风速对波节管传热性能的影响

本文通过实验研究，找出了空气的流速（即风速）对一种新型换热元件－波节管传热性能的影响规律，为选用波节管作为传热器提供了节能和经济效益具佳的最佳风速。     

光管与波节管传热性能试验研究

本文对Hsn70-1A波节管与Hsn70-1A光管进行了不同风速下传热性能的对比试验研究。通过试验结果可以看出波节管的传热性能明显优于光管，本实验的风速范围0．8～8m／s。     

换热管内旋向自交叉转子强化传热性能研究

利用综合传热性能实验台,研究对比旋向自交叉转子、同向转子的换热器和光管的传热性能。结果发现:通过Webb性能比较方法,在同样面积和同等泵功率情况下,同向转子比光管换热器的换热量最大可提高为6.99%,而旋向自交叉转子比光管的换热量最大可提高8.11%,并计算推导了旋向自交叉转子与同向转子、光管之间的准则关联式;同时研究了换热量与转子外径的关系,结果发现换热量随转子外径变大而增多。     

圆形凸胞管内传热数值模拟及场协同分析

在普通光滑圆管基础上提出一种新型凸胞换热管,对凸胞管和光滑管的传热特性进行数值模拟,通过改变流速比较无量纲半径I、节距P、排布方式对换热性能的影响,应用场协同理论分析其强化传热机理。模拟结果表明:在所研究的雷诺数范围内,Nu随着无量纲半径I的增加而增加,综合换热性能PEC指数在Re=17 534、无量纲半径I=0.2时为最大;凸胞节距P对Nu的影响较弱,较小的凸胞节距其综合换热性能更优;凸胞对排流动阻力大,错排综合换热性能优于对排;从速度场、温度场分布及场协同原理分析凸胞换热管的强化传热机理。     

波壁管几何尺寸对流动与传热特性的影响

基于数值模拟的方法,分析在低雷诺数下波壁管波形变化对流体流动与传热特性的影响,并分析了相同功耗下波壁管的综合传热性能。结果表明:波幅和波长变化对波壁管传热均有影响,强化效果与波幅成正比,与波长成反比;当功耗相同时,小波幅的波壁管有较好的综合换热效果,大波幅的波壁管强化传热以较大能量消耗作为代价;雷诺数大于2 000时,增大波长能达到较好的综合换热效果。     

相变换热器烟气侧流动及传热特性的数值模拟

对壁温均匀的相变换热器换热管外烟气的流动状态与翅片管的换热过程进行数值模拟,分析烟气入口速度、翅片间距及翅片管横向间距、纵向间距对流动传热特性的影响。结果表明:随着烟气入口速度的增加,换热量和烟气流动阻力均增加;一定范围内增大翅片间距,能够强化传热性能,降低烟气流动阻力;翅片管横向间距的增大能强化传热,而纵向间距的增大会减弱传热性能,二者均能够降低烟气的流动阻力。     

纵向涡发生器几何参数对微通道流动传热特性的影响研究

为增强微通道的流动和换热特性,对微通道结合纵向涡发生器进行了数值模拟,分析不同雷诺数下纵向涡发生器的长度、横向间隙对微通道流动与换热性能指标的影响。结果表明:在进口速度为0.5～2 m/s时,雷诺数的增加会引起微通道内的换热性能增强,摩擦因子减小及综合传热性减小;涡发生器长度对换热影响较小,但增加涡发生器长度会引起阻力增加,横向间距对阻力影响较小,但增加横向间距会引起换热性能提高;涡发生器长度为0.30～0.40 mm时综合因子为0.94～1.21,横向间隙为0.1～0.5 mm时综合因子为0.88～1.17;纵向涡发生器长度为0.3 mm和横向间隙为0.5 mm时,有利于综合传热性能的提高。在低雷诺数时微通道结合纵向涡发生器的强化传热和综合传热因子要比高雷诺数时好。     

槽式太阳能DSG系统集热管内强化传热的数值模拟

为了强化集热管内蒸汽换热,避免管壁温度过高,对槽式太阳能直接产生蒸汽系统(DSG)采用内螺纹管和光管时过热段的传热及阻力特性进行了数值模拟,分析了螺纹高度、螺距和雷诺数对螺纹管内换热特性和流动阻力特性的影响,并与光管的数值模拟结果进行了比较.结果表明:内螺纹管增强了管内蒸汽扰动,提高了集热管换热性能,降低了管壁温度.螺纹管的努塞尔数Nu是光管的1.6～2.4倍,且螺纹高度越高、螺距越小,换热性能越好;螺纹管的阻力系数f是光管的3.1～8.7倍,且螺纹高度越高、螺距越小,f越大.     

