共查询到19条相似文献,搜索用时 157 毫秒
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介绍了一种适用于小流量大温升的新型盘状螺旋管换热器,具有结构简单、质轻,体积小的特点;利用相关的实验研究,获得其换热性能和流动阻力特性。实验结果表明,其在小流量下仍具有较高的传热系数,适合于做热泵热水器的水冷换热器。 相似文献
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为了研究改变翅片材料对套片式翅片管换热器性能的影响,分别对采用铝翅片和黄铜翅片的套片式翅片管换热器(结构参数基本相同)进行传热特性与空气流动阻力特性的试验。试验得到了试件在一系列试验工况下的传热数据与管外空气流动阻力数据,通过计算得出了相应的传热准则关系式与管外空气流动阻力准则关系式,绘制了传热系数和管外空气流动阻力的有关图线。结果表明:黄铜翅片套片式换热器与铝翅片套片式换热器相比,换热性能优势明显,其原因主要是铝材比铜材软,与铜管胀接后的接触热阻大,因此换热性能更弱。 相似文献
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《工程热物理学报》2020,(7)
通过实验的方法,分别分析了采用大导角半径(Large corrugation fillet radii,rl)的非对称波节管、对称波节管和光管管壳双侧的传热性能和阻力性能的影响规律,研究非对称波节管流向对换热器总换热性能和总阻力性能的影响。研究结果表明,非对称波节管和对称波节管的综合换热性能均优于光管,且壳侧的综合换热性能提升优于管侧。非对称波节管的换热性能与对称波节管差别较小,但阻力性能更低,rl位于管侧波节前流段或壳侧波节后流段均可以明显降低阻力性能。非对称波节管换热器在逆流下,rl在管侧前流段时,换热器整体综合换热性能最优,平均是光管换热器的1.44倍;在并流下,rl在管侧后流段时,换热器整体综合换热性能相对更好,比光管换热器提升了39.07%。 相似文献
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Abstract This article presents the empirical study of a heat pipe heat exchanger that was directly experiencing the ambient tropical air in its evaporator section. The performance of the heat pipe heat exchanger was monitored during two weeks of operation to determine the performance curves. The temperature of return air was controlled at about 22°C as the representative temperature of inside air, and a face velocity of 2 m/s on the heat pipe heat exchanger coil was established for this purpose. It was found that for the present investigation, the heat pipe heat exchanger can pay for itself in 1.5 years. 相似文献
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霜形成对翅片管换热器空气侧表面传热系数影响的实验研究 总被引:1,自引:1,他引:0
在空冷系统中,换热器空气侧的表面结霜问题是影响其应用和发展的主要问题。通过对结霜条件下翅片管换热器空气侧换热性能的实验研究,得出了空气湿度、翅片间距、风速等参数变化对空气侧当量表面传热系数的影响;结果表明在一定的范围内,结霜前期h0值随结霜时间τ急剧下降,在结霜后期,这些参数对h0值的影响大为削弱。 相似文献
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工业能耗占我国总能耗超过70%,而其能源利用效率不足50%,因此工业余热高效回收利用是节能减排的重要途径之一。热泵技术是提升能量品位的有效方法,但吸收式热泵需要配置三个不同温度品位的热源或热汇,而电动热泵受热力学循环、工质物性、压缩机耐温耐压限制以及避免润滑失效一般只能工作于有限温度范围(<100℃)之内,因此该研究将吸收式循环与压缩式循环进行深度耦合,用于直接回收工业余热制取高温热水,同时确保压缩机的安全稳定运行.该文首先分析耦合热泵换热器的运行原理,其次建立了耦合热泵换热器的数学模型,最后对模型进行求解分析了关键参数对耦合热泵换热器性能影响变化规律。在设计工况下,当制取133℃热水时,耦合热泵换热器COP达到3.6,压缩机排气压力为1.2 MPa,排气温度为79℃,远低于压缩机耐温耐压上限和润滑油失效温度,因此耦合热泵换热器在利用余热制取高温热水或蒸汽领域具有一定的应用潜力。 相似文献
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鉴于以加热或冷却为目的的热量传递过程,其不可逆性应以NFDA1的耗散率来度量,为此可以用换热器中的NFDA1耗散率定义换热器的当量热阻,它既包含换热器中的传热热阻,还包含了由非逆流形式和非平衡流引起的附加热阻. 换热器当量热阻的倒数称之为换热器的当量热导. 通过NFDA1耗散定义的换热器当量热阻建立了传热不可逆性与有效度的联系,并导得了换热器有效度与当量热导(热阻)和热容量流比的统一函数关系式,它适用于不同流程布置的换热器. 因此,有效度-热导(热阻)方法能更方便于不同类型换热器性能的分析和比
关键词:
换热器
热阻
耗散
熵产 相似文献
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Cooling technology is facing new challenges with the increase of electronic equipment power onboard aircraft. The traditional heat sink based on high-altitude bleed air does not satisfy this increase of cooling demands. In this article, an air/air-type skin heat exchanger is studied for cooling aircraft electronic equipment. It uses outside high-altitude cold air rather than bleed air as a heat sink. This cooling technology can effectively remove the heat load of high-power electronic devices without greatly increasing aircraft performance penalty. To assess its high-altitude heat transfer performance, an experimental prototype was designed and made. Some experiments were conducted on a ground experimental test. The heat transfer criteria formulas were obtained for both the side air in the skin heat exchanger and its convective heat transfer coefficients. Based on these experimental analyses, the heat transfer performances of the skin heat exchanger in a high-altitude cruise condition are deduced when it is assumed to be installed at an unfavorable position and a favorable position, separately. This work tries to provide a technical support for its future onboard application. 相似文献
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Forced convection heat transfer from a helically coiled heat exchanger embedded in a packed bed of spherical glass particles was investigated experimentally. With dry air at ambient pressure and temperature as a flowing fluid, the effect of particle size, helically coiled heat exchanger diameter, and position was studied for a wide range of Reynolds numbers. It was found that the particle diameter, the helically coiled heat exchanger diameter and position, and the air velocity are of great influence on the convective heat transfer between the helically coiled heat exchanger and air. Results indicated that the heat transfer coefficient increased with increasing the air velocity, increasing helically coiled heat exchanger diameter, and decreasing the particle size. The highest heat transfer coefficients were obtained with the packed-bed particle size of 16 mm and heat exchanger coil diameter of 9.525 mm (1/4 inch) at a Reynolds number range of 1,536 to 4,134 for all used coil positions in the conducted tests. A dimensionless correlation was proposed for Nusselt number as a function of Reynolds number, particle size, coil size, and coil position. 相似文献