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Thermal Protective Performance of Heat and Flame Resistant Fabrics in Different Radiant and Convective Heat Exposures 被引量:1
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作者 崔志英 刘华 张渭源 《Journal of Donghua University(English Edition)》 EI CAS 2008年第5期581-584,共4页
The thermal protective performance (TPP) is important for heat and flame resistant fabrics. In this study, fabrics which are made of flame resistant cotton, Nomex, polybenzimidazole (PBI), polysulfonamide (PSA),... The thermal protective performance (TPP) is important for heat and flame resistant fabrics. In this study, fabrics which are made of flame resistant cotton, Nomex, polybenzimidazole (PBI), polysulfonamide (PSA), kermel, and blend of kermei with rayon fiber are investigated on high intensity of different radiant and convective heat source. The mechanism of heat transfer in different situations is discussed. It is identified that exposed candition has an important effect on thermal protective performance. TPP rating increases with the increasing percentage of convective heat. 展开更多
关键词 TPP heat flux heat and flame resistant fabric radiant convective
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Performance comparison of heat exchangers using sextant/trisection helical baffles and segmental ones 被引量:5
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作者 Yaping Chen Hongling Tang +2 位作者 JiafengWu Huaduo Gu Shifan Yang 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2019年第12期2892-2899,共8页
The shell side flow fields of both sextant and trisection helical baffle heat exchangers are presented on meridian and multilayer hexagon slices.It verifies that the performance of sextant schemes is better than those... The shell side flow fields of both sextant and trisection helical baffle heat exchangers are presented on meridian and multilayer hexagon slices.It verifies that the performance of sextant schemes is better than those of the other kinds of helical baffle heat exchangers.The main mechanisms are due to the restricted leakage flow in the minimized gaps with increased baffle number and by one row of tubes dampen the leakage flow in the circumferential overlapped area of the adjacent helical baffles.The performance features were simulated on two different angled sextant helical heat exchangers and each compared with two trisection ones of either identical helical pitch or identical incline angle.The results verified that the performances of helical heat exchangers are mainly determined by the helical pitch rather than the baffle incline angle.The average values of comprehensive index hoΔpo-1/3 of the trisection helical schemes T-24.1°and T-29.7°are correspondingly 3.47%and 3.34%lower than those of the sextant ones X-20°and X-25°with identical helical pitches.The comparison results show that the average values of shell side h.t.c.hoand comprehensive index hoΔpo-1/3 of the optimal dual helix sextant scheme DX30°are respectively 7.22%and 23.56%higher than those of the segment scheme S100. 展开更多
关键词 heat transfer Computational fluid dynamics Convection HELICAL BAFFLE heat exchangeRS SEXTANT HELICAL baffles
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Calculation Method of Passive Residual Heat Removal Heat Exchanger and Numerical Simulation 被引量:1
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作者 Qiming Men Xuesheng Wang +1 位作者 Xiang Zhou Xiangyu Meng 《Journal of Power and Energy Engineering》 2014年第9期8-14,共7页
The tube inside and outside heat transfer mechanism of Passive Residual Heat Removal Heat Exchanger (PRHR HX) was analyzed. The calculation method of this special heat exchanger under natural convection condition in I... The tube inside and outside heat transfer mechanism of Passive Residual Heat Removal Heat Exchanger (PRHR HX) was analyzed. The calculation method of this special heat exchanger under natural convection condition in In-containment Refueling Water Storage Tank (IRWST) was carried out. The single-tube coupling model three-dimensional natural circulation in the IRWST was simulated numerically using Fluent. The heat transfer and flow characteristics of the fluid in IRWST were obtained. The comparison of the results between theoretical arithmetic and numerical simulation showed that the theoretical calculation method is suitable for the heat transfer calculation of PRHR HX. 展开更多
关键词 PASSIVE RESIDUAL heat Removal heat exchangeR heat Transfer Calculation Method Numerical Simulation Natural CONVECTION
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Duty Cycle of a Radiant Ceiling Heating System under Extremely Cold-Temperature Conditions:A Theoretical Assessment
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作者 Mohamed Lateb Hachimi Fellouah 《Journal of Energy and Power Engineering》 2019年第10期359-368,共10页
This work focuses on the estimation of a duty cycle of a radiant ceiling heating system with a panel surface temperature of 35℃and a heat flux of 65 W/m2 that corresponds to a thermal comfort for sedentary occupants.... This work focuses on the estimation of a duty cycle of a radiant ceiling heating system with a panel surface temperature of 35℃and a heat flux of 65 W/m2 that corresponds to a thermal comfort for sedentary occupants.The results obtained are based on the theoretical heat transfer equations that govern the radiant and natural convection heat exchange mechanisms,and experimental heat transfer coefficients available in the literature.The results of the examined radiant heating system with specific conditions showed that a duty cycle of 6.46 min alternated by 13.36 min in shutting-down position is required to assure an acceptable thermal comfort for the enclosure space occupants.In addition,the study showed that for extremely cold-temperature conditions the heating system requires a daily operating load of about 61.2%which clearly proves the efficiency of these radiant heating systems in terms of energy consumption. 展开更多
关键词 radiant CEILING PANELS natural CONVECTION transfer thermal COMFORT radiant heating systems DUTY cycle energy consumption.
