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CFD Modeling to Evaluate User Safety by Using Flame Retardants in Asphalt Road Pavements during Large Tunnel Fires
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作者 Ciro Caliendo Isidoro Russo Gianluca Genovese 《Computer Modeling in Engineering & Sciences》 2025年第7期693-715,共23页
Road pavements in tunnels are usually made of asphalt mixtures,which,unfortunately,are flammable materials.Hence,this type of pavement could release heat,and more specifically smoke,in the event of a tunnel fire,there... Road pavements in tunnels are usually made of asphalt mixtures,which,unfortunately,are flammable materials.Hence,this type of pavement could release heat,and more specifically smoke,in the event of a tunnel fire,thereby worsening the environmental conditions for human health.Extensive research has been conducted in recent years to enhance the fire reaction of traditional asphalt mixtures for the road pavements used in tunnels.The addition of the Flame Retardants(FRs)in conventional asphalt mixtures appears to be promising.Nevertheless,the potential effects of the FRs in terms of the reduction in consequences on tunnel users in the event of a large fire do not seem to have been sufficiently investigated by using fluid dynamics analysis as a computational tool.Given this gap of knowledge,this article aims to quantitatively evaluate whether the use of flame-retarded asphalt mixtures,as opposed to traditional ones without FRs,might mitigate the adverse effects on the safety of evacuees and fire brigade by performing numerical analyses in the case of a tunnel fire.To achieve this goal,3D Computational Fluid Dynamics(CFD)models,which were executed using the Fire Dynamics Simulator(FDS)tool,were established in the case of a major fire of a Heavy Goods Vehicle(HGV)characterized by a maximum Heat Release Rate(HRRmax)of 100 MW.The people evacuation process was also simulated,and the Evac tool was used.Compared to the traditional asphalt pavements without FRs,the simulation findings indicated that the addition of the FRs causes a reduction in CO and CO_(2)levels in the tunnel during the aforementioned fire,with a minor number of evacuees being exposed to the risk of incapacity to self-evacuate,as well as certain safety benefits for the operability of the firefighters entering the tunnel downstream of the fire when the tunnel is naturally ventilated. 展开更多
关键词 Asphalt pavement combustion flame retardants road tunnel fire cfd modeling user safety operability of fire brigade
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Simulating Urban Flow and Dispersion in Beijing by Coupling a CFD Model with the WRF Model 被引量:13
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作者 缪育聪 刘树华 +3 位作者 陈笔澄 张碧辉 王姝 李书严 《Advances in Atmospheric Sciences》 SCIE CAS CSCD 2013年第6期1663-1678,共16页
The airflow and dispersion of a pollutant in a complex urban area of Beijing, China, were numerically examined by coupling a Computational Fluid Dynamics (CFD) model with a mesoscale weather model. The models used w... The airflow and dispersion of a pollutant in a complex urban area of Beijing, China, were numerically examined by coupling a Computational Fluid Dynamics (CFD) model with a mesoscale weather model. The models used were Open Source Field Operation and Manipulation (OpenFOAM) software package and Weather Research and Forecasting (WRF) model. OpenFOAM was firstly validated against wind-tunnel experiment data. Then, the WRF model was integrated for 42 h starting from 0800 LST 08 September 2009, and the coupled model was used to compute the flow fields at 1000 LST and 1400 LST 09 September 2009. During the WRF-simulated period, a high pressure system was dominant over the Beijing area. The WRF-simulated local circulations were characterized by mountain valley winds, which matched well with observations. Results from the coupled model simulation demonstrated that the airflows around actual buildings were quite different from the ambient wind on the boundary provided by the WRF model, and the pollutant dispersion pattern was complicated under the influence of buildings. A higher concentration level of the pollutant near the surface was found in both the step-down and step-up notches, but the reason for this higher level in each configurations was different: in the former, it was caused by weaker vertical flow, while in the latter it was caused by a downward-shifted vortex. Overall, the results of this study suggest that the coupled WRF-OpenFOAM model is an important tool that can be used for studying and predicting urban flow and dispersions in densely built-up areas. 展开更多
关键词 WRF model cfd model OPENFOAM dispersion.
