan Wu , Zhu Yang , Wen-Quan Tao
Molten salt storage tanks are crucial for long-term and high-capacity thermal energy storage and electricity peak shifting. However, their foundation is vulnerable to structural damage from material overtemperature and large deformations under combined thermal and hydrostatic loads. In this work, steady-state and transient thermal-mechanical behavior of non-cooled, air-cooled, and water-cooled foundation configurations are studied. The influence of high temperature on the structural response is analyzed. The result shows that thermal effects alter the deformation pattern especially at the edge of the foundation, and increase the maximum displacement from 105.0 mm to 125.5 mm. The investigations of steady-state air- and water-cooled cases show that the cooling tubes can effectively control and uniform the foundation temperature, particularly preventing the concrete overtemperature, while increasing the edge deformation, local stress concentration and maximum displacement. The influences of the environment temperature and cooling fluid velocity on the temperature and deformation are also investigated, and discussions between comparable air- and water-cooled cases have been made. Transient simulations of a 2-hour salt filling process and a 1-hour thermal storage process show that the average temperature of the upper layers rises following the variations of the molten salt temperature and level, and the foundation settlement increases with time. The structural response exhibits delayed thermal and mechanical equilibrium during thermal storage. The study also proposes three future research directions: improved foundation model, extended study scope, and artificial intelligence combination.
熔盐储罐是实现长期大容量蓄热和电力调峰的关键。然而,在热和静水复合荷载作用下,其基础容易受到材料过温和大变形的结构破坏。在这项工作中,研究了非冷却、风冷和水冷基础结构的稳态和瞬态热力学行为。分析了高温对结构响应的影响。结果表明:热效应改变了地基的变形模式,特别是在地基边缘,使最大位移从105.0 mm增加到125.5 mm;风冷和水冷稳态工况研究表明,冷却管能有效控制和均匀基础温度,特别是防止混凝土过温,同时增加边缘变形、局部应力集中和最大位移。研究了环境温度和冷却流体速度对温度和变形的影响,并对风冷和水冷的比较情况进行了讨论。对2 h盐充填过程和1 h蓄热过程的瞬态模拟表明,随着熔盐温度和水位的变化,上层平均温度升高,地基沉降随时间增加。在蓄热过程中,结构响应表现出延迟的热和力学平衡。提出了改进基础模型、扩大研究范围和人工智能结合三个未来的研究方向。
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引用次数: 0
An efficient low-carbon hydrogen-electricity cogeneration system based on coal-biomass complementary gasification coupling with solid oxide fuel cells 基于煤-生物质互补气化耦合固体氧化物燃料电池的高效低碳氢电热电联产系统
IF 6.9 2区 工程技术 Q2 ENERGY & FUELS Pub Date : 2026-01-07 DOI: 10.1016/j.applthermaleng.2026.129713
Zhong Zhang , Hao Yang , Sheng Li
Currently, hydrogen production primarily relies on fossil fuels, suffering from low energy efficiency and high carbon emissions. Developing low-carbon, efficient, and economically viable hydrogen production solutions has become a critical issue requiring urgent attention. This research proposes a hydrogen-electricity cogeneration system based on complementary coal-biomass gasification technology and solid oxide fuel cells. This system employs the synergistic effects of coal and biomass during gasification to enhance thermodynamic efficiency and reduce carbon emission intensity. Additionally, the system utilizes heat recovered from the SOFC stack and afterburner to supply thermal energy for the pyrolysis reaction. This enhances the energy grade matching between the thermal supply and demand sides, enabling efficient utilization of SOFC waste heat. This research utilized Aspen Plus software to simulate and validate both the novel and reference systems, evaluating their performance across three dimensions of thermodynamics, carbon emissions, and economic viability. Compared to the reference system, the novel system demonstrated a 4.64% improvement in energy efficiency, a 4.05% increase in exergy efficiency, and a 60.36% reduction in CO2 emissions. During the lifecycle, the new hydrogen-electric cogeneration system achieved a DPP of 5.42 years and an NPV of 171,057.92 k$, demonstrating better economic performance than the reference system. Sensitivity analysis indicates that increasing SOFC temperature, pressure, and fuel utilization enhances power generation performance. Additionally, hydrogen price, discount rate, and fuel cost are key parameters influencing system economics. This research offers new perspectives for developing efficient coal and biomass utilization technologies and low-carbon hydrogen production techniques.
