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给出了一种利用测定圆管对流传热温度场求解确定成分的非共沸混合物的组分的方法。基于定压力条件下液体低雷诺数圆管层流充分发展段流体力学特性,利用数值方法求解变热参数对流传热模型温度场特性,采用反问题方法对对流传热控制方程的热参数进行非线性模拟和反算,通过反演计算热参数得到物质组分的定量值。对非线性热参数条件的对流传热控制方程和反问题L-M方法进行了误差分析,通过试验比较,测定了对流传热过程温度场的理论计算组分与预设的组分。结果表明,测定温度场推算的非共沸混合物组分与实际测定结果满足预设误差。 相似文献
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探究两相闭式热虹吸管的传热混沌,以及操作参数对其混沌性和传热性能的影响,建立混沌特征参数与传热性能间的联系。通过搭建实验台测量两相闭式热虹吸管稳定运行过程中不同工况下的管壁温度信号,基于非线性分析的混沌理论研究处理测量的温度脉动信号,绘制吸引子轨迹图,建立最大Lyapunov指数与传热特征参数的联系,揭示传热性能与混沌特性的关系。结果表明:两相闭式热虹吸管具有确定性混沌行为,操作参数对混沌性和传热性能具有显著影响,混沌性与传热性能呈正相关关系。 相似文献
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在脉动气流强化传热实验台上进行了层流(雷诺数RP为171)中不同振动参数(频率厂分别为15Hz、30Hz、45Hz、59Hz,振幅Pmax为45~286Pa)下脉动气流横掠高温共烧陶瓷发热管的传热实验研究.结果表明:层流中低频大振幅的脉动气流能显著强化圆柱体的传热过程,相对努塞尔数随着压力振幅的增大而增大,随着脉动频率的增大而减小,最大相对努塞尔数N“,可超过2.55;在Re=171时,脉动气流强化传热的经验公式为Nux=0.2684+0.5867pmax^0.388.3/f^0.3170,该经验公式的相关系数为R=0.9941,揭示了脉动气流强化圆柱体传热过程对振动参数的非线性依赖性. 相似文献
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本文对双室流化换热器的传热过程进行了分析,并对影响传热的因素-气固对流换热系数及颗粒循环量进行了实验研究。结果表明:强化传热应从增大颗粒循环量入手;本换热器可对传热实行调节,具有较好的操作性能。 相似文献
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间歇式热处理炉传热计算与分析 总被引:1,自引:0,他引:1
建立了台车式热处理炉炉膛传热数学模型和辐射换热器工作模型,分析了换热器的传热特性(空气预热温度、壁温、传热系数)随炉况的变化。结果表明,辐射换热器的传热特性随炉子的升温及保温过程变化而波动很大,因而对炉子的热工性能产生了影响。 相似文献
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为分析相变蓄热装置在充热和放热过程中的热性能,设计并搭建一套相变蓄热供热装置中试实验系统,研究主要运行参数对相变蓄热装置热性能的影响;在此基础上,结合项目案例,对相变蓄热供热系统经济性进行分析。结果表明:相变材料(Phase Change Material, PCM)凝固过程中的传热主要受相变介质内部导热控制;而在其熔化过程中自然对流对传热起重要控制作用;蓄热装置充热速率快于放热速率。提高传热流体流量有助于增强PCM中的热传递,缩短充/放热时间,但蓄热装置内PCM温度分布均匀性有所降低;为降低系统能耗,提高储放热效率,优先选用小流量进行充/放热。该相变蓄热供热项目的动态投资回收期为3.55年,具有良好的经济性。研究结果可对相变蓄热供热系统的设计及应用推广提供参考依据。 相似文献
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涡轮薄层污泥干化是涉及导热、对流传热与传质、高速旋流相耦合的复杂过程,掌握污泥的耦合干化机理与规律、确定干化设备核心参数,是该技术成功应用的关键。本文用机理分析方法构建涡轮薄层干化过程传热、传质的数学模型,基于该模型对污泥干化过程开展数值模拟,揭示涡轮薄层干化过程单一气相和气固两相流的速度、温度和含水率的分布规律,探究涡轮薄层干化的关键技术及参数。设计开发涡轮薄层污泥干化系统并开展实验研究。结果表明:干化机内部的桨叶阵列设计能够实现物料的顺利运输,桨叶末端是干化机内混合传热效果最佳位置,最优桨叶安装角度为45°,出口污泥含水率可降至20%。 相似文献
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Zhizhao Che Teck Neng Wong Nam-Trung Nguyen 《International Journal of Heat and Mass Transfer》2012,55(7-8):1947-1956
Plug flow can significantly enhance heat transfer in microchannels as compared to single phase flow. Using an analytical model of flow field, heat transfer in plug flow is investigated. The constant-surface-temperature boundary condition is considered. Three stages of the heat transfer in plugs are identified: (i) development of thermal boundary layer; (ii) advection of heated/fresh fluid in the plug; and (iii) thermally fully developed flow. Due to the transport of heated fluid and fresh fluid within the plug by the recirculating flow, oscillations of the Nusselt number at high Peclet numbers are observed and explained. The effects of the Peclet number and the plug length on the heat transfer process are evaluated. The results show that short plugs are preferable to long plugs since short plugs result in high Nusselt numbers and high heat transfer indices. 相似文献
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V. Talimi Y.S. Muzychka S. Kocabiyik 《International Journal of Heat and Mass Transfer》2012,55(23-24):6463-6472