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CFD Model of Dense Gas-solid Systems in Jetting Fluidized Beds 被引量:2
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作者 Kai Zhang Jiyu Zhang +1 位作者 Biiang Zhang John Yates 《Chemical Research in Chinese Universities》 SCIE CAS CSCD 2002年第2期117-120,共4页
A CFD code has been developed based on the conservation principles describing gas and solid flow in fluidized beds. This code is employed to simulate not only the spatiotemporal gas and solid phase velocities and v... A CFD code has been developed based on the conservation principles describing gas and solid flow in fluidized beds. This code is employed to simulate not only the spatiotemporal gas and solid phase velocities and voidage profiles in a two dimensional bed but also fluid dynamics in the jet region. The computational results show that gas flow direction is upward in the entire bed accompanied with random local circulations, whilst solid flow direction is upward at the center and downward near the wall. The radical reason of strong back mixing of solid particles and good transfer behavior between two phases is that the jet entrains solid particles. Numerical calculation indicates that gas velocity, solid velocity and pressure profile have a significant change when the voidage is 0 8. The simulated time averaged voidage profiles agree with the experimental results and simulated data reported by Gidaspow and Ettehadieh(1983). Therefore, CFD model can be regarded as a useful tool to study the jet characteristics in dense gas solid fluidized beds. 展开更多
关键词 Jetting fluidized bed cfd model Gas solid dynamics Modified SIMPLE
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Improved CFD modeling of full dissolution of alumina particles in aluminum electrolysis cells considering agglomerate formation 被引量:2
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作者 Shui-qing ZHAN Ming-mei JIANG +1 位作者 Jun-feng WANG Jian-hong YANG 《Transactions of Nonferrous Metals Society of China》 SCIE EI CAS CSCD 2021年第11期3579-3590,共12页
The full alumina dissolution process in aluminum electrolysis cells was investigated using an improved computational fluid dynamics(CFD)model based on the previous researches by consideration of agglomerate formation.... The full alumina dissolution process in aluminum electrolysis cells was investigated using an improved computational fluid dynamics(CFD)model based on the previous researches by consideration of agglomerate formation.The results show that the total mass of alumina agglomerate and its maximum size are mainly dependent on the feeding amount and increase with increasing it.Higher superheat can effectively inhibit the agglomerate formation and thus promote the full alumina dissolution behavior.The full alumina dissolution process mainly includes a fast stage and a slow stage,with an average dissolution rate of 17.24 kg/min and 1.53 kg/min,respectively.About 50%(mass percentage)of the total alumina particles,almost all of which are the well-dispersed alumina fine grains,dissolve within the fast dissolution stage of about 10 s.The maximum values of the average dissolution rate and final percentage of the cumulative dissolved alumina mass are obtained with a feeding amount of 1.8 kg for a superheat of 12℃.The formation of the alumina agglomerates and slow dissolution characteristics play a dominant role in the full dissolution of alumina particles. 展开更多
