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《机械工程与自动化》2020,(5)
首先,经相关理论计算确定了散热器的肋间距为5 mm,肋高为15 mm;然后,利用自建实验台对散热器在3种不同功率、不同风速下的散热过程进行对比实验分析,说明了散热器在高功率情况下散热状况受气体流速影响较大;最后运用Workbench仿真软件对不同肋厚的散热器结构进行热分析,得到了在风冷对流工况下,肋厚为1.5 mm,风速为1.0 m/s时散热器的散热性能最佳,且满足了散热设计要求。 相似文献
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CPU散热器结构设计与热分析 总被引:5,自引:0,他引:5
CPU散热器是将CPU核心热量迅速导出的关键,已成为获得新一代电子芯片的主要问题之一。采用数值模拟方法对放射状太阳花CPU散热器进行三维流场及温度场分析,探讨放射状散热器在不同的肋片形状、肋片数N和肋片厚度等各种不同的参数作用下,对于整体散热器散热和流动性能的变化与影响,同时分析了太阳花散热器自然对流和瞬时动态特性。 相似文献
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空调散热器的散热性能是影响空调工作性能的重要因素,如何合理设计散热器结构以提高空调散热性能是目前亟待解决的问题。现利用ANSYS软件建立了散热器的有限元模型,并对其进行了热学性能分析,研究了散热性能与散热器结构的关系,然后对结果进行了对比分析,得到了散热器温度分布云图、相同结构不同鳍片数对散热器散热性能影响的关系曲线图以及不同结构相同鳍片数对散热器散热性能影响的关系曲线图,为空调散热器的优化设计提供了重要的依据。 相似文献
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通过在液冷式CPU散热器蛇形流道内填充不同粒径的不锈钢珠,使液冷式CPU散热器流道形成类似多孔介质的复杂流道以提高其散热性能。通过对改进前后液冷式CPU散热器的试验研究,分析了各因素对液冷式CPU散热器的传热和流阻性能的影响规律。结果表明:在本试验范围内,相同Re和Pr下,改进后散热器的对流换热系数为改进前的1.2~4.8倍,阻力系数f是改进前的1.4~4倍;散热器填充Φ4mm开孔不锈钢珠的强化传热效果最佳,芯片表面温度较填充前降低了33,°对流换热系数增大4.8倍,而流动阻力仅增加了1.4倍。 相似文献
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为了提高水冷散热器的散热能力、控制其温度均匀性,研究四种不同水冷散热器的进出水方式对芯片散热效果的影响。A型散热器采用传统的散热器形式,进出口位于散热器两端。B-D型散热器采用中间垂直射流,在散热器四角分别设置1个、2个、4个出水口。通过数值模拟分析不同冷却水流量下散热器的换热效果。数值模拟结果经过试验验证。通过Nu数、速度分布、压力损失、综合效应四个方面对散热器的换热性能进行分析。结果显示四出口散热器的Nu数低于单出口散热器,但流动阻力小,散热器综合系数较高,不会造成局部热点。中间射流四出口散热器具有较好的换热和流动效果。 相似文献
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通过数值模拟方法对百叶窗翅片散热器流道中流体的流动和传热性能进行研究,将数值模拟结果与文献实验关联式计算结果进行对比,验证了数值模拟方法的正确性。将百叶窗翅片散热器的翅片间距与百叶窗间距两者关联起来,分析了其比值Fp/Lp和百叶窗倾角对于百叶窗翅片流道传热和压降性能的影响。而后分析了百叶窗翅片结构参数对于百叶窗流道间流体流动效率的影响。研究表明,百叶窗翅片的传热系数和压降随着Re数的增大而增大,随着百叶窗翅片间距与百叶窗间距比值Fp/Lp的增大而减小,随着百叶窗倾角的增大而增大。流动效率随着Re数的增大而增大,随着百叶窗翅片间距与百叶窗间距比值的增大而减小,随着百叶窗倾角的增大而增大。 相似文献
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通过改变肋片的焊接尺寸以及焊接形状建立肋片传热模型,采用CFD(Computational Fluid Dynamic)模拟的方法,将模拟结果与传统铸造肋片的传热情况进行对比,研究不同焊接方式以及焊接尺寸对整个肋片的换热量以及换热系数的影响.结果显示,肋片焊接后,对整个肋片的换热量和换热系数有一定的影响,但影响较小.其中换热量根据焊接尺寸的增加先减小后增大;而换热系数呈波浪形变化,但有减小的趋势. 相似文献
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用CFD软件FLUENT对散热器常用的平翅片和波纹翅片表面的流体流动及换热过程进行了数值模拟,获得了翅片表面的流场、温度场、压力场以及换热量、换热系数的变化规律。模拟结果表明在相同气流量的条件下,波纹翅片的压力损失比平翅片的大,平均表面换热系数及换热量均比平翅片的高,翅片的形状结构对流场分布和强化换热效果的影响较大。 相似文献
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Nae-Hyun Kim Do-Young Kim Jun-Hyun Hwang 《Journal of Mechanical Science and Technology》2008,22(12):2498-2508
The effect of inclination angle on the heat transfer and pressure drop characteristics of brazed aluminum heat exchangers
was experimentally investigated under wet conditions. Three samples having different fin pitches (1.25, 1.5 and 2.0 mm) were
tested. Results show that heat transfer coefficients are not affected by the inclination angle. However, friction factors
increase as the inclination angle increases with negligible difference between the forward and backward inclination. The effect
of fin pitch on the heat transfer coefficient and on the pressure drop is also discussed. Comparison of the dry and wet surface
heat transfer coefficients reveals that dry surface heat transfer coefficients are significantly larger than wet surface heat
transfer coefficients. Possible explanation is provided by considering the condensate drainage pattern. The data are also
compared with the existing correlation.