目前,制氢主要依靠化石燃料,能源效率低,碳排放高。开发低碳、高效、经济可行的制氢解决方案已经成为一个迫切需要关注的关键问题。本研究提出了一种基于煤生物质互补气化技术和固体氧化物燃料电池的氢电热电联产系统。该系统利用煤和生物质在气化过程中的协同效应,提高热力效率,降低碳排放强度。此外,该系统利用SOFC堆和加力燃烧器回收的热量为热解反应提供热能。这增强了热供需双方之间的能源等级匹配,使SOFC废热得到有效利用。本研究利用Aspen Plus软件模拟并验证了新系统和参考系统,从热力学、碳排放和经济可行性三个维度评估了它们的性能。与参考系统相比,新系统的能源效率提高了4.64%,能源效率提高了4.05%,二氧化碳排放量减少了60.36%。在生命周期内,新系统的DPP为5.42年,NPV为171,057.92 k$,经济效益优于参考系统。灵敏度分析表明,提高SOFC温度、压力和燃料利用率可以提高发电性能。另外,氢气价格、折现率和燃料成本是影响系统经济性的关键参数。该研究为煤炭和生物质高效利用技术以及低碳制氢技术的发展提供了新的视角。
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引用次数: 0
Experimental study of phase change transpiration cooling based on temperature difference drive 基于温差驱动的相变蒸腾冷却实验研究
IF 6.9 2区 工程技术 Q2 ENERGY & FUELS Pub Date : 2026-01-06 DOI: 10.1016/j.applthermaleng.2026.129728
Shupeng Xie, Fei He, Caiyi He, Mu Li, Juntao Xu
Transpiration cooling is an efficient active thermal protection technique for high-heat-flux components of high-speed aircraft. Traditional transpiration cooling depends on external devices to deliver coolant to porous structures, which increases energy consumption and mass load. To address this issue, a phase change transpiration coolant self-supply system driven by temperature differences is proposed. In this system, non-uniform heat flux induces temperature gradients and thereby density variations within the internal piping, generating a pressure gradient to drive coolant flow. The performance of the coupled system with piping and porous structure exposed to high-temperature mainstream is evaluated using a high-enthalpy wind tunnel and a high-speed camera system. The results show that the self-supply system driven by temperature differences is feasible, providing a promising approach for active thermal protection in extreme environments. The cooling process can be divided into single-phase (SPFP) and two-phase (TPFP) regimes according to whether boiling occurred within the pipe during the stable stage. In the SPFP case, cooling mainly relies on liquid evaporation at the cooling cavity, achieving a maximum efficiency of only 5.1 %. In contrast, in the TPFP case, periodically generated bubbles in the pipeline carry large amounts of coolant into the porous structure, enhancing convective heat transfer and enabling a transition from gas-film to liquid-film cooling, thereby increasing the maximum efficiency to 59.9 %. Moreover, both temperature and temperature difference significantly affect the system performance. Higher temperature promotes boiling and bubble formation, while a larger temperature difference enhances coolant transport. The synergy of these factors intensifies heat transfer but may also amplify pressure oscillations.
