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1.
降膜结晶过程的数值模拟   总被引:5,自引:0,他引:5  
本文采用数值方法对在工业上有着广泛应用前景的降膜结晶分离过程进行了模拟,提出了一套描述降膜结晶过程的降膜流动、传热、传质及结晶相变相互耦合的以控制容积为基础的有限差分的湍流数值计算模型和算法。本模型的计算结果与以前简化模型的计算结果相比,更符合实验值.  相似文献   

2.
建筑排风冷能回收是降低建筑能耗的重要手段。本文基于Fluent提供的VOF模型,编写蒸发冷凝相变的UDF程序,对用于建筑排风冷量回收的平行流热管内部的蒸发和冷凝特性进行了数值模拟,计算结果揭示了平行流热管内的气液两相流特性以及复杂相变传热传质的演变过程。结果表明:蒸发主要发生在液池内部,冷凝主要发生在冷凝段和绝热段的近壁面部位;相变传质过程是保证热管高效换热的关键因素。本文结果为设计平行流热管换热器提供理论依据。  相似文献   

3.
针对溴化锂溶液水平薄膜流动下吸收水蒸汽的过程,本文建立、求解了其数学模型,同时采用激光全息干涉方法进行了局部光测实验,并将实验结果与本文模型的计算结果进行了比较和分析,表明实验与数值计算结果基本吻合,从而在局部细节验证了模型的正确性,揭示了水平薄膜流吸收蒸汽过程的传热传质机理,并在光测试验上取得了一定成果。  相似文献   

4.
循环床中气固两相局部传热传质规律的研究   总被引:5,自引:0,他引:5  
本文对含湿颗粒在循环床中干燥过程的传热传质规律进行了实验研究。本文发展的一种利用双热电偶参考标定法,获得了气、固两相沿床高的局部温度。对气体表观流速,固体循环率,颗粒初始含湿量对传热传质的影响进行了分析和讨论。所获得的循环床中传热传质系数的实验关联式,可供干燥颗粒、造粒、粒面包裹等工业设计参考使用。  相似文献   

5.
将直接模拟蒙特卡洛(DSMC)方法与传热传质理论相结合,建立了考虑颗粒碰撞与热质传递过程的气固两相撞击流理论模型。应用所建理论模型计算分析了撞击流内的热质传递过程,以及颗粒预热温度对传递过程的影响。结果表明:利用所建模型对撞击流干燥过程的计算结果合理、正确,该模型能够有效地用于撞击流内传热传质过程的理论分析;撞击流内传递过程的有效体积位于两喷嘴之间区域,且在撞击区内的传递过程得到强化;提高颗粒的预热温度可以有效提高干燥装置的干燥强度。  相似文献   

6.
为准确预测一次干燥时间,降低能耗,应用准稳态传热传质理论,在考虑干燥层传质能力对干燥速率影响的情况下,建立了基于微元法的传质控制模型。利用循环计算的方法,对模型进行了求解。计算结果表明:所建立的模型能准确地预测冻干过程,模拟值与实验值吻合良好。若对模型进一步完善和修正,对实际应用有一定的指导意义。  相似文献   

7.
波纹板片上降膜吸收过程的传热传质数值仿真   总被引:1,自引:0,他引:1  
建立了在连续的竖直波纹板上降膜吸收过程的传热传质数学模型,并进行了无因次化处理和仿真数值计算。给出了溶液液膜内流场、温度场、质量分数分布的计算结果,比较了交叉双尺度波纹板片和当量平板上的吸收传热和传质系数随不同溶液喷淋密度的变化结果,显示出前者具有更好的性能,并讨论了波纹节距对传热和传质系数的影响关系。  相似文献   

8.
从理论上分析了膜换湿过程中传质过程和传热过程之间的耦合关系,建立了相应的物理数学模型,发展了一种计算热质耦合的方法。分析结果表明传质过程对传热过程的影响主要体现在两方面:一是质量流携带的焓对传热过程的影响,二是吸附和脱附产生的吸附热对传热过程的影响。而传热过程对传质过程的影响主要体现在温度对膜湿阻的影响。采用数值模拟的方法对热质耦合过程进行了研究,结果表明:当热流与质量流方向相同时,热阻随湿度差的增大显著增大,而当热流与质量流方向相反时,热阻随湿度差的增大显著变小,而膜两侧湿度差对湿阻基本无影响。温度的升高会显著增大传质通量,同时降低湿阻,从而使得热流密度和热阻也受到显著的影响。  相似文献   

9.
矩形封闭腔内非饱和多孔介质的传热传质特性研究   总被引:1,自引:0,他引:1  
本文建立了矩形封闭腔内非饱和多孔介质的二维传热传质数理模型,并对R113的蒸发相交进行了数值模拟。根据计算结果着重讨论了流体瑞利数Ra,介质达西数Da以及腔体冷热端温差△T的变化对其传热传质特性的影响,得出一些有用的可指导工程实践的结论。  相似文献   

10.
近年来微槽内的液体流动和传热受到了广泛关注,成为新的研究热点。本文在对热润湿作用下水平螺旋管表面反重力流形成及其流动特性进行探索的基础上,建立了适用于水平螺旋槽管壁面二元混合物反重力流蒸发传热传质耦合的物理模型。模拟结果表明,由于液膜内部存在着传质,径向有明显的浓度梯度,从而降低了蒸发传热的温度推动力。酒精溶液的浓度越...  相似文献   