Enhancement in heat transfer using two phase slug flow in microtubes and microchannels has encouraged researchers to focus on this topic as one of the potential methods for miniaturizing heat sinks and exchangers. Numerical simulation of two phase slug flow is time consuming, so some researchers conduct their numerical studies using the moving frame of reference technique for a unit cell consisting of only one slug, i.e. a single phase study, in order to accelerate the simulation process. Both single phase and two phase simulation methods have been performed in the present study and results have been compared. This shows to what extent the moving frame of reference assumption is valid in the case of two phase flow in hydrophilic microtubes when a thin liquid film exists around moving gas bubbles. The present comparison has been conducted for pressure drop and heat transfer for two thermal boundary conditions i.e. constant wall temperature and constant wall heat flux. It has been shown that the moving frame of reference method overpredicts pressure drop and heat transfer and possible reasons have been discussed. This also shows that in a slug flow with no film around bubbles more heat transfer could be achieved. 相似文献
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Yurong He Yubin Men Yunhua Zhao Huilin Lu Yulong Ding 《Applied Thermal Engineering》2009,29(10):1965-1972
A numerical study has been performed by using both single phase method and combined Euler and Lagrange method on the convective heat transfer of TiO2 nanofluids flowing through a straight tube under the laminar flow conditions. The effects of nanoparticles concentrations, Reynolds number, and various nanoparticle aggregates sizes are investigated on the flow and the convective heat transfer behaviour. The results show significant enhancement of heat transfer of nanofluids particularly in the entrance region. The numerical results are compared with the experimental data and reasonable good agreement is achieved. 相似文献
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Numerical simulations on performance enhancement of a cross-flow latent thermal energy storage heat exchanger
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基于列管式换热器具有传热面积大、结构紧凑、操作弹性大等优点,使其在相变储能领域具有广阔的应用前景。本文建立一种新型列管式相变蓄热器模型,在不考虑自然对流的情况下,利用Fluent软件对相变蓄热器进行二维储热过程的数值模拟。本文主要研究斯蒂芬数、雷诺数、列管排列方式、肋片数以及相变材料的导热系数对熔化过程的影响,并对熔化过程中固液分界面的移动规律进行了分析。模拟结果表明,内肋片强化换热效果明显,特别是对应用低导热系数相变材料[导热系数小于1 W/(m·K)]的列管式蓄热器,相对于无肋片结构,加入肋片(Nfn=2)可缩短熔化时间52.6%。 相似文献
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M. Lacroix 《Solar Energy》1993,50(4)
A theoretical model was developed to predict the transient behavior of a shell-and-tube storage unit with the phase change material (PCM) on the shell side and the heat transfer fluid (HTF) circulating inside the tubes. The multidimensional phase change problem is tackled with an enthalpy-based method coupled to the convective heat transfer from the HTF. The numerical predictions are validated with experimental data. A series of numerical experiments are then undertaken to assess the effects of various thermal and geometric parameters on the heat transfer process and on the behavior of the system. Results show that the shell radius, the mass flow rate, and the inlet temperature of the HTF must be chosen carefully in order to optimize the performance of the unit. 相似文献