玻璃包覆纯铜丝快速冷却温度场数值模拟

建立了玻璃包覆纯铜丝快速冷却过程温度场的有限元计算模型,模拟得出了冷却过程丝线横断面的温度分布图及节点温度随时间的变化关系。研究了冷却水温度、水流速度对玻璃包覆纯铜丝冷却效果的影响。结果表明:快冷时玻璃层内的温差最大可达45 K/m,铜芯内温差最大为0.12 K/m; 随着冷却水流速增大,冷却效果增强,流速达到0.5 m/s时冷却能力饱和; 冷却水温在283～303 K范围内变化时,冷却效果基本不变。     

高功率微波管收集极的散热分析

利用欧拉两相流模型和沸腾换热模型计算了高功率微波管收集极的散热问题。在给出电子束能量沉积规律的基础上,得到了热源项在收集极及冷却水中的分布形式。利用CFD软件计算了脉宽为45 ns、重频为50 Hz、平均功率为27 kW电子束作用下的收集极温度分布,重点研究了冷却水流速对散热效果的影响。研究结果表明,冷却水流速为1.5 m/s时,内壁面稳态峰值温度超过了收集极材料的熔点,会导致一定时间后收集极损坏;散热峰值处对流换热大约占总换热量的71.7%,激冷换热大约占28.1%,相变换热占0.2%。冷却水流速小于5 m/s时,收集极最高温度随流速增加快速下降;5~10 m/s时,温度下降缓慢;超过10 m/s后,温度下降速度增大。针对该电子束条件,收集极安全工作要求冷却水流速不得低于5 m/s。     

液态锂实验装置中水冷效率模拟

应用商业软件CFX 计算了液态锂流速、热通量、冷却水的速度和温度对自由流动液态锂在热负荷作用下液态锂温度和水冷效率的影响。结果表明：液态锂温度随液态锂流速的增大而降低。热通量小于2MW·m^-2 时,水冷能够满足对液态锂温度控制的要求;在更大热通量作用下,水冷却显现出冷却能力不足。增大冷却水流速是降低液态锂温度、提高冷却效率的有效途径;冷却水温度对液态锂温度和冷却效率的影响较小。     

(La0.2Nd0.8)0.67Pb0.33MnO3的Preisach分析

测量了居里点为TC=220K的钙钛矿(La0.2Nd0.8)0.67Pb0.33MnO3 (LNPMO)在外场为ha=3978.87A/m ，2K相似文献   

应力作用下EuTiO3铁电薄膜电热效应的唯象理论研究

基于Laudau-Devonshire的热动力学模型, 计算了EuTiO₃铁电薄膜材料的电热效应. 结果显示在外加应力的调控下, 电极化、电热系数以及绝热温差都会随之变化. 外加垂直于表面的张应力加大, 薄膜的相变温度升高, 绝热温差增加, 最大绝热温差所对应的工作温度向高温区移动. 对于二维平面失配应变u_m =-0.005的薄膜, 当外加张应力σ₃ = 5 GPa时, 其最大电热系数为1.75×10^-3 C/m²·K, 电场变化200 MV/m 时室温下绝热温差ΔT 的最大值可达到14 K 以上, 绝热温差ΔT ≥13 K 的工作温区超过120 K, 表明可以通过调控外部应力来获取室温时较大的绝热温差. 此结果预示着铁电EuTiO₃ 薄膜在室温固态制冷方面可能具有较好的应用前景.     

冷却倾斜板熔体处理过程边界层分布及流动传热的理论研究

针对倾斜板熔体处理晶粒细化与半固态成形原理,研究了倾斜板熔体处理过程边界层分布,建立了熔体传热和冷却速率的计算模型.计算结果表明,随着斜板倾角和熔体初始流动速度的增大,熔体在倾斜板上从层流向紊流的转变时间减少;温度边界层厚度随着熔体初始流动速度的增加而减小,斜板倾角对温度边界层厚度的影响较小;温度边界层厚度和速度边界层厚度都随熔体流动距离的增加而增大,在层流区,温度边界层厚度远大于速度边界层厚度,而在紊流区,温度边界层厚度与速度边界层厚度重合;倾斜板上熔体冷却速率与熔体厚度成反比,初始流速小于1m/s时,熔体的冷却速率沿着倾斜板长度方向逐渐增大,初始流速为1m/s时,熔体的冷却速率沿倾斜板长度方向基本不变,当初始流速大于1m/s时,熔体冷却速率沿倾斜板长度方向逐渐减小;倾斜板上熔体冷却速率在100—1000 K/s之间,属于亚快速凝固范畴.     