多孔泡沫金属散热模型数值模拟与分析

多孔泡沫金属在紧凑型换热器领域具有广阔的应用前景。本文对具有随机结构的多孔介质中的流动和传热进行了耦合分析。采用有限元法研究了不同孔隙率(30%、50%、70%和90%)泡沫多孔材料的传热特性和阻力特性。利用 作为性能评价指标,即h越大,Δp越小,换热性能越好。通过改变孔隙度和入口流速从而分析整体的换热性能。结果表明,对于换热特性,泡沫金属的对流换热在高度方向上存在明显的温度梯度,边界层沿流动方向可以很好地发展,在高流速下具有更好地换热能力。随着孔隙率的增大,流体扰动变少从而局部速度将会减小,因此换热量也会降低。对于阻力特性,随着孔隙率的减小,内部压力显著增大,压力损失也显著变大。孔隙率为70%时,多孔泡沫金属具有更高的均匀性,同时通过实验验证了模型具有一定的有效性。     

板式空气_空气热交换器热工性能实验研究

本文以两台波纹铝板空气一空气热交换器为例,对其传热和阻力特性进行了实验研究,得出了雷诺数在900～4000范围内,传热因子j和平均摩擦阻力系数f随雷诺数的变化规律,并分析了热交换器结构和不同强化传热元件对其换热和阻力特性的影响。     

Turbulent heat transfer enhancement in a heat exchanger using helically corrugated tube

The augmentation of convective heat transfer in a single-phase turbulent flow by using helically corrugated tubes has been experimentally investigated. Effects of pitch-to-diameter ratio (P/D_H = 0.18, 0.22 and 0.27) and rib-height to diameter ratio (e/D_H = 0.02, 0.04 and 0.06) of helically corrugated tubes on the heat transfer enhancement, isothermal friction and thermal performance factor in a concentric tube heat exchanger are examined. The experiments were conducted over a wide range of turbulent fluid flow of Reynolds number from 5500 to 60,000 by employing water as the test fluid. Experimental results show that the heat transfer and thermal performance of the corrugated tube are considerably increased compared to those of the smooth tube. The mean increase in heat transfer rate is between 123% and 232% at the test range, depending on the rib height/pitch ratios and Reynolds number while the maximum thermal performance is found to be about 2.3 for using the corrugated tube with P/D_H = 0.27 and e/D_H = 0.06 at low Reynolds number. Also, the pressure loss result reveals that the average friction factor of the corrugated tube is in a range between 1.46 and 1.93 times over the smooth tube. In addition, correlations of the Nusselt number, friction factor and thermal performance factor in terms of pitch ratio (P/D_H), rib-height ratio (e/D_H), Reynolds number (Re), and Prandtl number (Pr) for the corrugated tube are determined, based on the curve fitting of the experimental data.     

工业供热中汽汽再热器换热强化数值研究

为了强化工业供热中的汽汽换热,通过CFD技术对不同类型换热管的流动及换热特性进行了研究。结果显示：光滑壁面时管壁两侧的高、低温蒸汽的温度梯度沿着流向逐渐变化,对流换热逐渐增强;相比于光滑管,采用内波节管和内螺纹波节管时,高温蒸汽侧的温度梯度增大,而低温蒸汽侧的壁面温度梯度明显增大;采用壁面异型结构能够改变管壁内温度梯度,采用内螺纹波节管尤甚。采用内波节管和内螺纹波节管的平均Nu相比于光滑管显著提高,最大值分别提高了26%和30%。     

Heat transfer augmentation in 3D internally finned and microfinned helical tube

Experiments are performed to investigate the single-phase flow and flow-boiling heat transfer augmentation in 3D internally finned and micro-finned helical tubes. The tests for single-phase flow heat transfer augmentation are carried out in helical tubes with a curvature of 0.0663 and a length of 1.15 m, and the examined range of the Reynolds number varies from 1000 to 8500. Within the applied range of Reynolds number, compared with the smooth helical tube, the average heat transfer augmentation ratio for the two finned tubes is 71% and 103%, but associated with a flow resistance increase of 90% and 140%, respectively. A higher fin height gives a higher heat transfer rate and a larger friction flow resistance. The tests for flow-boiling heat transfer are carried out in 3D internally micro-finned helical tube with a curvature of 0.0605 and a length of 0.668 m. Compared with that in the smooth helical tube, the boiling heat transfer coefficient in the 3D internally micro-finned helical tube is increased by 40-120% under varied mass flow rate and wall heat flux conditions, meanwhile, the flow resistance is increased by 18-119%, respectively.     

Numerical investigation for improved heat transfer characteristics in micro‐fin tubes

Generally, internal micro‐fin tubes are used for increasing the life and performance of electronic devices. The micro‐fins enhance the heat transfer rate by increasing the surface area with an increase of the pressure drop. In this study, heat transfer and pressure drop are analyzed by varying Reynolds number with the increase in the number of fins in tubes. Heat transfer and pressure drop, together with turbulence kinetic energy of micro‐fin tubes (helical and straight) and a smooth tube, have been evaluated for different Reynolds numbers (60 000, 40 000, 20 000, and 2000) at a constant temperature of 350 K, which clearly establishes laminar to turbulent flow. It is observed that the helical micro‐fin tube has a better result compared with the straight micro‐fin tube and smooth tube at Reynolds numbers 60 000, 40 000, and 20 000 at velocity 2, 1, and 0.5 m/s, respectively. This study is an attempt to establish a comparison of different micro‐fin geometries with varying Reynolds numbers, concluding that a high Reynolds number is suitable for the same.     