关键词 aluminum electrolysis alumina dissolution agglomerate formation theoretical modeling cfd modeling
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CFD modelling of Iongwall goaf gas flow to improve gas capture and prevent goaf self-heating 被引量:1
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作者 REN Ting-xiang 《Journal of Coal Science & Engineering(China)》 2009年第3期225-228,共4页
CFD models have been developed to investigate the Iongwall goaf gas flow patternsunder different mining and geological control conditions.The Iongwall goaf wastreated as porous regions and gas flow was modelled as a m... CFD models have been developed to investigate the Iongwall goaf gas flow patternsunder different mining and geological control conditions.The Iongwall goaf wastreated as porous regions and gas flow was modelled as a momentum sink added to themomentum equation.Gas desorption from the caved goaf and destressed coal seamswithin the mining disturbed area was modelled as additional mass sources in the continuityequation.These CFD models were developed according to specific Iongwall layoutsand calibrated against field monitoring data.Two case studies were presented demonstratingthe application of CFD modelling of goaf gas flow characteristics for improved goafgas capture and the reduction of oxygen ingress into the goaf areas for self-heating prevention.Results from the case studies indicate that the optimum goaf drainage strategywould be a combination of shallow (near the face) and deep holes to improve the overalldrainage efficiency and gas purity.For gassy Iongwall faces retreating against the seam dip,it is recommended to conduct cross-measure roof hole drainage targeting the fracturedzones overlying the return corner,rather than high capacity surface goaf drainage deep inthe goaf. 展开更多
关键词 cfd modelling Iongwall goaf gas goaf drainage self-heating prevention
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A CFD Model to Evaluate Near-Surface Oil Spill from a Broken Loading Pipe in Shallow Coastal Waters
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作者 Portia Felix Lee Leon +2 位作者 Derek Gay Stefano Salon Hazi Azamathulla 《Fluid Dynamics & Materials Processing》 EI 2024年第1期59-77,共19页
Oil spills continue to generate various issues and concerns regarding their effect and behavior in the marine environment,owing to the related potential for detrimental environmental,economic and social implications.I... Oil spills continue to generate various issues and concerns regarding their effect and behavior in the marine environment,owing to the related potential for detrimental environmental,economic and social implications.It is essential to have a solid understanding of the ways in which oil interacts with the water and the coastal ecosystems that are located nearby.This study proposes a simplified model for predicting the plume-like transport behavior of heavy Bunker C fuel oil discharging downward from an acutely-angled broken pipeline located on the water surface.The results show that the spill overall profile is articulated in three major flow areas.The first,is the source field,i.e.,a region near the origin of the initial jet,followed by the intermediate or transport field,namely,the region where the jet oil flow