首页 | 本学科首页   官方微博 | 高级检索  
     

非共沸混合工质管内流动凝结换热系数的分析与计算
引用本文:陈民,李沛文,王秋旺,陶文铨.非共沸混合工质管内流动凝结换热系数的分析与计算[J].化工学报,2001,52(2):114-118.
作者姓名:陈民  李沛文  王秋旺  陶文铨
作者单位:西安交通大学能源与动力工程学院!陕西西安710049,西安交通大学能源与动力工程学院!陕西西安710049,西安交通大学能源与动力工程学院!陕西西安710049,西安交通大学能源与动力工程学院!陕西西安710049
摘    要:对非共沸混合工质R32 /R134a的管内流动凝结局部换热系数进行了理论分析和计算 .计算表明 ,非共沸混合工质的管内流动凝结换热系数总是低于具有等同物性的纯工质的换热系数 ,其换热系数下降的程度不仅受浓度的影响 ,还受干度的影响 .对混合工质R32 /R134a而言 ,换热系数的极小值出现在R32质量分数为10 %~ 30 %的区域内

关 键 词:非共沸混合工质  凝结换热  理论计算  R32  R134α  换热系数
文章编号:0438-1157(2001)02-0114-05
修稿时间:1999年7月6日

THEORETICAL CALCULATION ON FORCED CONVECTIVE CONDENSATION HEAT TRANSFER COEFFICIENT OF NONAZEOTROPIC MIXTURES INSIDE TUBE
CHEN Min,LI Peiwen,WANG Qiuwang and TAO Wenquan.THEORETICAL CALCULATION ON FORCED CONVECTIVE CONDENSATION HEAT TRANSFER COEFFICIENT OF NONAZEOTROPIC MIXTURES INSIDE TUBE[J].Journal of Chemical Industry and Engineering(China),2001,52(2):114-118.
Authors:CHEN Min  LI Peiwen  WANG Qiuwang and TAO Wenquan
Abstract:A theoretical approach to forced convective condensation heat transfer coefficient of nonazeotropic mixtures inside smooth tubes was developed. Calculations were performed for R32/R134a mixtures with the R32 mass fraction ranged from 0 to 60.1%. The results revealed that there was a reduction of heat transfer coefficient for a nonazeotropic mixture when compared with that of a single component substance with the same thermophysical properties. The reduction of the heat transfer coefficient depended not only on the mass fraction of the mixture, but also on the vapor quality of fluid. Besides, minimum heat transfer coefficients were observed at mass fractions ranging from 10% to 30% for R32/R134a mixtures.
Keywords:nonazeotropic mixture  condensation heat transfer  theoretical calculation  
本文献已被 CNKI 维普 万方数据 等数据库收录!
点击此处可从《化工学报》浏览原始摘要信息
点击此处可从《化工学报》下载全文
设为首页 | 免责声明 | 关于勤云 | 加入收藏

Copyright©北京勤云科技发展有限公司  京ICP备09084417号