环境风下光伏-温差发电系统耦合特性分析

综合考虑环境风和冷却流体的耦合作用,建立了采用纳米流体冷却的光伏(PV)-温差发电(TE)系统的性能分析数学模型,探讨了聚光比、风速、冷却流体流速、负载和热电材料品质因数等对其性能的影响。结果表明:采用纳米流体为冷却介质提高了系统的总效率;系统最佳负载值不同于温差发电模块效率最大时的负载;风速对系统最大效率的影响随着热电材料品质因数的变化而变化。     

高功率微波管收集极的散热分析北大核心CSCD

利用欧拉两相流模型和沸腾换热模型计算了高功率微波管收集极的散热问题。在给出电子束能量沉积规律的基础上,得到了热源项在收集极及冷却水中的分布形式。利用CFD软件计算了脉宽为45ns、重频为5OHz、平均功率为27kW电子束作用下的收集极温度分布,重点研究了冷却水流速对散热效果的影响。研究结果表明,冷却水流速为1．5m／s时,内壁面稳态峰值温度超过了收集极材料的熔点,会导致一定时间后收集极损坏;散热峰值处对流换热大约占总换热量的71．7％,激冷换热大约占28．1％,相变换热占0．2％。冷却水流速小于5m／s时,收集极最高温度随流速增加快速下降;5～10m／s时,温度下降缓慢;超过10m／s后,温度下降速度增大。针对该电子束条件,收集极安全工作要求冷却水流速不得低于5m／s。     

La0.67Pb0.33MnO3的Preisach分析

测量了居里点TC=360K的钙钛矿La0.67Pb0.33MnO3在2K关键词： Preisach模型 磁滞回线 磁化强度 磁化率     

ITER �Թ�ŵ�缫����ȴ����

对清洗放电时ITER辉光放电电极采用水冷和气冷条件下的电极冷却进行了计算。当辉光放电清洗功率为9000W,冷却水的流速为4~6m.s-1,入口温度为室温25°C时,电极的温升不会超100°C。当冷却媒介为氦(He),速度为300m.s-1,入口温度为室温25°C时,最高温度不会超过200°C。计算表明,当仅仅考虑因辉光放电电功率所导致电极发热时,水冷可以满足电极辉光放电时的冷却要求。     

Crackless linear through-wafer etching of Pyrex glass using <Emphasis Type="Italic">liquid-assisted</Emphasis> CO<Subscript>2</Subscript> laser processing

Pyrex glass etching is an important technology for the microfluid application to lab-on-a-chip devices, but suffers from very low etching rate and mask-requiring process in conventional HF/BOE wet or plasma dry etching as well as thermal induced crack surface by CO₂ laser processing. In this paper, we applied the liquid-assisted laser processing (LALP) method for linear through-wafer deep etching of Pyrex glass without mask materials to obtain a crackless surface at very fast etching rates up to 25 μm/s for a 20 mm long trench. The effect of laser scanning rate and water depth on the etching of the 500 μm thick Pyrex glass immersed in liquid water was investigated. The smooth surface without cracks can be achieved together with the much reduced height of bulge via an appropriate parameter control. A mechanism of thermal stress reduction in water and shear-force-enhanced debris removal is discussed. The quality improvement of glass etching using LALP is due to the cooling effect of the water to reduce the temperature gradient for a crackless surface and natural convection during etching to carry away the debris for diminishing bulge formation. An erratum to this article can be found at     

R410A和R22在水平内螺纹管内冷凝性能的实验研究

实验研究了环保替代制冷工质R410A和R22在冷凝温度40℃时在内螺纹强化管(外径为9.52mm)内的冷凝换热特性,对二者的冷凝换热性能进行了对比,并研究了测试管外冷却水流量对换热系数的影响。结果表明:在管外冷却水流量相同时,R22的总换热系数K普遍比R410a小,而管内传热系数hr比R410A大。R22与R410A的总传热系数K均随管外冷却水流量的增加而增加,当制冷剂流量Gm大于300kg.s-1.m-2时,管外冷却水流量对总传热系数K的影响变小。     

环形磁场金属等离子体源冷却流场的数值模拟与优化

环形磁场金属等离子体源作为一种全新的等离子体源结构,可用于产生高度离化、无大颗粒、高密度的离子束流,但传统流道结构不能保证其高效、均匀散热,大功率工作时可能引起密封胶圈的烧蚀失效,需对其冷却流场进行优化设计.利用Solidworks Flow Simulation软件对等离子体源冷却流道进行模拟,分析出入水孔分布角度、孔数、孔径以及入水孔高度对冷却效果的影响规律,并对流道结构参数进行优化.结果表明,增大水孔的周向分布范围,有利于提高散热的均匀性;入水孔设置在结构上层有利于减少冷却水的温度分层现象,使铜套和密封胶圈都处于较好的冷却状态;适当减小孔径有利于增大冷却水射流速度,增大湍流程度强化传热,提高换热效率.优化后的流场结构可以提高冷却水的利用率,在相同流量条件下获得更好的冷却效果,改善等离子体源的放电稳定性,为环形磁场金属等离子体源的冷却结构设计提供理论依据.     

