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An experimental study is performed on heat transfer and pressure drop characteristics in multiple-intersection flow networks consisting of a 60° intersection angle. Air is used as the working fluid. Both the pitch-to-hydraulic diameter ratio and the Reynolds number are varied. Results are expressed in terms of the heat transfer and friction factors and their ratio, called the “goodness factor.” It is found that the flow networks are characterized by a much higher goodness factor than a pin-finned surface of equivalent geometry when flow conditions are in the range of interested heat exchange applications. 相似文献
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厚翅片管内流体流动和传热的数值分析 总被引:4,自引:0,他引:4
本文应用Patankar等人[1]研究薄翅片管的湍流模型,对一种工业化的厚翅片管内的流体流动和传热进行了数值分析。计算范围包括了层流和湍流(Re=101~106),所得计算结果与较窄范围内实验所测的传热与阻力数据相当符合,本计算结果具有较大的推广价值。 相似文献
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Enhancement of heat transfer in a heat exchanger via a DC corona discharge was studied experimentally using a single-tube shell-and-tube heat exchanger. Air was the working fluid in both the tube and shell sides. Excitation of the tube side was via a single wire electrode, while that of the shell side was via four rod electrodes oriented symmetrically at 90° intervals. Three series of experiments were performed: (1) excitation of the tube side only, (2) excitation of the shell side only, and (3) simultaneous excitation of the tube and shell sides. Both heat transfer and pressure drop measurements were performed, with Reynolds number and electric field potential as parametric quantities in the tube and shell sides. It was found that highest enhancements take place when the tube and shell sides are excited simultaneously, yielding a 322% increase in the overall heat transfer coefficient. Study of the heat transfer enhancements per unit pumping power indicates that for the range of parameters studied, the technique is most efficient at moderate Reynolds numbers and at electrode potentials in the midrange between threshold and sparkover limits. 相似文献
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提出一种新的针肋结构,采用直径为0.25 mm的圆柱型针肋,在一定的错排和顺排相结合的优化布置方式下,能获得较高的换热效率.在三维空间上的对流换热模拟表明,铜制的针肋结构的换热系数要高出百叶窗翅片24%~34%,而流阻仅高出10%~16%.总换热量取决于翅片材料的导热性能,导热系数越高,针肋的强化作用约明显.本文提出的针肋翅片结构可以用来制造紧凑性更高的换热器. 相似文献
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A new w-type spirally fluted tube with enhanced heat transfer characteristics was developed and manufactured. The heat transfer and pressure drop characteristics of tubes with various geometric parameters were measured over a range of Reynolds numbers from 8,000 to 30,000 for water flowing horizontally through the tube with steam condensing on the outside surface. Experimental correlations for the pressure drop and the heat transfer coefficient were developed from a large amount of data using multivariable linear regression analysis. Factors influencing the heat transfer and flow were analyzed. The experiments showed that heat transfer coefficient can be increased by 3–8% with the pressure drop reduced by 5–10% compared with an ordinary spirally fluted tube. 相似文献
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绕圆柱体自由表面磁流体流动和传热的研究 总被引:1,自引:0,他引:1
本文对在不同雷诺数下,绕圆柱体的磁流体自由表面流动及传热进行了模拟,分析了磁场对绕流圆柱尾迹和涡分离的影响,获得了两种雷诺数下的电磁力密度、流场和温度场分布。结果表明,磁场不仅影响了流动的形态,而且对湍流有抑制作用,降低了自由表面的更新机制,从而减少了传热能力;在相同的Hartmann数下,相比低雷诺数下的流动换热情况,高雷诺数下的湍流不能被完全抑制,自由表面与尾迹的相互作用也较强,因而自由表面换热也较强。 相似文献
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The use of thermochromic liquid crystal technique (LCT) and true-colour image processing system in heat transfer modelling is described. Experimental procedure, led on rig at Technical University of Gdansk, cover full-field flow patterns in heat exchanger element (flat plate with fine-tubes in-line, staggered and with vortex generators) describing local heat transfer coefficient and Nusselt number on the surfaces. Also the dependence of average heat transfer and pressure drop on Reynolds number and geometrical parameters is investigated. 相似文献
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《Heat Recovery Systems and CHP》1993,13(1):67-77
The effects upon the performance of plate fin-tube cross flow heat exchangers due to outer surface geometry are considered. The finning parameter varying through 11 to 23, a total of ten geometrically distinct configurations were tested over a Reynolds number range from 100 to 30,000. The tube outside diameter with the collar thickness defines the characteristic dimension. The convective heat transfer coefficients are presented as plots of Colburn j-factor versus Reynolds number and compare well with previous studies. Typical data spread being ±10 percent range, the j-factor, the Reynolds number, and the finning parameter are correlated. 相似文献
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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
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An experimental investigation was made to study heat transfer in a pipe which is oscillated about an axis that is parallel to, but offset from, the pipe axis. Air was used as working fluid. The experimental setup was designed so as to provide oscillating motion of a test pipe. The measurement systems were installed on the oscillating section. For both steady and oscillating flows, the bulk air temperature and wall temperature, pressure drop, and frequency were measured. The parameters for this study were chosen as Reynolds number from 5,000 to 20,000 and oscillating frequencies from 10 to 20 Hz. The variations of Nusselt number versus these parameters were determined and presented graphically. Heat transfer enhancement of 42% was achieved at constant pumping power for oscillatory flow. 相似文献