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Study of the Heat Transfer of a Two-Tubular Exchanger with a Hemispherical End Buried
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作者 Dhahri Imen 《Energy and Power Engineering》 CAS 2022年第11期705-718,共14页
In this paper, a numerical study of a buried hemispherical double-pipe heat exchanger with soil by using geothermal energy is presented. Since the local air-wall exchange coefficient throughout the heat exchanger is u... In this paper, a numerical study of a buried hemispherical double-pipe heat exchanger with soil by using geothermal energy is presented. Since the local air-wall exchange coefficient throughout the heat exchanger is unknown, a study of mathematics based on the theory of Green’s functions in the unsteady state was developed. The complexity of the geometry has led us to develop a numerical study that allows us to obtain results that reflect the importance of heat exchange. The applications are numerous, especially in the storage of energy in the soil to optimize greenhouses according to the cycle of the seasons. 展开更多
关键词 Laminar Forced Convection Nusselt Number Horizontal heat exchanger Temperature Distribution
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Effects of the Form Factor and the Force of the Gravity on the Thermal Exchanges by Natural Convection in a Rectangular Cavity Filled with Nanofluid
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作者 L. Eljamali A. Wakif +2 位作者 Z. Boulahia M. Zaydan R. Sehaqui 《Engineering(科研)》 2019年第1期59-73,共15页
Effects of the form factor on natural convection heat transfer and fluid flow in a two-dimensional cavity filled with Al2O3-nanofluid has been analyzed numerically. A model was developed to explain the behavior of nan... Effects of the form factor on natural convection heat transfer and fluid flow in a two-dimensional cavity filled with Al2O3-nanofluid has been analyzed numerically. A model was developed to explain the behavior of nanofluids taking account of the volume fraction φ. The Navier-Stokes equations are solved numerically by alternating an implicit method (Method ADI) for various Rayleigh numbers varies as 103, 104 and 105. The nanofluid used is aluminum oxide with water Pr = 6.2;solid volume fraction φ is varied as 0%, 5% and 10%. Inclination angle Φ varies from 0° to 90° with a step the 15° and the form report