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作 者:严俊杰[1] 李鲁宁[1] 胡申华[2] 郭迎利[1]
机构地区:[1]西安交通大学能源与动力工程学院,西安710049 [2]新疆大学电气工程学院,乌鲁木齐830008
出 处:《西安交通大学学报》2007年第1期1-4,36,共5页Journal of Xi'an Jiaotong University
基 金:教育部新世纪优秀人才支持计划资助项目(NCET-04-0940)
摘 要:针对开式系统中水膜闪蒸的换热特性进行了实验研究.实验参数选择如下:循环水过热度为1~15K;闪蒸室压力分别为20.4、30.2、47.4kPa;水膜厚度分别为100和300mm;循环水流量分别为0.028、0.056、0.083kg/s.实验结果表明:闪蒸换热系数的变化范围为60~140kW/(m^2·K),并随过热度的增大而减小,随闪蒸室内饱和压力的升高而增大,随水膜厚度的增大而减小.根据实验结果,基于闪蒸过程类似核态沸腾,给出了换热系数与各影响参数之间关系的实验关联式,与实验结果的误差小于27%.Heat transfer characteristics of flash evaporation of water film in an open system were studied. The tests were conducted at superheat temperature differences of 1-15K, flash evaporation pressures of 20.4, 30. 2 and 47.4 kPa, water film thicknesses of 100 and 300 mm, and mass flux of 0. 028, 0. 056, 0. 083 kg/s. The results show that under the operating condition, heat transfer coefficient ranges from 60 to 140 kW/(m^2 K) which decreases with the increase of superheat, increases with the increase of flash evaporation pressure and decreases with the increase of water film thickness. According to the results in this experiment, based on the similarity between flash evaporation and nuclear boiling, an experimental expression of heat transfer coefficient with all of the influence parameters was presented with the maximum error of 27%.
分 类 号:TK124[动力工程及工程热物理—工程热物理]
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