检索规则说明:AND代表“并且”;OR代表“或者”;NOT代表“不包含”;(注意必须大写,运算符两边需空一格)
检 索 范 例 :范例一: (K=图书馆学 OR K=情报学) AND A=范并思 范例二:J=计算机应用与软件 AND (U=C++ OR U=Basic) NOT M=Visual
作 者:谢迎春 马洪亭[1] 徐畅 马硕 陈默 刘军 孙国强 XIE Yingchun;MA Hongting;XU Chang;MA Shuo;CHEN Mo;LIU Jun;SUN Guoqiang(School of Environmental Science and Engineering,Tianjin University,Tianjin 300350,China;CNNP Kunhua Energy Development Co.,Ltd.,Hangzhou 311113,Zhejiang,China)
机构地区:[1]天津大学环境科学与工程学院,天津300350 [2]中核坤华能源发展有限公司,浙江杭州311113
出 处:《化工进展》2023年第3期1187-1194,共8页Chemical Industry and Engineering Progress
基 金:国家自然科学基金(51876137);中核集团横向课题(0505000281)。
摘 要:为研究竖管渗流降膜蒸发式冷凝器,通过仿真和实验相结合的手段,探究了冷凝器单管在不同管外温度、空气雷诺数与液体雷诺数等多工况下的传热特性。结合此前研究中存在的问题,合理选择了物理模型与边界条件,获得了降膜过程的轴向温度、热通量分布等并对径向位置进行了时间序列分析。结果表明逆向通风传热效果优于顺向通风,但易加剧管段下部液膜不稳定甚至出现干壁。通过时间序列分析发现干壁区域会被液膜快速覆盖,因此短暂干壁对整体传热影响并不十分明显,仍需注意逆向通风强度过高会对管子下部液膜的稳定性造成显著影响,本文工况下推荐单管空气雷诺数不宜超过3500。此外,测试结果显示本文单管传热量约为2200W,与模拟结果相差6.7%,单管综合传热系数为1400W/(m^(2)·K)左右。In order to study the vertical pipe seepage falling film evaporative condenser,the heat transfer characteristics of the single condenser tube under different external temperature,air Reynolds number and liquid Reynolds number were explored by using the combination of simulation and experiment method.Combined with the problems in previous research,the physical model and boundary conditions were selected reasonably,the axial distribution of temperature and heat flux density of the falling film process were obtained,and the radial position was analyzed in time series.The results showed that the heat transfer effect of reverse ventilation was better than that of co-directional ventilation,but it was easy to aggravate the instability of the liquid film in the lower part of the pipe section and even cause dry wall.It was found that the dry wall area would be covered by the liquid film immediately through time series analysis.Therefore,the effect of short-term dry wall on the overall heat transfer would not very obvious.It was still necessary to pay attention to the great influence of the high reverse ventilation intensity on the stability of the lower liquid film.It was recommended that the single-pipe air Reynolds number should not exceed 3500 under the working conditions of this paper.In addition,the test results showed that the heat transfer of a single tube in this paper was about 2200W,which was 6.7% different from the simulation results,and the comprehensive heat transfer coefficient of the single tube was about 1400W/(m^(2)·K).
分 类 号:TK172[动力工程及工程热物理—热能工程]
正在载入数据...
正在载入数据...
正在载入数据...
正在载入数据...
正在载入数据...
正在载入数据...
正在载入数据...
正在链接到云南高校图书馆文献保障联盟下载...
云南高校图书馆联盟文献共享服务平台 版权所有©
您的IP:216.73.216.15