varies as R = 0.25, 0.5, 1 and 4. The problem considered is a two-dimensional heat transfer enclosure. The vertical walls are differentially heated;the right is cold when the left is hot. The horizontal walls are assumed to be insulated. The nanofluid in the cavity is considered as incompressible, Newtonian and laminar flow. The nanoparticles are assumed to have a shape and a uniform size. However, it is supposed that the two fluid phases and nanoparticles are in a state of thermal equilibrium and they sink at the same speed. The thermophysical properties of nanofluids are assumed to be constant at the exception of the variation of density in the force of buoyancy, which is based on the approximation of Boussinesq values. 展开更多
关键词 NANOFLUID heat Transfer THERMAL exchangeS Natural Convection The FORCE of the GRAVITY Form Factor
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An Investigation into the Effect of Porous Medium on Performance of Heat Exchanger
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作者 Hadi Dehghan Peiman Aliparast 《World Journal of Mechanics》 2011年第3期78-82,共5页
In this paper, a detailed numerical investigation of two-dimensional laminar forced convection in a porous channel with inlet and outlet slot is presented. A uniform heat flux is applied on one wall of channel and ano... In this paper, a detailed numerical investigation of two-dimensional laminar forced convection in a porous channel with inlet and outlet slot is presented. A uniform heat flux is applied on one wall of channel and another wall is isolated. The flow in the porous medium is modeled using the Brinkman-Forchheimer-extended Darcy model in which the inertia and boundary effects are taken into consideration and thermal dispersion effects are not included in the energy equation. Parametric studies are conducted to evaluate the effects of particle diameter, Reynolds number on the heat transfer and friction factor. Nusselt number and friction factor are developed for efficient design of a porous heat exchanger based on the present configuration. In order to solve this problem Fluent software was used. 展开更多
关键词 Porous Medium FORCED CONVECTION Fluent heat exchangeR LAMINAR Flow
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工业竖窑内低速高温物料流动换热模型研究
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作者 朱蓉甲 鄂加强 叶恒棣 《中南大学学报(自然科学版)》 EI CAS CSCD 北大核心 2024年第10期3641-3650,共10页
