几何参数对层板冷却性能影响的数值模拟研究

对12种不同几何结构尺寸的层板进行了系统的耦合传热数值计算，研究了通道高度、扰流柱直径、孔间距与孔径比等几何参数对层板冷却效果的影响。结果表明，在相同的冷气密流条件下，减小通道高度可显著提高冷却效果，孔间距对冷却效果影响不大。这里的结果可为层板的优化设计提供参考。     

涡轮动叶表面气膜冷却换热实验研究

这里在大尺寸低速叶栅传热风洞中，对某型涡轮动叶表面有无气膜冷却的换热情况进行了详细的实验研究，实验结果表明，不同孔位出流的换热由于孔排下游表面来流速度及叶片表面曲率的不同而有着不同的规律，即主流雷诺数对叶片表面特别是压力面和前缘区域的换热系数比的影响较小，吹风比对换热系数影响较大，并且随气膜孔位置和来流雷诺数的变化而情况复杂。     

Effect of hole shape on the heat transfer in a rectangular duct with perforated blockage walls

Heat transfer coefficients were measured by the improved hue detection based liquid crystal technique in a turbine blade internal cooling passage model with blockage walls. In the experiments, blockages with 9 holes of circular, wide, narrow shapes were used and for the circular shape, the number of hole of 7, 9, and 11 were tested. For all cases, the perforated area was kept same. Results showed that the staggered impingement jets increased heat transfer coefficient, however, pressure drop also increased greatly. Generally, Nusselt number ratio and the thermal performance factor decreased as Reynolds number increased. For all Reynolds numbers tested, the blockage wall with wide holes gave more uniform heat transfer coefficient and higher thermal performance factor. As the number of hole increased from 7 to 11, the distribution of heat transfer coefficient became uniform and the thermal performance factor increased. This paper was presented at the 9^th Asian International Conference on Fluid Machinery (AICFM9), Jeju, Korea, October 16–19, 2007.     

液滴低温气体雾化射流冷却换热理论分析与实验研究

论述低温气体雾化射流冷却原理及特点,以池内膜态沸腾为基础,将喷雾颗粒的冲击作为一种扰动,建立雾滴射流进入切削区冷却高温壁面的模型,讨论雾滴冷却高温壁面的换热系数,着重探讨工艺参数水流密度对喷雾冷却换热系数的影响.进行了不同水剂量的低温气体雾化射流冷却钛合金高温壁面的瞬态实验,获得了钛合金试件表面温度分别为100℃、150℃、200℃和250℃时,低温气体雾化射流冷却达到最佳冷却效果时水剂量,分析了水剂量对冷却效果的理论依据,结果证实该模型对实际应用具有一定的指导作用.     

铸件和铸型间界面传热系数的试验研究

在铸造凝固过程的数值模拟中,铸件/铸型间的界面传热系数是非常关键的一个参数.为提高数值模拟精度,文中采用铝合金铸件设计了金属型铸造试验,考虑了铸型厚度对结果的影响,使用特制的热电偶采集了铸件内部不同位置的温度值.以此实测的温度场数据为基础,结合数值模拟技术和界面传热系数“反问题”的求法,得到界面传热系数与时间的函数关系.结果表明:铸型厚度不同会影响铸件铸型间的热流和界面传热系数的变化规律,且界面传热系数在铸件冷却中并非常数,随着凝固过程的继续而减小.最后将所得界面传热系数用于凝固过程的温度场模拟,与试验结果进行了对比分析,得到了合理的分布,说明此界面传热系数测定方法可行.     

塑料薄膜与流延辊换热过程的模拟分析

为实现流延辊辊面温度场的均匀性和稳定性,保证塑料薄膜的高质生产,应用F luent软件对双向回流式螺旋流道的流延辊的换热过程进行了数值模拟;分析了流延膜在流延辊上冷却时的导热、对流、辐射综合的非稳态传热过程,了解了流延膜冷却过程中的传热机理,得出了流延辊内部流道结构、冷却水的流量对流延辊换热强度的影响趋势。研究结果表明,该研究可以为流延辊结构的合理设计、流道参数的优化提供指导。     

Interfacial heat transfer coefficient between metal and die during high pressure die casting process of aluminum alloy

The present work focused on the determination of the interfacial heat transfer coefficient (IHTC) between metal and die during the high pressure die casting (HPDC) process. Experiments were carried out on an aluminum alloy, ADC12Z, using “step shape” casting—so-called because of its shape. The IHTC was successfully determined by solving one of the inverse heat problems using the nonlinear estimation method first used by Beck. The calculation results indicated that the IHTC immediately increased after liquid metal was brought into the cavity by the plunger and decreased as the solidification process of the liquid metal proceeded. The liquid metal eventually solidified completely, a condition when the IHTC tended to be stable. Casting thickness played an important role in affecting the IHTC between the metal and die not only in terms of its value but also in terms of its change tendency. Also, under the test conditions, different change tendencies of the metal solid fraction were found between castings with different thicknesses and the die. __________ Translated from Acta Metallurgica Sinica, 2007, 43(1): 103–106 [ 译自: 金属学报]     

Experimental measurement and numerical computation of the air side convective heat transfer coefficients in a plate fin-tube heat exchanger