This paper was recommended for publication in revised form by Associate Editor Man-Yeong Ha
Nae-Hyun Kim is a Professor of Mechanical Engineering, University of Incheon. His area of interest spans boiling and condensation, heat
transfer enhancement and heat exchanger design. He has been active in heat transfer community, and was a Chairman of Thermal
Engineering Division of KSME. He holds several editorial position including Journal of Enhanced Heat Transfer. He is a recipient
of Asian Academic Award awarded by SAREK and JSRAE. 相似文献
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针对由传统弓形折流板结构带来的壳程流动死区,从而引起的流动阻力大、传热效率低等问题,本文对折流板进行开孔,通过数值模拟的方法研究开孔折流板结构对列管式翅片换热器壳侧流体流动、传热及阻力性能的影响。研究发现,折流板开孔后,壳程流动死区明显减小,壳程传热系数及压降同比开孔前降低了;综合换热性能同比开孔前提升了。壳程压降随开孔率及板间距的增大而减小,壳程努塞尔数Nu随板间距的增大逐渐增大。从综合换热性能及场协同的角度分析发现,开孔率x=0.229、折流板间距H=85 mm的列管式换热器综合传热性能最佳。 相似文献
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An experimental study was conducted to investigate the effects of air-side fouling and cleaning on the performances of various
condenser coils used in unitary air-conditioning systems. A total of six condenser coils with different fin geometry and row
number were tested. Performance tests were performed at three different conditions: clean-as-received, after fouling, and
after cleaning. In all cases, it was observed that the fouling was mostly confined to the frontal face of the heat exchanger
as reported in the previous investigations. The amount of deposited dust was more dependent on fin geometry for the single-row
heat exchangers than for the double-row heat exchangers. The predominant effect of fouling was to cause a more significant
increase in air-side pressure drop than a degradation in heat transfer performance. For the single-row heat exchangers, the
pressure drop increased by 28 to 31%, while the heat transfer performance decreased by 7 to 12% at the standard air face velocity
of 1.53 m/s depending on fin shape. For the double-row heat exchangers, the pressure drop increased by 22 to 37%, and heat
transfer performance decreased by only 4-5% at the same air face velocity. Once the contaminated coils were cleaned according
to the given cleaning procedure the original performance of the heat exchangers could almost be recovered completely. The
pressure drop could be restored within 1 to 7% and the heat transfer performance could be recovered to within 1 to 5% of the
originally clean heat exchangers. Therefore, it is concluded that a periodic application of the specified cleaning technique
will be effective in maintaining the thermal performance of the condenser coils. 相似文献
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干湿工况下波纹翅片管换热器空气侧特性的对比 总被引:2,自引:1,他引:1
对7个带亲水层和3个不带亲水层波纹翅片管换热器在析湿工况下空气侧的换热压降特性进行了试验研究,在不同的入口风速和入口相对湿度下比较了干湿工况下的空气侧特性。结果表明,对带亲水层的波纹翅片,析湿工况下的压降显著地高于干工况下的;当入口风速小于0.5 m/s时,湿工况下的换热性能低于干工况下的,当入口风速增加到2.0 m/s时,湿工况下的换热性能则强于干工况下的。析湿工况下带亲水层波纹翅片的换热性能比不带亲水层波纹翅片的偏低一些,但是表面涂上亲水层可以大大降低空气侧的压降。提出析湿工况下波纹翅片管换热器空气侧的换热和压降关联式,平均误差分别为8.70%和7.90%,可用于设计波纹翅片管换热器或者评价它的性能。 相似文献
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同轴套管式地热能开采技术是用于中深层地热能开采的有效方式。为了增强同轴套管式换热器的换热效率,提出了一种带螺旋翅片的新型同轴套管式换热器。基于有限体积法,对比分析新型与普通型同轴套管式换热器的换热性能,得到螺旋翅片结构对换热性能的影响,揭示其强化传热机理。结果表明:通过增加螺旋翅片的翅高或减小螺旋翅片的螺距,可有效增强同轴套管式换热器内流体流动的湍流动能,达到提高换热性能的目的;与普通光滑管换热器相比,翅高为19 mm,螺距为300 mm的新型换热器在雷诺数为27000时,努赛尔数提高了35.5%,摩擦系数提高了91%,热性能系数达到最高1.093;增加翅片和减小螺距都可以增加采出温度和采热功率,翅高为19 mm,螺距为300 mm换热器较光滑管换热器采热温度提高了5.4 K,采热功率提高了32.4%。为高效同轴套管式换热器设计提供了理论依据。 相似文献