从气固两相流动传热控制方程出发,应用数量级分析方法,推导适用于工业竖窑内低速流动的高温物料冷却过程的一维气固换热数值模型。基于FLUENT 2021R2仿真平台与MATLAB R2021平台,分别采用完整的气固流动传热模型与上述简化的一维换热模... 从气固两相流动传热控制方程出发,应用数量级分析方法,推导适用于工业竖窑内低速流动的高温物料冷却过程的一维气固换热数值模型。基于FLUENT 2021R2仿真平台与MATLAB R2021平台,分别采用完整的气固流动传热模型与上述简化的一维换热模型对某一工业石灰竖窑高温石灰冷却过程进行计算,对比不同冷却气流速度与换热高度下FLUENT仿真结果与一维气固换热模型计算结果。研究结果表明:气、固两相能量控制方程中扩散项的影响可以忽略;气流速度对气固相温度的影响远大于换热高度对气固相温度的影响;当气流速度较大时,这2种模型计算结果偏差主要出现在高温段,而当气流速度较小时,则主要出现在低温段;当冷却气流速度适中时,这2种模型计算得到的气相温度偏差均小于固相温度偏差,大部分区域气固相温度偏差小于20%。 展开更多
关键词 工业竖窑 低速流动 气固换热 数量级分析 对流项 扩散项
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涡旋压缩机浮动式静盘的性能优化研究
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作者 刘兴旺 李登辉 +3 位作者 刘晓明 李远航 蒋强强 陈荣道 《压缩机技术》 2024年第2期12-16,共5页
针对浮动式静盘涡旋压缩机静盘背部温度过高且集中于排气管处的问题,提出带散热结构的浮动式静盘背压机构,研究了新机构的质能交换,分析了热量交换过程,给出了各腔体传热的数学模型,并对新机构进行CFD模拟计算,得到了不同外界温度下的... 针对浮动式静盘涡旋压缩机静盘背部温度过高且集中于排气管处的问题,提出带散热结构的浮动式静盘背压机构,研究了新机构的质能交换,分析了热量交换过程,给出了各腔体传热的数学模型,并对新机构进行CFD模拟计算,得到了不同外界温度下的静盘背部温度分布情况。与原浮动式静盘背压机构对比分析可得,新机构有效地改善了静盘背部中心温度过高的问题,使静盘温度分布更加均匀,可以解决因温度过高而造成的变形、摩擦磨损以及泄漏等问题,提高了压缩机的可靠性。 展开更多
关键词 浮动式静盘 质能交换 数值模拟 对流传热
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热辐射特征参数对快堆锥形顶盖空间换热特性影响的研究 被引量:1
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作者 冯佳琪 陆道纲 +1 位作者 张钰浩 于宗玉 《核科学与工程》 CAS CSCD 北大核心 2024年第1期55-62,共8页
池式钠冷快堆的钠池内充满高温液态钠,其上方覆盖有氩气,高温液态钠主要通过辐射换热及对流换热的方式向快堆主容器上部结构及氩气空间传递热量,其换热特性及其影响因素十分复杂。辐射发射率及液态钠蒸发形成的气溶胶层对主容器上部结... 池式钠冷快堆的钠池内充满高温液态钠,其上方覆盖有氩气,高温液态钠主要通过辐射换热及对流换热的方式向快堆主容器上部结构及氩气空间传递热量,其换热特性及其影响因素十分复杂。辐射发射率及液态钠蒸发形成的气溶胶层对主容器上部结构的热工水力特性会造成一定影响。因此,为保证主容器上部结构在不同温度载荷下的安全性与稳定性,十分必要获取不同辐射发射率及不同气溶胶层分布下的温度分布。本研究建立大型池式钠冷快堆主容器上部锥形顶盖空间(以下简称“锥顶盖”)数值计算模型,开展数值模拟计算,得到不同发射率及气溶胶层厚度影响下锥顶盖的温度场。研究结果表明,发射率越高,锥顶盖斜肩及氩气空间温度越高;当气溶胶层存在于靠近钠液面的高度范围时(0~0.2 m),增加其厚度可使氩气空间局部温度升高,但对锥顶盖斜肩温度影响有限。发射率增高53%,则辐射换热量增加31.47%,格拉晓夫数(Gr)减少19.29%,辐射换热效果增强,自然对流效果减弱;气溶胶层高度由0增加到0~0.1 m时,对辐射换热量的吸收增加22.68%,格拉晓夫数(Gr)减少19.29%,气溶胶层高度由0~0.1 m增加到0~0.2 m时,透过气溶胶层的辐射换热量减少了0.04%,格拉晓夫数(Gr)增加了0.9%,辐射换热效果减弱,自然对流效果加强。 展开更多
关键词 快堆锥形顶盖空间 辐射换热 自然对流 发射率 吸收系数
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不同供暖末端办公建筑室内热环境和人体热舒适调研
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作者 赵胜凯 杨柳 +1 位作者 高斯如 翟永超 《暖通空调》 2024年第7期98-105,共8页
为明确寒冷气候区办公建筑辐射供暖和对流供暖模式下的室内热环境参数是否能满足人体热舒适需求,本研究选取西安市不同供暖模式的办公建筑为调研对象,同时进行了室内物理环境测试和人体热舒适主观问卷调查,调研期间共获得1 120份有效问... 为明确寒冷气候区办公建筑辐射供暖和对流供暖模式下的室内热环境参数是否能满足人体热舒适需求,本研究选取西安市不同供暖模式的办公建筑为调研对象,同时进行了室内物理环境测试和人体热舒适主观问卷调查,调研期间共获得1 120份有效问卷。结果显示:对流供暖模式下室内空气温度和竖直温差显著高于辐射供暖,且室内存在过热现象;辐射和对流供暖的中性温度分别为17.4℃和20.4℃,较高的室内空气温度形成了较高的中性温度和可接受温度上限。 展开更多
