1) analogy of heat and mass transfer
传热传质比拟
2) Mass/heat transfer analogy
传质/传热比拟
1.
The paper investigates the effect of change of the fin length of wing-type vortex generators (WVG) on heat transfer enhancement and pressure drop characteristics of finned oblate oval tube heat exchangers with six WVGs per tube, which are fixed in fin pitch and the ratio of height of WVGs to fin pitch under the same attack angle, via mass/heat transfer analogy of naphthalene sublimation.
应用萘升华传质／传热比拟实验方法,研究了固定片间距、相同三角翼形涡产生器翼高比和攻击角条件下, 涡产生器翼展改变时每管六涡扁长椭圆管管片式换热器换热板芯的换热和阻力特性,分析了涡产生器翼展的变化对错排椭圆管管片式换热器强化传热与阻力特性的影响。
3) heat/mass transfer analogy
传热-传质比拟
4) heat and mass transfer
传热传质
1.
Analysis of Heat and Mass Transfer Behavior of the PTA Oxidation Reaction Condensers;
PTA氧化反应冷凝器传热传质行为分析
2.
Theoretical model for calculation of the characteristics of heat and mass transfer for the slurry droplets;
雾滴传热传质特性的理论计算模型
3.
Analysis of heat and mass transfer on cornea in vacuum freeze-drying experiment;
角膜真空冷冻干燥实验的传热传质分析
5) mass and heat transfer
传质传热
1.
3D Simulation of mass and heat transfer for planar anode-supported solid oxide fuel cell;
平板式阳极支撑固体氧化物燃料电池传质传热仿真研究
2.
The process of mass and heat transfer on air gap membrane distillation was analyzed using water as medium,in particular,some condensation problems of air gap were put foreward,and some theoretical models about membrane flux were established and the validity of the models was cheched by experiments.
分析了以纯水为工质的空气隙膜蒸馏传质传热过程,提出了间隙冷凝问题,建立了膜通量理论计算模型,并进行数学求解,以实验为基础,验证了模型的正确性。
3.
A theoretical study on mechanism of mass and heat transfer was carried out based on several assumptions, namely one dimensional steady flow and non condensable gas in the air gap.
采用一维定常流动及空气间隙层中不冷凝的假定，对空气隙膜蒸馏系统的传质传热机理进行了理论研究，数学推导中对相关物理量进行了量阶分析，提出小量假设，导出了计算蒸馏通量的理论公式。
6) heat transfer and mass transfer
传热传质
1.
Based on heat transfer and mass transfer analysis, the mathematic model of drying process is established.
通过对传热传质过程的分析,建立干燥过程的数学模型,分别总结出烟叶在恒速干燥阶段和降速干燥阶段的能量平衡方程,推导出烟叶温度、水分随热空气的温度以及干燥时间的变化关系,对于优化控制设备的工艺参数、指导烟叶复烤生产、节约能耗有着重要的作用。
2.
Based on heat transfer and mass transfer analysis,the mathematic model of drying process is established.
通过对传热传质过程的分析,建立了干燥过程的数学模型,分别总结出烟叶在恒速干燥阶段和降速干燥阶段的能量平衡方程,推导出烟叶温度、水分随热空气的温度以及干燥时间的变化关系,对于优化控制设备的工艺参数、指导烟叶复烤生产、节约能耗有着重要的作用。
3.
On this basis set up was a phase-transformation heat transfer and mass transfer constant-pressure model for the drying process of a wet region with liquid-phase saturation-degree S and temperature T serving as parameters.
建立了以液相饱和度S和温度T为参数的湿区干燥过程相变传热传质常压模型。
补充资料：传热
分子式：
CAS号：
性质：见热传递
CAS号：
性质：见热传递
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