transitions into an underwater oil plume flow and starts to move horizontally,and finally,the far-field,where the oil re-surface and spreads onto the shore at a significant distance from the spill site.The behavior of the oil in the intermediate field is investigated using a simplified injection-type oil spill model capable of mimicking the undersea trapping and lateral migration of an oil plume originating from a negatively buoyant jet spill.A rectangular domain with proper boundary conditions is used to implement the model.The Projection approach is used to discretize a modified version of the Navier-Stokes equations in two dimensions.A benchmark fluid flow issue is used to verify the model and the results indicate a reasonable relationship between specific gravity and depth as well as agreement with the aerial data and a vertical temperature profile plot. 展开更多
关键词 cfd model Navier-Stokes equations projection method water surface oil spill shallow coastal waters
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CFD modeling of reaction and mass transfer through a single pellet: Catalytic oxidative coupling of methane 被引量:1
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作者 Siavash Seyednejadian Nakisa Yaghobi +1 位作者 Ramin Maghrebi Leila Vafajoo 《Journal of Natural Gas Chemistry》 EI CAS CSCD 2011年第4期356-363,共8页
In this study a mathematical model of a small scale single pellet for the oxidative coupling of methane(OCM)over titanite pervoskite is developed.The method is based on a computational fluid dynamics(CFD)code whic... In this study a mathematical model of a small scale single pellet for the oxidative coupling of methane(OCM)over titanite pervoskite is developed.The method is based on a computational fluid dynamics(CFD)code which known as Fluent may be adopted to model the reactions that take place inside the porous catalyst pellet.The steady state single pellet model is coupled with a kinetic model and the intra-pellet concentration profiles of species are provided.Subsequent to achieving this goal,a nonlinear reaction network consisting of nine catalytic reactions and one gas phase reaction as an external program is successfully implemented to CFD-code as a reaction term in solving the equations.This study is based on the experimental design which is conducted in a differential reactor with a Sn/BaTiO3 catalyst(7-8 mesh) at atmospheric pressure,GHSV of 12000 h-1,ratio of methane to oxygen of 2,and three different temperatures of 1023,1048 and 1073 K.The modeling results such as selectivity and conversion at the pellet exit are in good agreement with the experimental data.Therefore,it is suggested that to achieve high yield in OCM process the modeling of the single pellet should be considered as the heart of catalytic fixed bed reactor. 展开更多
关键词 catalyst pellet oxidative coupling of methane modeling cfd catalytic reactions ETHANE
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A CFD Model for Fluid Dynamics in a Gas-fluidised Bed 被引量:1
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作者 ZHANGKai StefanoBrandani 《Chemical Research in Chinese Universities》 SCIE CAS CSCD 2004年第4期483-488,共6页