关键词 辐射供暖 对流供暖 办公建筑 室内热环境 热舒适 中性温度 可接受温度 现场调研
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管翅式相变储热系统结构/热源条件强化传热数值模拟研究
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作者 刘云龙 龙威 +1 位作者 别玉 林婷婷 《太阳能学报》 EI CAS CSCD 北大核心 2024年第9期655-661,共7页
基于焓法的凝固/熔化模型,在考虑自然对流的情况下,建立管壳式相变换热器的熔化模型,并研究管翅片布局和热边界条件对相变材料瞬态熔化行为的影响机理。针对均匀的管翅片布局和恒定壁温热边界条件,设计一种具有方形波动热源的偏心结构,... 基于焓法的凝固/熔化模型,在考虑自然对流的情况下,建立管壳式相变换热器的熔化模型,并研究管翅片布局和热边界条件对相变材料瞬态熔化行为的影响机理。针对均匀的管翅片布局和恒定壁温热边界条件,设计一种具有方形波动热源的偏心结构,并对两者之间的强化传热规律进行比较和分析。结果表明,偏心布局可使相同传热面积中热传递盲区的熔化得到改善,而方形波动热源可增强前熔化阶段中央区域的自然对流;能量存储参数对比表明,相比原始结构,偏心布局结构或方形波动热源的熔化时间分别缩短12.5%和6.25%,而同时优化热源和结构的熔化时间缩短31.25%。方形波动热源和偏心结构能显著提高换热器的熔化速率。 展开更多
关键词 相变材料 传热性能 管壳式 传热盲区 自然对流 数值模拟 强化传热
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风速与风向对人体热交换影响的CFD仿真模拟 被引量:1
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作者 张珊珊 杨杰 《安全与环境工程》 CAS CSCD 北大核心 2024年第2期129-136,共8页
为了提升灾害环境中人体热损伤评估精度并保障应急救援人员的生命安全,首先将暖体假人进行三维激光扫描得到数值假人,并按照人体生理构造将其划分为20个区块,通过ICEM软件建立气候室,设置0°~180°的风向;然后通过FLUENT软件计... 为了提升灾害环境中人体热损伤评估精度并保障应急救援人员的生命安全,首先将暖体假人进行三维激光扫描得到数值假人,并按照人体生理构造将其划分为20个区块,通过ICEM软件建立气候室,设置0°~180°的风向;然后通过FLUENT软件计算得到0.2~5.0 m/s风速时的人体显热换热量和辐射换热量,在此基础上求得对流换热量;最后将模拟结果与文献中数据进行对比验证,并分析不同风速与风向对人体热交换的影响。结果表明:提出的计算流体动力学(CFD)仿真模拟方法可有效模拟人体不同部位的换热量;风速的增加会促进人体与环境之间的热交换,当风速从0.2 m/s增加到5.0 m/s时,人体整体对流换热量从56 W/m^(2)增加到360 W/m^(2);人体表面局部部位之间对流换热量有明显的差异,其中四肢部位与环境之间的热交换受风速影响更为明显;风向对人体整体对流换热几乎没有影响,但躯干部位对流换热量受风向的影响较大;在非对称风向(45°、90°、135°)下,人体对流换热量呈现非对称式分布。本研究可为人员安全评估、极端环境下人体热反应建模、防护装备研发等提供基础数据。 展开更多
关键词 个体防护 辐射换热量 对流换热量 风速 风向 数值假人 计算流体动力学(CFD)
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固体蓄热电锅炉对流管束优化设计研究
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作者 侯子维 张忠涛 +1 位作者 王家璇 师涌江 《河北建筑工程学院学报》 CAS 2024年第1期146-154,共9页
针对现有固体蓄热电锅炉换热效率较低、锅炉房占地面积大的不足,主要对新型固体蓄热电锅炉的对流管束部分进行优化,将对流管束蓄热体进行系统分析。考虑资金的时间价值,从技术经济动态角度进行分析,将系统的费用通过费用现值法折现至初... 针对现有固体蓄热电锅炉换热效率较低、锅炉房占地面积大的不足,主要对新型固体蓄热电锅炉的对流管束部分进行优化,将对流管束蓄热体进行系统分析。考虑资金的时间价值,从技术经济动态角度进行分析,将系统的费用通过费用现值法折现至初期,以系统寿命期内的成本折现值最小为目标,以对流管束物理结构与热量守恒为约束构建数学模型,对该模型提出求解方法以及算法的程序说明。最终通过优化固体蓄热电锅炉的对流管束直径、管间距和长度这三个自变量,在满足采暖热负荷的情况下,使寿命周期内的成本折现值达到最小。 展开更多
关键词 固体蓄热电锅炉 换热效率 优化设计 对流管束
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叉排微通道换热器的换热性能
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作者 魏骏豪 孔令伟 +1 位作者 方刚毅 邢菲 《厦门大学学报(自然科学版)》 CAS CSCD 北大核心 2024年第3期541-549,共9页