11.
An experimental analysis of ammonia-water absorption process was performed for the falling film and bubble modes in a plate-type absorber. The experiments were made to examine the effects of solution flow rate and gas flow rate on the performance of the absorber. It was found that the bubble mode is superior to the falling film mode for mass transfer performance, and more heat was generated in the bubble mode. Increase of solution flow rate rarely affected the mass transfer, but improved the heat transfer. As the gas flow rate increased, fluidization occurred in the bubble mode and influenced the thermal boundary layer. However, channeling appeared in the falling film mode and decreased the heat transfer area. Increase of the gas flow rate greatly enhanced the performance of heat transfer in the bubble mode but made it worse in the falling film mode. Finally, the results were converted into dimensionless numbers to elucidate physical phenomena and we plotted Sherwood number versus Reynolds number for mass transfer performance and Nusselt number versus Reynolds number for heat transfer performance.  相似文献   

12.
The dynamic process of rewetting of the overheated surface by gravitationally falling film of cryogenic liquid was firstly modeled numerically with consideration of local distribution of heat transfer coefficient in the wetting zone along the 2D front. The front shape corresponding to self-organizing regular structures observed in experiments was obtained in the numerical experiment. Evolution of the front shape was studied. It was shown that local motion velocities of different areas of the 2D wetting front differed significantly. Total time of transitional process was determined by the minimal velocity of evaporating liquid boundaries in the front zones between boiling jets. This model allows quantitative determination for the wetting front velocity, variable in time and space, and temperature fields in the heater. Reliability of calculation results was proved by direct comparison with experimental data.  相似文献   

13.
Heat transfer in the laminar-wavy film of liquid falling over the heated plate is studied numerically. To describe the wavy film flow the integral model is applied. Calculation results demonstrate the effect of physical properties of liquid and wavy flow parameters on heat transfer intensification by stationary running waves.  相似文献   

14.
Three-dimensional interfacial waves developing on the free surface of falling liquid films are known to intensify heat and mass transfer. In this context, the present paper studies the effect of electrostatic as well as of thermo-capillary forces on a falling film of a dielectric liquid. Therefore, measurements of the local film thickness using a confocal chromatic imaging method were performed under isothermal and heated conditions. The experimental results show that both forces destabilize the flow. It is found, that the application of an additional electric field under heating conditions enhances the generation of rivulets, thereby reducing the overall heat transfer coefficient.  相似文献   

15.
吸收式热泵降膜吸收过程传热传质理论分析及实验关联   总被引:2,自引:0,他引:2  
本文对吸收式热泵的降膜吸收过程中动量、能量及质量传递进行了较全面的理论分析,建立了变膜厚降膜吸收数学模型,揭示了吸收过程中热量、动量、质量传递过程间的相互作用关系并提出以PE数为核心的凝结式降膜吸收理论。依据该理论,成功地对降膜吸收过程传热实验数据进行关联,获得了实用传热计算的无因次准则公式。  相似文献   

16.
根据传热传质分离的吸收形式,设计加工了一台溴化锂绝热降膜吸收的实验装置,对溴化锂水溶液在倾斜平板上对水蒸气的吸收特性进行了实验研究,分析了预冷却温差、溶液流量及平板倾角对吸收过程的影响。实验结果表明:预冷却温差、溶液流量及平板倾角越大,溴化锂溶液对水蒸气的吸收效果越好,并认为吸收过程可以分成三个步骤,另外就热质分离吸收器的设计过程中的溴化锂溶液的最小速度提出建议。  相似文献   

17.
Investigation results on hydrodynamics, heat transfer, and crisis phenomena in laminar-wave liquid films falling down the surfaces of different geometry are presented in this study. Freon mixture R21/R114 with initial concentration of low-boiling component of 4?C16.6 % was used as the working liquid. The film Reynolds number at the inlet to the experimental section varied from 60 to 700. The heat flux density was changed within 0?C5 W/cm2. The images of wave surface of the falling liquid film and formation of dry spots were visualized and recorded by the high-speed video camera. Results of investigation of the wave structure of the film surface, measurements of heat transfer coefficients under the conditions of boiling, and critical heat fluxes in the film flow over the smooth and structured surfaces are presented.  相似文献   

18.
水平管降膜蒸发器传热优化研究   总被引:1,自引:0,他引:1  
基于分布参数方法,对大型制冷系统中的水平管外降膜蒸发进行了传热优化数值模拟计算.在计算中,分析了饱和的液态制冷剂R134a在水平的铜管束外流动蒸发的换热特性.模型考虑了不同的管子类型和2流程不同管程布置对蒸发器换热特性的影响,结果表明,蒸发器采用Turbo-EHP管的性能高于其它管;不同管程布置对蒸发器性能的影响比较大,其中,下进上出管程布置的换热性能优于其它管程布置.同时,本文考虑了传热管外"干斑"对换热的影响.本文结论对于大型制冷系统中的降膜蒸发器传热优化设计具有指导性意义.  相似文献   

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