A modified particle bed model derived from the two-fluid momentum balance equations was employed to predict the gas-fluidised bed behaviour. Additional terms are included in both the fluid and the particle momentum ba... A modified particle bed model derived from the two-fluid momentum balance equations was employed to predict the gas-fluidised bed behaviour. Additional terms are included in both the fluid and the particle momentum balance equations to take into account the effect of the dispersed solid phase. This model has been extended to two-dimensional formulations and has been implemented in the commercial code CFX 4.3. The model correctly simulates the homogeneous fluidisation of Geldart Group A and the bubbling fluidisation of Geldart Group B in gas-solid fluidised beds. 展开更多
关键词 Gas-solid fluidised beds Modified particle bed model HYDRODYNAMICS cfd simulation
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Design Wind Speed Evaluation Technique in Wind Turbine Installation Point by Using the Meteorological and CFD Models
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作者 Takanori Uchida 《Journal of Flow Control, Measurement & Visualization》 2018年第3期168-184,共17页
It is highly important in Japan to choose a good site for wind turbines, because the spatial distribution of wind speed is quite complicated over steep complex terrain. We have been developing the unsteady numerical m... It is highly important in Japan to choose a good site for wind turbines, because the spatial distribution of wind speed is quite complicated over steep complex terrain. We have been developing the unsteady numerical model called the RIAM-COMPACT (Research Institute for Applied Mechanics, Kyushu University, Computational Prediction of Airflow over Complex Terrain). The RIAM-COMPACT is based on the LES (Large-Eddy Simulation). The object domain of the RIAM-COMPACT is from several m to several km, and can predict the airflow and gas diffusion over complex terrain with high precision. In the present paper, the design wind speed evaluation technique in wind turbine installation point by using the mesoscale meteorological model and RIAM-COMPACT CFD model was proposed. The design wind speed to be used for designing WTGs can be calculated by multiplying the ratio of the mean wind speed at the hub-height to the mean upper-air wind speed at the inflow boundary, i.e., the fractional increase of the mean hub-height wind speed, by the reduction ratio, R. The fractional increase of the mean hub-height wind speed was evaluated using the CFD simulation results. This method was proposed as Approach 1 in the present paper. A value of 61.9 m/s was obtained for the final design wind speed, Uh, in Approach 1. In the evaluation procedure of the design wind speed in Approach 2, neither the above-mentioned reduction rate, R, nor an upper-air wind speed of 1.7 Vo, where Vo is the reference wind speed, was used. Instead, the value of the maximum wind speed which was obtained from the typhoon simulation for each of the investigated wind directions was adopted. When the design wind speed was evaluated using the 50-year recurrence value, the design wind speed was 48.3 m/s. When a somewhat conservative safety factor was applied, that is, when the 100 year recurrence value was used instead, the design wind speed was 52.9 m/s. 展开更多
关键词 Design WIND SPEED Complex TERRAIN METEOROLOGICAL model cfd model
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Fundamentals of Direct Inverse CFD Modeling to Detect Air Pollution Sources in Urban Areas 被引量:1
