共查询到18条相似文献,搜索用时 78 毫秒
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在模化试验验证的基础上,通过数值模拟,获得了翅片间距P_f及开缝数量n_s对开缝翅片管换热器性能的影响规律:n_s≤6时,翅片侧Nu和流动阻力均随着P_f增大而减小;n_s6时,翅片侧Nu随P_f增大先减小后增大,而阻力逐渐降低;P_f=3.51~3.97 mm时,随n_s增大,阻力逐渐增大,n_s=4~6时,翅片侧Nu逐渐增大,n_s=6~8时,翅片侧Nu变化较小;P_f=3.97~4.43 mm时,n_s由4片增加至8片,翅片侧Nu和阻力均逐渐增大。根据不同结构的开缝翅片管换热器的综合流动换热性能,提出了P_f与n_s的最佳组合。 相似文献
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通过对不同开缝数量、不同相对开缝高度的单向开缝翅片管换热器进行模拟,分析开缝数量、相对开缝高度对单向开缝翅片管换热器传热与阻力性能的影响规律。结果表明:在开缝数量为3~7片时,翅片侧Nu和f因子随着开缝数量的增加而增大,但Nu增幅逐渐减小;将开缝的数量取为5片能得到最好的综合性能;在相对开缝高度为0.3~0.7时,翅片侧Nu和f因子随着相对开缝高度的增加而增大,但当相对开缝高度在0.5~0.7范围内,翅片侧Nu的增幅减小;将相对开缝高度取为0.5能得到最好的综合性能。 相似文献
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通过对不同相对横向管间距S1/do、相对纵向管间距S2/do的单向开缝翅片管换热器进行模拟,分析研究参数范围内S1/do与S2/do变化对单向开缝翅片管换热器性能的影响规律,模拟结果的准确性得到了模化试验的验证。结果表明:在S1/do=2.10~2.84、S2/do=1.76~2.50范围内,单向开缝翅片管换热器翅片侧的阻力受S2/do的影响更大;单向开缝翅片管换热器综合性能受S1/do、S2/do影响的程度相当。 相似文献
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为了获得翅片间距Pf对平直翅片管换热器的传热与阻力特性的影响规律,根据相似模化原理对3种不同Pf的平直翅片管换热器进行了试验研究。结果表明:雷诺数Rea在4 000~8 000范围内,努赛尔数Nua数随Rea的增大而增加,欧拉数Eua随Rea的增大而降低;同一Rea下,Nua随Pf减小而增加,但增加不明显,Eua随Pf增大而降低;同一Rea下,Pf越大,综合流动传热性能越好,但实际换热面积会减小,需综合考虑。研究成果可为汽轮发电机平直翅片管换热器的结构和性能优化提供依据。 相似文献
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为解决空气源热泵冬季在制热工况下因室外机内翅片换热器换热效率低引起系统供能性能下降的问题,以组合式翅片管换热器为研究对象,在模化实验的基础上,采用数值模拟的方法分别对翅片换热器的传热及流阻性能影响因素进行分析.研究结果表明:在本文研究背景下,入口风速、翅片厚度、开缝数目对前开孔后开缝型的翅片组合形式换热器传热效率具有一定程度的影响;以上述三种因素为目标函数对换热器进行多目标优化时,入口风速取3 m/s,翅片厚度为0.16 mm,后排开缝数目为6,换热器能得到较好的综合性能;在此基础上,拟合出适合于该组合形式的传热和流阻关联式. 相似文献
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L型高低翅片管传热性能试验哈尔滨工业大学尚希禹沈阳航空工业学院金乾,朱宝娟1前言近年来,为提高冷却元件的传热能力,减少管束传热面积,翅片管式换热器在石油化工、电站等行业得到广泛的应用。本文在传热风洞上对4个厂家的两种规格的铜管绕铝翅片的单管,L型高翅... 相似文献
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Experimental Study on Heat Transfer and Pressure Drop Characteristics of Four Types of Plate Fin-and-TUbe Heat Exchanger Surfaces 总被引:3,自引:0,他引:3
ExperimentalStudyonHeatTransferandPressureDropCharacteristicsofFourTypesofPlateFin-and-TUbeHeatExchangerSurfaces¥H.J.Kang;W.L... 相似文献
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Jun Liu Fenghao Wang Wanlong Cai Zhihua Wang Qingpeng Wei Jiewen Deng 《国际能源研究杂志》2019,43(12):6337-6352
Deep borehole heat exchanger (DBHE) is attracting attention intensively owing to much more geothermal extraction, higher efficiency for heat pumps, and lesser land demand compared with shallow borehole heat exchanger. DBHE is usually dipped into several thousand meters in the subsurface, having a complicated heat transfer with surrounding rock–soil. However, the heat transfer characteristics below surface under different conditions are rarely studied. In this study, a numerical model considering the comprehensive effects of geothermal gradients and heat loss from inner pipe was proposed. The model was validated with experimental data and Beier analytical solution. Based on the model, the effects of primary design parameters on the heat transfer performance below surface along the pipe were investigated. The results indicate that temperature at pipe bottom increases with inlet flow rate decreasing, while the heat load cannot be extracted fully to the surface because of the heat loss of inner pipe. When the inlet flow rates decrease from 41.39 to 4.52 m3/h, the heat loss ratio increases from 25.5% to 63.7%. It is an effective way of insulating inner pipe to reduce heat loss under low inlet flow rates. Increasing the velocity in inner pipe by lessening the inner pipe diameter can also decline the heat loss well. While by this way, the increasing pumping power resulting from the higher velocity in inner pipe has to be considered. This study is significant to effective optimization of DBHE and energy conservation of buildings. 相似文献
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Kwang-Tzu YANG 《热科学学报(英文版)》2005,14(2):172-180
Experiments were carried out to study the heat transfer characteristics of a single-row aluminum fin-and-tube crossflow heat exchanger with an emphasis in the regime of low flow rate of the in-tube fluid. The Chilton-Colburn analogy, in conjunction with the least-squares power-law technique, was used to correlate experimental data. Both air- and water-side heat transfer correlations were developed in the form of the Nusselt numbers as a function of Reynolds and Prandtl numbers. The experimental observations are quantitatively compared to the predictions of correlations available in the published literature. Different transfer mechanisms were found to be operative in the ranges of water-side Reynolds numbers based on the hydraulic diameter. In a range of Reynolds number from 1,200 to 6,000, the water-side thermal resistance accounts for less than ten percent of the overall thermal resistance. The dominant thermal resistance is always on the air-side. On the other hand, the thermal resistance of water-side is nearly equal to that of air-side in a Reynolds number range from 500 to 1,200. 相似文献
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