Size effect in the melting and freezing behaviors of Al/Ti core-shell nanoparticles using molecular dynamics simulations

The thermal stability of Ti@Al core/shell nanoparticles with different sizes and components during continuous heating and cooling processes is examined by a molecular dynamics simulation with embedded atom method. The thermodynamic properties and structure evolution during continuous heating and cooling processes are investigated through the characterization of the potential energy, specific heat distribution, and radial distribution function(RDF). Our study shows that, for fixed Ti core size, the melting temperature decreases with Al shell thickness, while the crystallizing temperature and glass formation temperature increase with Al shell thickness. Diverse melting mechanisms have been discovered for different Ti core sized with fixed Al shell thickness nanoparticles. The melting temperature increases with the Ti core radius. The trend agrees well with the theoretical phase diagram of bimetallic nanoparticles. In addition, the glass phase formation of Al–Ti nanoparticles for the fast cooling rate of 12 K/ps, and the crystal phase formation for the low cooling rate of 0.15 K/ps. The icosahedron structure is formed in the frozen 4366 Al–Ti atoms for the low cooling rate.     

Char characteristics and particulate matter formation during Chinese bituminous coal combustion

The characteristics of char particles and their effects on the emission of particulate matter (PM) from the combustion of a Chinese bituminous coal were studied in a laboratory-scale drop tube furnace. The raw coal was pulverized and divided into three sizes, <63, 63–100, and 100–200 μm. These coal samples were subjected to pyrolysis in N₂ and combusted in 20 and 50% O₂ at 1373, 1523, and 1673 K, respectively. Char samples were obtained by glass fiber filters with a pore size of 0.3 μm, and combustion-derived PM was size-segregated by a low pressure impactor (LPI) into different sizes ranging from 10.0 to 0.3 μm. The characteristics of char particles, including particle size distribution, surface area, pore size distribution, swelling behavior and morphology property, were studied. The results show that, coal particle size and pyrolysis temperature have significant influence on the char characteristics. The swelling ratios of char samples increase with temperature increasing from 1373 to 1523 K, then decrease when the temperature further increases to 1623 K. At the same temperature, the swelling ratios of the three size fractions are markedly different. The finer the particle size, the higher the swelling ratio. The decrease of swelling ratio at high temperature is mainly attributed to the high heating rate, but char fragmentation at high temperature may also account for the decrease of swelling ratio. The supermicron particles (1–10 μm) are primarily spherical, and most of them have smooth surfaces. Decreasing coal particle size and increasing the oxygen concentration lead to more supermicron-sized PM formation. The influence of combustion temperature on supermicron-sized PM emission greatly depends on the oxygen concentration.     

供水温度对CO2空气源热泵系统性能的影响

为探究热泵供水温度对CO2空气源热泵系统性能的影响,保持室外环境温度15.5℃不变,调节热泵供水温度,测试冷却水流量、气冷器出水温度、压缩机排气温度、气冷器CO2进出口温差、压缩机排气压力、压缩机耗功量、系统制热量、气冷器热交换完善度、系统COP的变化情况。结果表明:供水温度由45℃升至85℃,气冷器出水温度、压缩机排气温度、气冷器CO2进出口温差、压缩机排气压力随之增加,冷却水流量随之减小。系统制热量增加了7.3%、气冷器热交换完善度下降了20.0%、系统COP下降了35%、压缩机功耗增加了65.1%。     

Microflow reactor synthesis of palladium nanoparticles stabilized with poly(benzyl ether) dendron ligands

A simple glass capillary microflow reactor system has been applied for the synthesis of palladium nanoparticles by thermal decomposition of palladium acetate (Pd(OAc)₂) in diphenyl ether in the presence of poly(benzyl ether) dendron ligands (PBED Gn-NH₂, n = 1–3) as a stabilizer. Effect of hydrodynamic parameters (capillary diameter, linear flow rate, volume flow rate, and reaction temperature) and concentrations (precursor and stabilizer) on the particle size was investigated. The particle size can be controlled by varying linear flow rate and temperature as well as ligand/precursor concentration ratio. Volume flow rate does not affect the particle size when the linear flow rate is held constant for different capillary diameters (150–320 μm). Unlike batch systems, in this microreactor system, smaller particles are produced at low ligand concentrations when the molar ratio of the ligand to metal precursor ranged from 1 to 5. As another characteristic of the microreactor synthesis, the concentration of the Pd precursor can be increased (up to 27 mM) with maintaining a constant particle size (3.1 ± 0.2 nm) and a good monodispersity, while in the batch system a significant increase and broadening in the particle size are observed with increasing precursor concentration.