1、

The solid-liquid interface moves away from the heat transfer surface , therefore, it makes phase change problem-linear.

由于相变过程中固液位置不断移动, 使得相变问题具有非线性的特征.

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2、

The Break Analysis for Heat Transfer Tubes in a Standard Vaporiser

标准式蒸发器换热管破裂分析

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3、

Influence Analysis of the Spacing among the Apparatus and Equipments on the Flow and Heat Transfer inside the Spacelab Racks

仪器设备间距对空间实验室机柜内部流动和传热的影响分析

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4、

Study on heat transfer between spot air conditioning area and high temperature surrounding area in warship

舰船局部空调区与高温环境区的传热研究

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6、

Boiling Heat Transfer Enhancement of Two Phase Flow in Lunate Channel

单管弦月形通道微膜热虹吸两相流沸腾传热实验研究

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7、

Study on enhanced heat transfer of lunate channel in solar energy air-conditioning system

弦月形通道在太阳能空调系统中的强化传热研究

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8、

STF ( Sweptback Trapezoid Flag) type dynamic insert in the characters of self excitation oscillation and finite span wing is used to enhance the turbulent heat transfer.

利用STF元件(后掠梯形一旗形插入件)的自激振荡组件系统特性和有限翼展机翼特性进行了管内紊流强化换热的研究。

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9、

Study on Effects of Heat Transfer Coefficient between Polymer and Mold on Melt Filling Flow in Micro Injection Molding

微注塑成型中熔体与壁面间传热系数对充模流动影响的研究

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10、

D Numerical Simulation on Mold Filling Coupling Fluid Flow and Heat Transfer in the Aluminium Alloy Casting

耦合传热与流动的铝合金铸件充型三维数值模拟

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11、

Heat Transfer Analysis of Process Gas in HXD

HXD气流干燥过程工艺气流传热分析

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12、

Heat transfer calculation and analysis of GPB plate-dryer

GPB型板式干燥机传热计算与分析

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13、

Numerical Simulation of 2D Jet-to-Crossflow Heat Transfer with Different Turbulence Models

应用不同紊流模型的二维横向射流传热数值模拟研究

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14、
15、

The convection heat transfer coefficient and the friction coefficient both decrease with the fin height increasing.

翅片高度增加,对流换热系数和摩擦系数减小.

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16、

In addition heat transfer coefficient and friction factor correlations are also obtained under experimental ranges. 2.

同时对所实验的三种换热器翅片表面在实验范围内拟合了相应的换热与阻力关联式.

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17、

The fluid flow and heat transfer in welding processes have major effect on welding quality.

焊接熔池中的流体流动及传热过程是影响焊接质量的重要因素.

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18、

It is shown that the Nusselt numbers inside microtube are still in the range of 3.66 and 4.36 with convective heat transfer boundary condition outside the tube.

结果表明,当管外为对流换热边界条件时,管内充分发展对流换热的Nu依然在3.66~4.36之间。

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19、

Experimental Investigation on Flow and Heat Transfer in Rough Microtube

微粗糙管内部流动与对流换热的实验研究

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20、

From the simulated result, gravity had so little effect on flow condensation heat transfer in microtube that it could be neglected.

模拟的结果表明,重力对微圆管流动凝结换热的影响非常小,可被忽略;

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