波纹管内流动与传热规律的数值计算

采用三维层流及低雷诺数湍流模型对波纹管内流动与传热性能进行了数值模拟,模拟结果与试验结果吻合良好.通过数值计算拓宽了波纹管流动与传热关联式的参数范围,发现在较大雷诺数(RP)范围内波纹管阻力系数随Re的变化趋势表现为指数规律.考察了不同波纹高度、波纹间距对流动与传热的影响,并对模型参数进行了综合性能评价,结果表明:波纹高度对波纹管内流动与传热的影响较波纹间距更显著;波纹管结构的强化传热性能只有在高Re条件下才得以体现,Re越大,波纹管综合性能因子也越高.通过数值计算得到了波纹管流动与传热的最优结构参数及最佳传热雷诺数范围.     

Thermal performance analysis of a tube finned surface

The present work submits an experimental work on the heat transfer and friction loss characteristic, employing a tube finned heating surface kept at a constant temperature in a rectangular channel. The tube fins attached on the surface (o.d.=29 mm) were arranged as either in‐line or staggered. The parameters for the study were Reynolds number (3700–30 000), depending on hydraulic diameter, the distance between the tube fins in the flow direction (S_y/D=1.72–3.45) and the fin arrangement. The change in the Nusselt number with these parameters was determined. For both tube fin arrangements, it was observed that increasing Reynolds number increased Nusselt number, and maximum heat transfer occurred at S_y/D=2.59. Thermal performances for both arrangements were also determined and compared with respect to heat transfer from the same surface without fins. With staggered array, a heat transfer enhancement up to 25 per cent for S_y/D=3.45 in staggered array was achieved in constant pumping power. Copyright © 2002 John Wiley & Sons, Ltd.     

Characterization of internal thermohydraulic flow and heat transfer improvement in a three-dimensional circular corrugated tube surfaces based on numerical simulation and design of experiment

To meet the requirements of development in heat exchangers design, the effect of different tubes geometrical parameters on its flow field analysis and thermal heat transfer performance are investigated in the current research work. The hydraulic thermal fluid coupling with computational simulations is applied. The numerical results are solving used flow transport and heat transfer equations, then these results are validated with available experimental data. The behavior of hydraulic and thermal flow in the corrugated tube is discussed with different geometrical parameters' position and shape. Turbulent flow in the tube is calculated in three-dimensional numerical simulations with optimization of a multiobjective algorithm are analyzed. The influences of various design parameters, for instance, the number of corrugated rings around the tube, distance between each corrugated ring, the diameter of the ring, and pitch of ring are investigated firstly in the flow field and then optimized by using the design of experiment (DOE). The influence of flow structural modifications such as static pressure, dynamic pressure, and pressure drop is taken into consideration as analyzed performance parameters. The DOE method is investigated based on implements and variances the L16 orthogonal arrays are chosen as the experimental strategy. Furthermore, the optimization results found that the maximum value of pressure difference was for corrugated diameter. The numerical method using DOE has enhanced heat transfer rate as compared to the smooth pipe. Moreover, the minimum T_out is for Case 11 (296.49°C) and the maximum T_out is for (303.10°C) hence the value of Nu number for both cases is 32.9 and 42, respectively. That means using this type of passive device can improve the heat transfer in the pipe. The outcomes illustrate that the performance evaluation factor (PEF) ratio of the corrugated pipe with different geometrical configurations is changed and increased as the corrugated pipe geometrically changed and the value of PEF is more than 1.3.     

新型横纹螺旋盘管强化传热的数值模拟

为了增强螺旋盘管的传热性能,对现有的普通螺旋盘管进行优化设计,提出一种管壁向内凸起形成环肋的异型管,称为横纹螺旋盘管。通过数值模拟方法对横纹螺旋盘管和普通盘管内部流动和传热过程进行模拟。应用场协同原理对其速度场和温度场的协同作用进行分析。实验数据与仿真结果的误差在5%以内,验证了数值模拟方法的正确性。在不同Re(雷诺数)条件下,计算两种盘管的Nu(努塞尔数),进而与Gnielinski(格尼林斯基)修正公式计算结果进行比较,误差在10%以内。结果表明:环肋结构通过工质旋转流动破坏边界层厚度,改善了管内速度场与温度场的协同程度,从而实现了强化传热。在较高的Re范围内,横纹螺旋盘管的Nu为普通盘管的1.29~1.43倍。因此,横纹螺旋盘管具有更好的传热性能,为异型螺旋盘管的研究及工程应用提供一定的理论依据。     

管内强化对流换热的热力经济性分析

鉴于管内换热和阻力同步增长的事实,依据Ｗｅｂｂ指标对管内强化对流换热方式下传热和流阻的综合热力性能进行了推导,得到了热力性能指标Ｑ／ＱＳ、Ｐ／ＰＳ和Ｆ／ＦＳ与管内对流换热努氏数Ｎｕ和管内阻力系数λ之间的函数关系式。在此基础上,对螺旋槽管强化管内换热的热力性能进行了分析。