[目的]探究叉排微通道换热器在船用燃气轮机间冷过程中的实验换热性能及其影响因素.[方法]针对增材制造加工的叉排微通道换热器,在低流动工况条件下进行对流换热实验,从结构和流动因素研究叉排微通道换热器的换热性能.[结果]通道宽度减... [目的]探究叉排微通道换热器在船用燃气轮机间冷过程中的实验换热性能及其影响因素.[方法]针对增材制造加工的叉排微通道换热器,在低流动工况条件下进行对流换热实验,从结构和流动因素研究叉排微通道换热器的换热性能.[结果]通道宽度减小0.50 mm使叉排换热器换热性能增强106.9%~61.9%;通道数增加1.6倍导致同流量下换热性能平均降低21.9%~50.8%,而同流速下换热性能平均降低11.6%;进口流量增加6.3倍,换热器换热性能提升44.0%;但换热性能受热侧空气进口温度的影响较小,相邻工况条件计算值变化最大仅为5.4%.[结论]工艺条件允许下减小通道尺寸可提升叉排微通道换热器性能,而增加通道数量则会带来负面影响;冷侧水进口流量增大能提升叉排微通道换热器换热量,从而增强换热性能;热侧空气进口温度的影响则较为复杂. 展开更多
关键词 换热单元 叉排微通道换热器 微通道对流换热实验 增材制造
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12 kV/4000 A环保气体绝缘开关设备散热结构设计
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作者 梁利娟 于盟 许通 《电工电气》 2024年第6期54-58,73,共6页
由于环保气体绝缘开关设备是完全密封的,其散热工况极差,针对12 kV/4 000 A环保气体绝缘开关设备研发中的热传递与散热问题,开发了一种组装式断路器。对断路器的内部结构设计进行了优化,增大有效的散热面积,同时优化风道与风机布局来进... 由于环保气体绝缘开关设备是完全密封的,其散热工况极差,针对12 kV/4 000 A环保气体绝缘开关设备研发中的热传递与散热问题,开发了一种组装式断路器。对断路器的内部结构设计进行了优化,增大有效的散热面积,同时优化风道与风机布局来进一步扩大散热面积,强化外部热对流交换。试验结果表明,温升值完全控制在标准要求的范围内,开发的12 kV/4 000 A环保气体绝缘开关设备满足温升标准,确保了开关柜运行的可靠性。 展开更多
关键词 环保气体绝缘开关设备 热传递 散热面积 热对流交换 温升控制
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Augmenting the Heat Sink for Better Heat Dissipation
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作者 Mohammed H. S. Al Ashry 《Circuits and Systems》 2015年第2期21-29,共9页
Heat sinks were invented to absorb heat from an electronic circuit conduct, and then to dissipate or radiate this heat to the surrounding supposedly, ventilated space, at a rate equal to or faster than that of its bui... Heat sinks were invented to absorb heat from an electronic circuit conduct, and then to dissipate or radiate this heat to the surrounding supposedly, ventilated space, at a rate equal to or faster than that of its buildup. Ventilation was not initially recognized as an essential factor to thermal dispersion. However, as electronic circuit-boards continued to heat up, circuit failure became a problem, forcing the inclusion of miniaturized high speed fans. Later, heat sinks with fins and quiet fans were incorporated in most manufactured circuits. Now heat sinks come in the form of a fan with fans made to function as fins to disperse heat. Heat sinks absorb and radiate excess heat from circuit-boards in order to prolong the circuit’s life span. The higher the thermal conductivity of the material used the more efficient and effective the heat sink is. This paper is an attempt to theoretically design a heat sink with a temperature gradient lower than that of the circuit board’s excess heat. 展开更多