蒸腾冷却是高速飞机高热流密度部件的一种有效的主动热防护技术。传统的蒸腾冷却依靠外部设备将冷却剂输送到多孔结构中,这增加了能耗和质量负荷。为了解决这一问题,提出了一种由温差驱动的相变蒸腾冷却剂自供系统。在该系统中,不均匀的热流导致内部管道内的温度梯度和密度变化,从而产生压力梯度来驱动冷却剂流动。采用高焓风洞和高速摄像系统对管道和多孔结构耦合系统在高温主流下的性能进行了评价。结果表明,基于温差驱动的自供电系统是可行的,为极端环境下的主动热保护提供了一种有希望的方法。根据稳定阶段管内是否发生沸腾,冷却过程可分为单相(SPFP)和两相(TPFP)两种。在SPFP的情况下,冷却主要依赖于冷却腔内的液体蒸发,最高效率仅为5.1%。相比之下,在TPFP的情况下,管道中周期性产生的气泡将大量冷却剂带入多孔结构,增强了对流换热,实现了从气膜冷却到液膜冷却的过渡,从而将最大效率提高到59.9%。而且,温度和温差对系统性能都有显著影响。较高的温度促进沸腾和气泡的形成,而较大的温差促进冷却剂的输送。这些因素的协同作用加强了热传递,但也可能放大压力振荡。
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引用次数: 0
Discrete thermal analysis of a marine reboiler under transcritical pressure conditions 跨临界压力条件下船用再沸器的离散热分析
IF 6.9 2区 工程技术 Q2 ENERGY & FUELS Pub Date : 2026-01-06 DOI: 10.1016/j.applthermaleng.2025.129668
Ibrahim Kaya, Yasin Ust
In response to the growing emphasis on greenhouse gas reduction, energy efficiency, and the decarbonization objectives of the International Maritime Organization, Transcritical Organic Rankine cycles have emerged as a promising technology for waste heat recovery at vessels. However, conducting thermal analyses of the heat exchangers operating under transcritical pressure conditions remains challenging due to the sharp variations in thermo-physical properties near the critical point. Consequently, conventional analysis methods, such as the effectiveness–number of transfer units (ε–NTU) method, often exhibit numerical instability or fail to converge under transcritical conditions. To overcome this limitation, the Discrete Sub-Heat Exchanger (DSHE) method was developed, wherein the heat exchanger is discretized into multiple sub-heat exchanger pairs with locally constant fluid properties at defined area condition. The method was implemented for the thermal analysis of a marine reboiler integrated into a waste heat recovery system operated by the exhaust gases of a 1980 kW turbocharged Tier-II marine diesel engine. Comparative simulations revealed that the ε–NTU method fails to converge at specific transcritical pressure and mass flow rate ranges, whereas the DSHE approach provides stable and consistent solutions. At higher pressures and mass flow rates, the deviation between outlet temperatures predicted by both methods decreases from approximately 20% to below 2%. Sensitivity analyses verified the numerical stability of the DSHE modelling, achieving convergence with residuals on the order of 10−5–10−6 beyond 1000 discrete elements. Overall, the DSHE method demonstrates a reliable and consistent tool for the thermal analysis of heat exchangers under transcritical pressure conditions, offering a robust approach for future studies involving two-phase or complex flow configurations with algorithm acceleration methods.
为了响应国际海事组织对温室气体减排、能源效率和脱碳目标的日益重视,跨临界有机朗肯循环已经成为一种很有前途的船舶废热回收技术。然而,由于在临界点附近热物理性质的急剧变化,对在跨临界压力条件下运行的热交换器进行热分析仍然具有挑战性。因此,传统的分析方法,如有效转移单元数(ε-NTU)方法,在跨临界条件下往往表现出数值不稳定性或不能收敛。为了克服这一限制,开发了离散亚热交换器(DSHE)方法,其中换热器被离散成多个亚热交换器对,这些亚热交换器对在规定的面积条件下具有局部恒定的流体性质。采用该方法对集成在废热回收系统中的船用再沸器进行了热分析,该系统由一台1980 kW涡轮增压Tier-II船用柴油机的废气驱动。对比仿真结果表明,ε-NTU方法在特定的跨临界压力和质量流量范围内不能收敛,而DSHE方法能提供稳定一致的解。在较高的压力和质量流量下,两种方法预测的出口温度之间的偏差从大约20%减小到2%以下。灵敏度分析验证了DSHE模型的数值稳定性,在超过1000个离散单元时,残差达到10−5 - 6阶。总体而言,DSHE方法为跨临界压力条件下换热器的热分析提供了可靠和一致的工具,为未来涉及两相或复杂流动配置的算法加速方法的研究提供了可靠的方法。
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引用次数: 0
Allam cycle technical and cost readiness levels: A review of the current technology status 全周期技术和成本准备水平:对当前技术状态的回顾
IF 6.9 2区 工程技术 Q2 ENERGY & FUELS Pub Date : 2026-01-06 DOI: 10.1016/j.applthermaleng.2025.129684