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作者 Mahmoud Bady 《Computational Water, Energy, and Environmental Engineering》 2013年第2期31-42,共12页
This paper presents the fundamentals of direct inverse modeling using CFD simulations to detect air pollution sources in urban areas. Generally, there are four techniques used for detecting pollution sources: the anal... This paper presents the fundamentals of direct inverse modeling using CFD simulations to detect air pollution sources in urban areas. Generally, there are four techniques used for detecting pollution sources: the analytical technique, the optimization technique, the probabilistic technique, and the direct technique. The study discusses the potentialities and limits of each technique, where the direct inverse technique is focused. Two examples of applying the direct inverse technique in detecting pollution source are introduced. The difficulties of applying the direct inverse technique are investigated. The study reveals that the direct technique is a promising tool for detecting air pollution source in urban environments. However, more efforts are still needed to overcome the difficulties explained in the study. 展开更多
关键词 INVERSE modeling OUTDOOR Environments REVERSE Simulation cfd
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催化裂化提升管反应器CFD模拟的研究进展
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作者 钟又皆秀 丁丽芹 钟汉斌 《广州化工》 2026年第5期12-14,25,共4页
流化催化裂化(FCC)是石油炼制的关键技术,提升管作为该工艺的核心反应器,其内部的复杂流动与反应直接影响产品分布和质量。通过计算流体力学(CFD)进行数值模拟有助于揭示这一过程内在机制,辅助设计和优化FCC工艺设备。对CFD模拟中的流... 流化催化裂化(FCC)是石油炼制的关键技术,提升管作为该工艺的核心反应器,其内部的复杂流动与反应直接影响产品分布和质量。通过计算流体力学(CFD)进行数值模拟有助于揭示这一过程内在机制,辅助设计和优化FCC工艺设备。对CFD模拟中的流动模型和反应动力学模型,以及FCC提升管反应器的研究进展进行了总结。通过改进曳力模型、考虑颗粒尺度效应及液滴的影响可显著提升模拟的准确性,为反应器结构及工艺条件的优化提供了理论依据。最后指出未来耦合分子水平动力学模型、提升模拟精度与计算效率、实现多尺度高效耦合将是推动FCC模拟技术进步的关键。 展开更多
关键词 流化催化裂化 提升管反应器 计算流体力学 流动模型 反应动力学模型
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基于CFD的埋地掺氢天然气管道泄漏扩散特性研究
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作者 卜凡熙 冷春苗 +3 位作者 黄作男 王文煜 高欣琪 王志华 《管道保护》 2026年第2期70-82,共13页
氢气在缓解化石能源短缺和促进新能源转型过程中扮演重要角色的同时,其储存和运输面临着新的挑战。本文采用计算流体力学(Computational Fluid Dynamics,CFD)数值模拟的方法对比了掺氢前后埋地天然气管道泄漏流场分布规律,基于正交试验... 氢气在缓解化石能源短缺和促进新能源转型过程中扮演重要角色的同时,其储存和运输面临着新的挑战。本文采用计算流体力学(Computational Fluid Dynamics,CFD)数值模拟的方法对比了掺氢前后埋地天然气管道泄漏流场分布规律,基于正交试验设计多因素协同作用下的模拟方案,根据模拟结果采用最小二乘法和多元非线性回归理论建立了地面最高风险点气体浓度预测模型。结果表明:掺氢后会扩大气体在土壤中的压力、速度和浓度的分布范围,当掺氢比由0增加至30%,对应的爆炸危险区半径从1.523 m扩大至1.612 m,增加了5.8%。地面最高风险点气体浓度预测模型的最大误差为8.359%,平均误差为5.744%。本研究为埋地掺氢天然气管道泄漏事故风险评价和二次爆炸事故预防提供依据。 展开更多
关键词 掺氢天然气 埋地管道 泄漏扩散 cfd 预测模型
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煤矿通风应急响应示踪气体与CFD模拟研究
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作者 王剑亮 《煤炭科技》 2026年第1期45-49,共5页
在煤矿突发事件应急处置过程中,存在救援人员无法直接进入事故地点的情况,此时通过远程手段快速准确分析矿井通风系统运行状态,助力矿山救援队伍做出科学决策至关重要。为此,结合示踪气体技术和计算流体动力学(CFD)建模方法,通过向煤矿... 在煤矿突发事件应急处置过程中,存在救援人员无法直接进入事故地点的情况,此时通过远程手段快速准确分析矿井通风系统运行状态,助力矿山救援队伍做出科学决策至关重要。为此,结合示踪气体技术和计算流体动力学(CFD)建模方法,通过向煤矿通风系统释放特定示踪气体,利用CFD模型对矿井内的气流流动进行数值模拟,建立4种通风破坏场景以模拟不同程度或类型的通风系统失效情况,并将模型预测结果与现场实验数据进行了对比验证,确保模型分析的有效性和准确性。实验与模型分析结果显示,结合示踪气体剖面的直接观测与CFD模型的数值模拟,能够有效识别矿井通风系统的变化特征,有助于提升矿井应急救援的响应速度和决策质量。 展开更多
关键词 矿井通风 示踪气体 cfd建模
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基于CFD-PBM耦合模型的搅拌槽中气体分散特性研究
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作者 李凯旋 李政权 +3 位作者 张博群 王贻得 石昊宇 周宗彦 《中国有色冶金》 北大核心 2026年第1期113-124,共12页