关键词 convective heat Transfer: heat Absorbed by the Natural AIR Flow Surrounding Hot Objects FORCED convective heat Transfer: Absorption of heat Using FORCED AIR Flow Conductivity: Is the Ability of a System to exchange or TRANSFER Temperature within a Body or MATERIAL through the Movement of Electrons MATERIAL That Does Not Conduct heat Is Considered a Nonconductor
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壳管式相变蓄热换热器换热特性的模拟研究 被引量:1
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作者 闫全英 郭媛 张静 《暖通空调》 2023年第11期144-149,共6页
设计了一种以石蜡为相变材料的圆柱型壳管式相变蓄热换热器,以三维单元相变储热模型为研究对象进行了换热数值模拟。分析了相变材料的液相比、温度场、平均温度及换热介质出口温度的变化规律,研究了该壳管式相变蓄热换热器在蓄、放热阶... 设计了一种以石蜡为相变材料的圆柱型壳管式相变蓄热换热器,以三维单元相变储热模型为研究对象进行了换热数值模拟。分析了相变材料的液相比、温度场、平均温度及换热介质出口温度的变化规律,研究了该壳管式相变蓄热换热器在蓄、放热阶段的换热特性。结果表明:液相石蜡的自然对流会增强相变材料与换热介质之间的换热,并加快石蜡的熔化和凝固速率;蓄热阶段液相比达到18.6%后,自然对流换热的影响逐渐明显;放热阶段初期,液相比在80 s内下降了63%,固态石蜡层完全包裹传热管束前的自然对流换热最强,之后逐渐减弱。 展开更多
关键词 壳管式相变蓄热换热器 换热特性 石蜡 相变材料 液相比 蓄热 放热 自然对流换热
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双螺旋盘管内膨胀石墨对相变材料的传热强化机制与蓄放热性能
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作者 郭艳芹 曾镇 +3 位作者 张弘光 凌子夜 张正国 方晓明 《储能科学与技术》 CAS CSCD 北大核心 2023年第12期3678-3689,共12页
本工作提出了一种双螺旋盘管与膨胀石墨强化传热的相变蓄热器结构,通过建立双螺旋管相变蓄热器模型,模拟了双螺旋管的螺距、材料热物性对蓄放热性能的影响规律。探讨了限制空间下相变材料自然对流与材料导热增强在传热强化过程中的控制... 本工作提出了一种双螺旋盘管与膨胀石墨强化传热的相变蓄热器结构,通过建立双螺旋管相变蓄热器模型,模拟了双螺旋管的螺距、材料热物性对蓄放热性能的影响规律。探讨了限制空间下相变材料自然对流与材料导热增强在传热强化过程中的控制作用。结果表明,在加工螺距限制条件下,减小螺距及增加螺旋数可以提升蓄热器放热性能。膨胀石墨可以提升相变材料热导率,同时会导致材料黏度增大,因此添加膨胀石墨能增强蓄热器的导热换热,但抑制自然对流换热。通过对比分析发现,在限制空间下材料的导热增强带来的传热强化程度能够弥补由于材料自然对流不足导致的传热损失。因此,本工作揭示了相变蓄热器传热强化的控制步骤在于材料热导率强化。基于实验和仿真结合的方式,本工作设计了一款用于加热生活热水的蓄热器结构,验证了所设计的蓄热器在宽进口温度、进口流量等操作工况下具有优异的放热性能。该蓄热器与电加热器相结合,能够在电热功率小于2200 W的条件下实现热水加热功率超3500 W,突破了家用电热设备的功率限制。 展开更多
关键词 双螺旋管 相变蓄热器 数值模拟 导热增强 自然对流
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混合纳米流体的对流换热及热经济性研究进展 被引量:2
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作者 孙杰 范影 +2 位作者 米俊锋 建伟伟 焦岩 《应用化工》 CAS CSCD 北大核心 2023年第9期2655-2659,共5页
综述了混合纳米流体在换热器中的对流换热及热经济性的研究现状。介绍了对流换热性能参数(总传热系数、对流换热系数、Nu数)的影响因素及变化机理。对混合纳米流体在换热器应用中的热经济性(热效率、熵产、火用损失、第二定律效率)进行... 综述了混合纳米流体在换热器中的对流换热及热经济性的研究现状。介绍了对流换热性能参数(总传热系数、对流换热系数、Nu数)的影响因素及变化机理。对混合纳米流体在换热器应用中的热经济性(热效率、熵产、火用损失、第二定律效率)进行了分析。 展开更多
关键词 混合纳米流体 换热器 对流换热 热经济性
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