Ameer Al-Dafaie, Kumar Patchigolla, Dawid P. Hanak
The Allam Cycle emerged as a near-zero CO₂ emission power generation technology that promised higher efficiency and comparable specific costs to conventional gas-fired power plants with post-combustion CO2 capture. Yet its commercial deployment has been hindered by uncertainties in technical maturity, flexibility, and cost accuracy. This review provided a systematic assessment of the Allam Cycle using a combined technology readiness level (TRL), flexibility, and cost readiness level (CRL) framework that linked component-level maturity, operational flexibility requirements, and the quality of cost estimates.  A structured matrix was developed to evaluate critical components, including plant control system, oxy-combustor, sCO₂ turbine, recuperator, and oxygen storage, against TRL, flexibility (startup, shutdown, load, and fuel variation), and cost class, using criteria adapted from established guidelines and recent sCO₂ literature. The analysis showed that, despite the common perception that the Allam Cycle approaches TRL 7 at the system level, most critical components remained in the TRL 3–6 range for a utility-scale plant, with the turbine and recuperator constrained by operating at up to 300 bar and turbine inlet temperatures above 1000 °C, which further hinders the commercial deployment. Existing performance assessments reported net electrical efficiencies up to about 54–55 % (LHV) for natural gas-fired Allam Cycles and 37–43 % (HHV) for coal-based configurations, but these figures were largely based on steady-state models with simplified treatment of ASU integration and limited part-load analysis.  From a cost perspective, most evaluations relied on specific capital costs of roughly 1300–1850 $/kW and Class 4–5 estimates, corresponding to CRL 3–4 with wide cost tolerances and limited project-specific detail. The review identified the need for further experimental validation of oxy-combustors and sCO₂ turbines under relevant operating conditions, development of advanced recuperators, integrated dynamic control strategies with ASU and oxygen storage, and higher-fidelity, location-specific cost assessments. The proposed TRL–flexibility–CRL matrix provided a practical roadmap to align experimental programs, component development, and techno-economic studies with the TRL ≥ 7–8 thresholds required for large-scale power-sector investments. It also highlighted priorities for maturing the Allam Cycle into a commercially robust decarbonized power option.
Allam循环作为一种几乎零二氧化碳排放的发电技术出现,与传统的燃气发电厂相比,它具有更高的效率和相当的特定成本,并且具有燃烧后二氧化碳捕获功能。然而,由于技术成熟度、灵活性和成本准确性的不确定性,它的商业部署受到了阻碍。该审查使用组合技术准备水平(TRL)、灵活性和成本准备水平(CRL)框架对Allam周期进行了系统评估,该框架将组件级成熟度、操作灵活性需求和成本估算的质量联系起来。开发了一个结构化矩阵来评估关键部件,包括工厂控制系统、氧气燃烧器、sCO₂涡轮机、回热器和氧气储存,根据TRL、灵活性(启动、关闭、负载和燃料变化)和成本类别,使用根据既定指南和最近的sCO₂文献改编的标准。分析表明,尽管人们普遍认为Allam循环在系统层面接近TRL 7,但对于公用事业规模的工厂来说,大多数关键部件仍保持在TRL 3-6范围内,涡轮机和回热器的工作温度最高为300 bar,涡轮进口温度高于1000°C,这进一步阻碍了商业部署。现有的性能评估报告显示,天然气Allam循环的净电效率约为54 - 55% (LHV),煤基配置的净电效率为37 - 43% (HHV),但这些数据主要基于稳态模型,简化了ASU集成处理和有限的部分负荷分析。从成本的角度来看,大多数评估依赖于大约1300-1850美元/千瓦的具体资本成本和4-5级估算,与CRL 3-4相对应,具有广泛的成本公差和有限的项目具体细节。该综述指出,需要在相关运行条件下对氧燃烧器和sCO₂涡轮机进行进一步的实验验证,开发先进的回热器,集成ASU和氧气存储的动态控制策略,以及更高保真度、特定地点的成本评估。拟议的TRL -灵活性- crl矩阵提供了一个实用的路线图,以使实验计划、组件开发和技术经济研究与大规模电力部门投资所需的TRL≥7-8阈值保持一致。它还强调了将Allam循环成熟为商业上强大的脱碳电力选择的优先事项。
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引用次数: 0