在气液搅拌的混合与分散过程中,气泡的尺寸和分布不仅决定气泡的上升速度和气体在液相中的停留时间,还直接影响含气率及气液接触面积。诸多学者采用计算流体动力学(CFD)研究了气泡尺寸分布、气体含量和液体速度,但均没有考虑气泡聚并和... 在气液搅拌的混合与分散过程中,气泡的尺寸和分布不仅决定气泡的上升速度和气体在液相中的停留时间,还直接影响含气率及气液接触面积。诸多学者采用计算流体动力学(CFD)研究了气泡尺寸分布、气体含量和液体速度,但均没有考虑气泡聚并和破碎的影响。群体平衡模型(PBM)重建了气泡尺寸分布,构建了气泡破碎和聚并的核函数,PBM与CFD结合,可以在搅拌罐等工艺设备中获得相当准确的气泡尺寸。本文采用CFD-PBM耦合模型,研究搅拌槽内气液分散过程的流体动力学,探究转速和气体流量对气泡尺寸分布、流场、数量浓度及气含率的影响,得到以下主要结论。该模型精度高于Basavarajappa的预测,且模拟结果对比最大误差不超过10%,能很好的预测气泡尺寸分布;搅拌转速显著影响气液混合效率,高转速(400 r/min)下气泡尺寸更小且分布均匀,气液传质性能显著提升;低气体流量(0.5 vvm)下,气泡生成量较少且分布不均匀,适当增加气体流量(0.7 vvm)有助于延长气泡滞留时间,但过高流量(0.9 vvm)可能导致气泡聚并和传质效率下降;高转速(400 r/min)下,搅拌桨叶片背液面区域会出现明显的气穴现象,这是由局部负压导致气体汇聚形成稳定的气腔,对搅拌效率和气液分散效果产生不利影响;通过合理调控转速和叶轮设计,可以减轻气穴现象所带来的不利影响,从而进一步提升搅拌效率和气体分散效果。实际生产中,可以通过优化搅拌速度与气体流量,来改善气泡分布和气液混合效果。 展开更多
关键词 搅拌槽 气液两相 cfd-PBM耦合模型 分散特性 气泡分布
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基于CFD-DEM方法的高炉炉料轨迹落点预测
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作者 何潺 刘丕亮 +1 位作者 林帅辉 吴博 《冶金能源》 北大核心 2026年第1期62-69,共8页
针对当前高炉炉料落点预测的不足,文章采用CFD-DEM方法分析高炉炉料轨迹和落点位置,并利用程树森等提出的数学模型验证CFD-DEM模型的准确性。该方法全面考虑多种影响因素,包括科里奥利力、煤气流量、溜槽的旋转速度和倾角等,直观和精准... 针对当前高炉炉料落点预测的不足,文章采用CFD-DEM方法分析高炉炉料轨迹和落点位置,并利用程树森等提出的数学模型验证CFD-DEM模型的准确性。该方法全面考虑多种影响因素,包括科里奥利力、煤气流量、溜槽的旋转速度和倾角等,直观和精准地再现炉料在高炉内的运动过程。结果表明:当溜槽转速为1.05 rad/s时,科里奥利力对焦炭和矿石落点的影响分别达到28%和22%,煤气流非均匀性使焦炭和矿石的落点半径外移2.74%和3.87%。精准预测料流轨迹落点必须综合考虑科里奥利力和煤气流的影响。与数学模型对比,CFD-DEM模型对焦炭和矿石落点半径预测均方根误差分别为0.060 m和0.055 m,最大相对偏差不超过5%,与数学模型预测结果几乎一致,因此能够准确预测高炉炉料轨迹落点,为后续高炉布料操作提供新的理论依据。 展开更多
关键词 无料钟炉顶高炉 cfd-DEM 数学模型验证 科里奥利力 气固耦合
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基于CFD-DEM耦合的碾米颗粒运动模拟与方法研究
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作者 杨勇 周龙 +2 位作者 范吉军 余南辉 李园 《食品与机械》 北大核心 2026年第1期64-71,共8页
[目的]针对卧式碾米机在碾米过程中造成颗粒破碎和过碾的问题,提出通过改变吸风气流方向提高糙米颗粒的碾磨质量。[方法]采用CFD-DEM耦合方法,分别对上吸风10 m/s、下吸风5 m/s和无风速3种状态进行数值仿真分析,并通过物理样机碾磨试验... [目的]针对卧式碾米机在碾米过程中造成颗粒破碎和过碾的问题,提出通过改变吸风气流方向提高糙米颗粒的碾磨质量。[方法]采用CFD-DEM耦合方法,分别对上吸风10 m/s、下吸风5 m/s和无风速3种状态进行数值仿真分析,并通过物理样机碾磨试验验证仿真结果。[结果]随着气流方向由上吸风转变到下吸风,颗粒沿Y轴的上升速度vy及三轴合成平均速度v整体降低,同层段位置处上吸风颗粒速度vy大于下吸风的,在碾白室中下部处明显观察到上吸风颗粒平均速度v大于下吸风颗粒的,碾磨区域内颗粒运动能力的差异导致容易过碾和破损区域的受力情况明显不同,颗粒运动能力强时碾白室底部颗粒受到的挤压力减小,颗粒运动能力弱时碾白室底部颗粒受到的挤压力增大;颗粒翻滚角速度在上吸风的作用下,对比无风速和下吸风效果增强;每种状态下3次的物理试验结果,上吸风10 m/s、无风速和下吸风5 m/s的碾磨度平均值分别为1.90%,2.20%,2.78%,破损率平均值分别为0.37%,0.46%,0.60%。[结论]上吸风状态下颗粒碾磨过程中的流动和受力特性优于无风速和下吸风的情况;上吸风比无风速和下吸风的碾磨度和破碎率明显下降。 展开更多
关键词 碾米颗粒 cfd-DEM 颗粒流动 多孔介质模型
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WRF-CFD模式耦合的山地风电场非定常仿真方法与验证
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作者 马国林 宋翌蕾 +1 位作者 田琳琳 赵宁 《中国电机工程学报》 北大核心 2026年第2期679-690,I0019,共13页
复杂地形风电场流动具有强烈的非定常现象和多尺度特征,其准确模拟是风资源精细化评估的难点。为兼顾宏观中尺度大气环流和微观非定常流动细节,该文结合中尺度气象研究与预报(weather research and forecasting,WRF)模式和微尺度计算流... 复杂地形风电场流动具有强烈的非定常现象和多尺度特征,其准确模拟是风资源精细化评估的难点。为兼顾宏观中尺度大气环流和微观非定常流动细节,该文结合中尺度气象研究与预报(weather research and forecasting,WRF)模式和微尺度计算流体动力学(computational fluid dynamics,CFD)技术,构建一套WRF-CFD模式耦合的复杂地形风电场非定常仿真方法。以国际经典案例Askervein山和Bolund岛为验证对象,研究复杂地形流场中平均风速和湍流强度的分布特征,并简要分析复杂地形中风力机布置策略。结果表明,基于WRF-CFD模式的数值模拟结果与实验观测值有较好的一致性,且优于中尺度数值模拟结果,在选取的特征点位置,风速绝对误差均在2 m/s以内。结果可为风力机的设计、布局、载荷评估及风电场运行控制提供一定参考。 展开更多
关键词 风资源评估 风电场 复杂地形 中微尺度耦合 气象研究与预报模式 计算流体动力学
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基于ICEM CFD软件的三联水闸水力特性三维数值模拟分析
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作者 莫润安 梁炎 +5 位作者 陈晖 邓西婷 王秀南 马丹荣 刘范学 张祖发 《水科学与工程技术》 2026年第1期39-43,共5页
