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刀片电池直冷冷却热管理系统设计与优化 被引量:2
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作者 赖艳红 罗立晟 +1 位作者 陈镜如 刘益才 《制冷技术》 2023年第2期72-77,共6页
针对比亚迪汉EV车型纯电动汽车的刀片电池设计了一种直冷式电池热管理系统,计算了刀片电池热负荷参数,以制定热管理系统设计目标,并通过数值仿真验证其可行性。对多腔结构和蛇形结构的直冷板进行对比分析,进一步总结提出优化建议。结果... 针对比亚迪汉EV车型纯电动汽车的刀片电池设计了一种直冷式电池热管理系统,计算了刀片电池热负荷参数,以制定热管理系统设计目标,并通过数值仿真验证其可行性。对多腔结构和蛇形结构的直冷板进行对比分析,进一步总结提出优化建议。结果表明,本文所设计的直冷式电池热管理系统可以将电池包的最高温度控制在20~40℃以内,且各单体电池温差小于5℃,满足散热目标。通过对比不同结构的直冷板的最高温度变化情况,得到蛇形结构直冷板的散热效果优于多腔结构。 展开更多
关键词 热管理 直冷冷却 刀片电池 数值分析
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Influence of thermal flow field of cooling tower on recirculation ratio of a direct air-cooled system for a power plant
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作者 Zhao Wanli Liu Peiqing 《Engineering Sciences》 EI 2008年第4期64-70,共7页
In order to get thermal flow field of direct air-cooled system,the hot water was supplied to the model of direct air-cooled condenser(ACC). The particle image velocimetery (PIV) experiments were carried out to get the... In order to get thermal flow field of direct air-cooled system,the hot water was supplied to the model of direct air-cooled condenser(ACC). The particle image velocimetery (PIV) experiments were carried out to get thermal flow field of a ACC under different conditions in low velocity wind tunnel,at the same time,the recirculation ratio at cooling tower was measured,so the relationship between flow field characteristics and recirculation ratio of cooling tower can be discussed. From the results we can see that the flow field configuration around cooling tower has great effects on average recirculation ratio under cooling tower. The eddy formed around cooling tower is a key reason that recirculation produces. The eddy intensity relates to velocity magnitude and direction angle,and the configuration of eddy lies on the geometry size of cooling tower. So changing the flow field configuration around cooling tower reasonably can decrease recirculation ratio under cooling tower,and heat dispel effect of ACC can also be improved. 展开更多
关键词 direct air-cooled condenser thermal flow field characteristics recirculation ratio PIV experiment
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Experimental Study on Latent Heat Storage Characteristics of W/O Emulsion-Supercooling Rate of Dispersed Water Drops by Direct Contact Heat Exchange
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作者 Shin-ichi Morita Yasutaka Hayamizu +2 位作者 Akihiko Horibe Naoto Haruki Hideo Inaba 《Journal of Thermal Science》 SCIE EI CAS CSCD 2013年第2期145-151,共7页
Recently, much attention has been paid to investigate the latent heat storage system. Using of ice heat storage system brings an equalization of electric power demand, because it will solved the electric -power-demand... Recently, much attention has been paid to investigate the latent heat storage system. Using of ice heat storage system brings an equalization of electric power demand, because it will solved the electric -power-demand-concentration on day-time of summer by the air conditioning. The flowable latent heat storage material, Oil/Water type emulsion, microencapsulated latent heat material-water mixture or ice slurry, etc., is enable to transport the latent heat in a pipe. The flowable latent heat storage material can realize the pipe size reduction and system efficiency improvement. Supercooling phenomenon of the dispersed latent heat storage material in continuous phase brings the obstruction of latent heat storage. The latent heat storage rates of dispersed water drops in W/O (Water/Oil) emulsion are investigated experimentally in this study. The water drops in emulsion has the diameter within 3 ~ 25μm, the averaged water drop diameter is 7.3μm and the standard deviation is 2.9μm. The direct contact heat exchange method is chosen as the phase change rate evaluation of water drops in W/O emulsion. The supercooled temperature and the cooling rate are set as parameters of this study. The evaluation is performed by comparison between the results of this study and the past research. The obtained experimental result is shown that the 35K or more degree from melting point brings 100% latent heat storage rate of W/O emulsion. It was clarified that the supercooling rate of dispersed water particles in emulsion shows the larger value than that of the bulk water. 展开更多
关键词 Heat Storage Latent Heat W/O Emulsion Direct Contact Heat Exchange
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