Novel bi-axial bifacial solar concave concentrator (BBfSCcT): Integrated experimental validation, TRNSYS modeling, and thermoeconomic optimization 新型双轴双面太阳能凹面聚光器(BBfSCcT):综合实验验证、TRNSYS建模和热经济优化
IF 6.9 2区 工程技术 Q2 ENERGY & FUELS Pub Date : 2026-01-06 DOI: 10.1016/j.applthermaleng.2026.129710
Ridha Chargui , Mbarek Marzougui , Lotfi Snoussi
This paper introduces a new sensor-based solar tracking system (STS) model, the bi-axis bifacial solar concave concentrator with tracking system (BBfSCcT), designed to optimize solar energy harvesting. Its unprecedented design integrates two anti-parallel solar panels (TAPSP), one front-facing and one rear, with a bi-axis STS, complemented by a parabolic dish acting as a concave concentrator. This innovative configuration, precisely controlled by a microcontroller that processes sensor signals, ensures perpendicular alignment with incident sunlight. The study addresses a critical research gap by providing a comprehensive mathematical model and optimization strategy for the BBfSCcT system, as limited computational research has previously accentuated its unique advantages. A six-day experimental investigation, validated by numerical simulations using Python and TRNSYS software, assessed power output, temperature variations, and overall system efficiency. The key findings confirm that this synergistic TAPSP configuration with BxSTS significantly enhances energy capture, achieving impressive thermal efficiencies. While the rear-facing panel (BSPy) experienced some power reduction due to localized high temperatures resulting from concentrated irradiation, a thorough economic analysis revealed a robust Net Present Value (NPV) of $ 6737.50 over 25 years and a rapid payback period of 4.45 years. These results position the novel BBfSCcT system as an economically feasible and environmentally sound solution for advanced solar energy generation.
本文介绍了一种新的基于传感器的太阳能跟踪系统(STS)模型——双轴双面太阳能凹面集中器跟踪系统(BBfSCcT),旨在优化太阳能收集。其前所未有的设计集成了两个反平行太阳能电池板(TAPSP),一个正面,一个背面,双轴STS,辅以抛物面盘作为凹面聚光器。这种创新的配置由处理传感器信号的微控制器精确控制,确保与入射阳光垂直对齐。由于之前有限的计算研究强调了BBfSCcT系统的独特优势,该研究通过为BBfSCcT系统提供全面的数学模型和优化策略,解决了一个关键的研究空白。为期六天的实验研究,通过使用Python和TRNSYS软件进行数值模拟验证,评估了功率输出、温度变化和整体系统效率。主要研究结果证实,这种与BxSTS协同的TAPSP配置显着提高了能量捕获,实现了令人印象深刻的热效率。虽然后面板(BSPy)由于集中辐照导致局部高温而降低了一些功率,但全面的经济分析显示,25年内的净现值(NPV)为6737.50美元,投资回收期为4.45年。这些结果使新型BBfSCcT系统成为一种经济可行且环保的先进太阳能发电解决方案。
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引用次数: 0
Multi-objective optimization of manifold micro/mini-channel heat sink through cooling with microencapsulated phase change material slurries 微囊化相变材料浆料冷却流形微/小通道散热器的多目标优化
IF 6.9 2区 工程技术 Q2 ENERGY & FUELS Pub Date : 2026-01-06 DOI: 10.1016/j.applthermaleng.2026.129731
Chen Wang, Shugang Wang, Jihong Wang
Micro/mini-channel heat sinks using microencapsulated phase change material slurries offer great potential for high-heat-flux cooling. However, achieving balanced thermo-hydraulic performance remains challenging due to the complex coupling among latent heat storage, flow resistance, and heat transfer. A three-dimensional model of a manifold micro/mini-channel heat sink was developed, and a Taguchi-Grey relational analysis framework was applied to perform multi-objective optimization of heat transfer, flow resistance, phase-change utilization, and temperature uniformity. Parametric analysis considered geometric and operational factors, including fin arrangement, fin and manifold dimensions, slurry concentration, and inlet temperature, to coordinate performance indicators. Results showed that fin height dominates