以广西壮族自治区玉林市三联水闸为研究对象,利用CAD图纸与BIM技术建立水闸三维几何模型,并采用ICEM进行网格划分与三维数值模拟计算,湍流模型采用标准k-ε数学模型,自由液面通过VOF法进行处理。结果表明:本次数值模拟的成果与标准公式... 以广西壮族自治区玉林市三联水闸为研究对象,利用CAD图纸与BIM技术建立水闸三维几何模型,并采用ICEM进行网格划分与三维数值模拟计算,湍流模型采用标准k-ε数学模型,自由液面通过VOF法进行处理。结果表明:本次数值模拟的成果与标准公式计算成果误差较小,说明一定程度上较为接近真实情况,从而验证了数值模拟的可靠性;水闸左岸翼墙突变直角段流态较差,导致水闸处断面流速和受力的不均匀性,影响了水闸的过流能力和受力;水闸左岸翼墙突变直角段交界处的流速存在一个较小的高速区,易导致翼墙处形成空化空蚀;左岸下游翼墙压力较大,易受到破坏,建议此处做好防护、监测工作及定期进行质量检查。 展开更多
关键词 水闸 水力特性 三维数值模拟 ICEM cfd k-ε湍流模型 VOF法
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基于CFD-DPM模型的挡煤板控尘机理研究
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作者 王振平 吴普豪 +1 位作者 王航 张铎 《煤矿安全》 北大核心 2026年第2期34-42,共9页
综采工作面是矿井粉尘污染最严重的区域之一,大采高工作面开采时落煤高度较大,采煤机割煤时产生的粉尘容易扩散至人行道,对矿工的身体健康造成严重威胁。为深入探究大采高工作面截割工序中挡煤板对粉尘的防控机理,以陕北张家峁煤矿1521... 综采工作面是矿井粉尘污染最严重的区域之一,大采高工作面开采时落煤高度较大,采煤机割煤时产生的粉尘容易扩散至人行道,对矿工的身体健康造成严重威胁。为深入探究大采高工作面截割工序中挡煤板对粉尘的防控机理,以陕北张家峁煤矿15211工作面为研究对象,建立了三维数值模型,采用计算流体动力学-离散相模型(CFD-DPM)的数值模拟方法,分析了不同挡煤板高度下综采工作面的风流特性、紊流分布和粉尘运移轨迹、分布范围及粒径分布变化。结果表明:随着挡煤板高度的增加,其对气流的分隔效应愈发显著,导致人行道区域气流流线减少,风速逐渐降低,而滚筒附近的风速则急剧上升,风速超过了2.5 m/s;当挡煤板高度达到1.6 m时,采煤机前方形成了长达30 m的高风速区域,增强的气流效应与物理阻隔相结合,有效改变了粉尘的运移路径与分布格局,显著抑制了粉尘的横向扩散,缩短了粉尘的暴露时间及运移距离;人行道内侧的粉尘污染区域显著减小,粉尘质量浓度降至50 mg/m^(3),大部分粉尘被有效地限制在了人行道外侧,对粒径大于40μm的粉尘拦截效果尤为明显;对比挡煤板为0.8 m与1.6 m时的粉尘质量浓度分布,随着挡煤板高度的增加,人行道呼吸带处的粉尘质量浓度显著降低,降尘率达50.2%;将数值模拟结果与现场实测数据进行比对,平均误差为6.9%,进一步验证了模拟的准确性和可靠性。 展开更多
关键词 挡煤板 综采工作面 cfd数值模拟 控尘机理 DPM模型
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Numerical aerodynamic analysis of bluff bodies at a high Reynolds number with three-dimensional CFD modeling 被引量:4
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作者 BAI YuGuang YANG Kai +4 位作者 SUN DongKe ZHANG YuGuang KENNEDY David WILLIAMS Fred GAO XiaoWei 《Science China(Physics,Mechanics & Astronomy)》 SCIE EI CAS 2013年第2期277-289,共13页
This paper focuses on numerical simulations of bluff body aerodynamics with three-dimensional CFD(computational fluid dynamics) modeling,where a computational scheme for fluid-structure interactions is implemented.The... This paper focuses on numerical simulations of bluff body aerodynamics with three-dimensional CFD(computational fluid dynamics) modeling,where a computational scheme for fluid-structure interactions is implemented.The choice of an appropriate turbulence model for the computational modeling of bluff body aerodynamics using both two-dimensional and three-dimensional CFD numerical simulations is also considered.An efficient mesh control method which employs the mesh deformation technique is proposed to achieve better simulation results.Several long-span deck sections are chosen as examples which were stationary and pitching at a high Reynolds number.With the proposed CFD method and turbulence models,the force coefficients and flutter derivatives thus obtained are compared with the experimental measurement results and computed values completely from commercial software.Finally,a discussion on the effects of oscillation amplitude on the flutter instability of a bluff body is carried out with extended numerical simulations.These numerical analysis results demonstrate that the proposed three-dimensional CFD method,with proper turbulence modeling,has good accuracy and significant benefits for aerodynamic analysis and computational FSI studies of bluff bodies. 展开更多
关键词 bluff body aerodynamic analysis fluid-structure interaction three-dimensional cfd modeling FLUTTER
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