convective heat transfer (84.22 %), manifold height strongly affects flow resistance (29.51 %) and phase-change utilization (62.2 %), and fin arrangement (34.19 %) mainly controls temperature uniformity. The optimized configuration yields a 3.5 K reduction in heated-wall temperature, a 9.72 % decrease in friction factor, and a 63.5 % improvement in temperature uniformity compared with the conventional design. The proposed optimization framework not only achieves a balanced improvement in thermo-hydraulic and phase-change performance but also clarifies the physical roles of key design parameters. This work therefore establishes a practical and interpretable multi-objective design strategy for manifold micro /mini-channel heat sinks employing microencapsulated phase change material slurries in compact electronic and energy systems.
使用微封装相变材料浆料的微/迷你通道散热器为高热流密度冷却提供了巨大的潜力。然而,由于潜热储存、流动阻力和传热之间的复杂耦合,实现平衡的热工性能仍然具有挑战性。建立了流形微/迷你通道散热器的三维模型,并应用田口灰关联分析框架对其传热、流动阻力、相变利用和温度均匀性进行了多目标优化。参数分析考虑几何和操作因素,包括翅片布置、翅片和流形尺寸、浆液浓度和入口温度,以协调性能指标。结果表明:翅片高度主导对流换热(84.22%),流形高度对流动阻力(29.51%)和相变利用(62.2%)影响较大,翅片布置主要控制温度均匀性(34.19%)。与传统设计相比,优化后的结构使热壁温度降低了3.5 K,摩擦系数降低了9.72%,温度均匀性提高了63.5%。提出的优化框架不仅实现了热液性能和相变性能的平衡提高,而且明确了关键设计参数的物理作用。因此,这项工作建立了一个实用的和可解释的多目标设计策略,用于在紧凑型电子和能源系统中使用微封装相变材料浆料的流形微/迷你通道散热器。
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引用次数: 0
Modeling of hydrogen sulfide formation in pulverized coal combustion and its application to a full-scale opposed-firing boiler 煤粉燃烧过程中硫化氢生成的模拟及其在全尺寸对燃锅炉上的应用
IF 6.9 2区 工程技术 Q2 ENERGY & FUELS Pub Date : 2026-01-06 DOI: 10.1016/j.applthermaleng.2026.129721
Hiroki Umetsu , Kenji Tanno , Hiroaki Watanabe , Masahiko Morinaga , Toshiaki Fukada
In pulverized coal-fired power plants, sulfur-induced corrosion of water wall tubes remains a significant operational issue. Accurate prediction of hydrogen sulfide (H2S) concentration distributions within the furnace is essential for evaluating corrosion risks and planning maintenance strategies. However, detailed reaction mechanisms for H2S prediction are computationally expensive, and simplified models have not been sufficiently validated for large-scale boilers, leaving a practical research gap. In this study, a simplified global reaction model was developed based on detailed chemical reaction analysis. We introduce a reduced model that preserves predictive accuracy while improving computational efficiency for furnace-scale simulations. The model's validity was evaluated by comparing simulation results with experimental data at two vastly different scales, differing by three orders of magnitude, under two-stage combustion conditions: a 760 kW (thermal input) single-burner test facility and a full-scale 2500 MW (thermal input) opposed-firing boiler. The results demonstrated good agreement with experimental data, including trends in H2S peak concentrations due to variations in coal properties such as fuel ratio and sulfur content. Subsequently, the influence of coal properties on the wall-side distribution of H2S concentration in the boiler was also investigated. The analysis revealed that while the effect of fuel ratio on H2S distribution was limited, sulfur content had a strong positive linear correlation with wall-peak H2S concentrations across all cases. These findings indicate the practical applicability of the simplified model for corrosion risk assessment and support its potential use as a tool for coal selection and furnace operation optimization in utility boilers.
在煤粉电厂中,硫致水冷壁管腐蚀仍然是一个重要的运行问题。准确预测炉内硫化氢(H2S)浓度分布对于评估腐蚀风险和规划维护策略至关重要。然而,H2S预测的详细反应机理在计算上是昂贵的,并且简化模型尚未在大型锅炉中得到充分验证,留下了实际研究的空白。在详细的化学反应分析的基础上,建立了一个简化的全局反应模型。我们引入了一个简化的模型,在保持预测精度的同时提高了炉级模拟的计算效率。通过将模拟结果与两级燃烧条件下的实验数据进行比较,对模型的有效性进行了评估,两级燃烧条件下的模拟结果相差三个数量级:760千瓦(热输入)单燃烧器测试设施和全尺寸2500兆瓦(热输入)对燃锅炉。结果与实验数据吻合良好,包括硫化氢峰值浓度的变化趋势,这是由于煤的特性(如燃料比和硫含量)的变化。随后,研究了煤的性质对锅炉内H2S浓度壁面分布的影响。分析表明,虽然燃料比对H2S分布的影响有限,但在所有情况下,硫含量与壁峰H2S浓度都有很强的线性正相关。这些发现表明简化模型在腐蚀风险评估中的实际适用性,并支持其作为公用事业锅炉选煤和炉体运行优化工具的潜在用途。
{"title":"Modeling of hydrogen sulfide formation in pulverized coal combustion and its application to a full-scale opposed-firing boiler","authors":"Hiroki Umetsu ,&nbsp;Kenji Tanno ,&nbsp;Hiroaki Watanabe ,&nbsp;Masahiko Morinaga ,&nbsp;Toshiaki Fukada","doi":"10.1016/j.applthermaleng.2026.129721","DOIUrl":"10.1016/j.applthermaleng.2026.129721","url":null,"abstract":"<div><div>In pulverized coal-fired power plants, sulfur-induced corrosion of water wall tubes remains a significant operational issue. Accurate prediction of hydrogen sulfide (H<sub>2</sub>S) concentration distributions within the furnace is essential for evaluating corrosion risks and planning maintenance strategies. However, detailed reaction mechanisms for H<sub>2</sub>S prediction are computationally expensive, and simplified models have not been sufficiently validated for large-scale boilers, leaving a practical research gap. In this study, a simplified global reaction model was developed based on detailed chemical reaction analysis. We introduce a reduced model that preserves predictive accuracy while improving computational efficiency for furnace-scale simulations. The model's validity was evaluated by comparing simulation results with experimental data at two vastly different scales, differing by three orders of magnitude, under two-stage combustion conditions: a 760 kW (thermal input) single-burner test facility and a full-scale 2500 MW (thermal input) opposed-firing boiler. The results demonstrated good agreement with experimental data, including trends in H<sub>2</sub>S peak concentrations due to variations in coal properties such as fuel ratio and sulfur content. Subsequently, the influence of coal properties on the wall-side distribution of H<sub>2</sub>S concentration in the boiler was also investigated. The analysis revealed that while the effect of fuel ratio on H<sub>2</sub>S distribution was limited, sulfur content had a strong positive linear correlation with wall-peak H<sub>2</sub>S concentrations across all cases. These findings indicate the practical applicability of the simplified model for corrosion risk assessment and support its potential use as a tool for coal selection and furnace operation optimization in utility boilers.</div></div>","PeriodicalId":8201,"journal":{"name":"Applied Thermal Engineering","volume":"289 ","pages":"Article 129721"},"PeriodicalIF":6.9,"publicationDate":"2026-01-06","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145974997","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}
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Applied Thermal Engineering
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