The air-side forced convective heat transfer of a plate fin-tube heat exchanger is investigated by experimental measurement and numerical computation. The heat exchanger consists of a staggered arrangement of refrigerant pipes with a diameter of 10.2 mm and a fin pitch of 3.5 mm. In the experimental study, the forced convective heat transfer was measured at Reynolds numbers of 1082, 1397, 1486, 1591 and 1649 based on the diameter of the refrigerant piping and on the maximum velocity. The average Nusselt number for the convective heat transfer coefficient was also computed for the same Reynolds number by using the commercial software STAR-CD with the standard k - ɛ turbulent model. It was found that the relative errors of the average Nusselt numbers between the experimental and numerical data were less than 6 percent in a Reynolds number range of 1082∼1649. The errors between the experiment and other correlations from literature ranged from 7% to 32.4%. However, the literature correlation of Kim et al. is closest to the experimental data within a relative error of 7%. This paper was recommended for publication in revised form by Associate Editor Man-Yeong Ha Jin-Gi Paeng recieved a bachelor’s degree in Aero Mechanical Engineering from Gyeong-sang National University in 2000. He then went on to recieve his M.S. degrees from Changwon National University in 2004. Currently, he completed the doc-tor’s course and a doctoral dissertation in 2007 and 2008, respectively. He will take a doctorate in 2008.     

The study of cooling channel optimization in blast furnace cast steel stave based on heat transfer analysis

The three-dimensional heat transfer and thermal stress of a steel cooling stave in a blast furnace at Maanshan Iron and Steel Co. Ltd. are built. The temperature and thermal stress fields of cooling stave are calculated by using finite element method software ANSYS. The results show the rise in maximum temperature and thermal stress of the stave hot surface is not high when cooling pipe is replaced by cooling elliptical tube. Because of the decrease in the cross-sectional area for cooling elliptical tube, the thickness of the cooling stave is reduced and cooling water flow is saved. As a result, the iron-making cost can be reduced.     

叶片前缘气膜冷却数值模拟

为了研究叶片前缘区域的换热特性,采用非结构化网格和realizable紊流模型,求解三维N-S方程,对前缘带有一排冷气孔的涡轮叶片进行了换热特性的数值模拟.分析了不同动量比,湍流度,孔间距及径向角下冷气射流的运动规律,换热分布以及冷效分布特点.结果表明,当动量比Ⅰ大于1时,在相同孔型下,动量比越高,冷效越大.在相同动量比下,孔间距越小,冷效越大.但动量比,孔间距及径向角对换热系数影响不大.当湍流度增加时,换热系数增加而冷效降低.沿展向,气膜孔中心区域冷效较高,两孔之间区域较低;而换热系数则相反,气膜孔中心区域换热系数较小,两孔之间区域较大.     

R134a冷水机组用高效换热管的试验研究及应用

通过换热管测试台对A、B2种双侧强化蒸发管的换热性能进行了测试研究。研究结果显示：对于同一管型而言,在工况不变的情况下,管内流速在1．0-2．0m／s时,换热管的综合换热系数会随着管内水流速的增加而呈上升趋势：两者的综合换热系数与其外齿周向齿数和轴向齿数有很大关系,外内齿数多综合换热系数高：新开发的高效换热蒸发管-B比原仃的蒸发管-A换热性能高6．6％。通过采用新开发的高效蒸发管-B每年可为公司节省成本约256．6余万元。     

Heat/mass transfer characteristics in the near-tip region on a turbine blade surface under combustor-level high inlet turbulence

Heat/mass transfer characteristics on the near-tip blade surface under combustor-level high inlet turbulence have been investigated within a high-turning turbine rotor passage by using the naphthalene sublimation technique. The inlet turbulence intensity and length scale are 14.7% and 80 mm, respectively. The tip gap-to-chord ratio is changed to beh/c = 0.74, 1.47, and 2.94 percents. Increasingh/c results not only in higher heat/mass transfer in the pressure-side tip region but also in more convective transport on the pressure surface even far away from the tip edge. Severe heat/mass transfer is always observed in the suction-side tip-leakage flow region which can be divided into two distinct high transport regions. There is a local maximum of heat/mass transfer along the trailing-edge centerline. This arises from the interaction of a tip-leakage vortex with a trailing-edge vortex shedding. Comparisons of the present data forh/c = 2.94 percents with the previous low turbulence one show that there is a large discrepancy of heat/mass transfer in the pressure-side near-tip area, which diminishes with departing from the tip edge. The suction-side heat/mass transfer in the tip-leakage flow region is less influenced by the high inlet turbulence than that at the mid-span. The leading-edge heat/mass transfer under the high inlet turbulence is always higher than that in the low turbulence case, while there is no big difference in the trailing-edge heat/mass transfer between the two cases.     

Analysis of conjugate heat transfer and turbulent flow in mechanical seals

A numerical investigation of conjugate heat transfer of turbulent flow within a mechanical seal chamber is presented. The computational model takes into account the heat generation at the contact interface between the rotating ring and the stationary ring, heat conduction into the rings, and heat convection into the surrounding fluid in the chamber. Correlations are developed for predicting the average heat transfer coefficient on the wetted outer surfaces of the seal rings assuming that the flow in the seal chamber is turbulent.     

凸轮磨削中热耗的分析与研究

磨削过程中产生的大量磨削热聚集在凸轮表面产生很大的温度梯度,降低了凸轮的加工质量和加工精度。文中分析了冷却液和空气在凸轮磨削中的冷却效果,提出了增强冷却液冷却效果和空气换热效果来降低凸轮磨削中的高温损伤的方法。     

中冷器冷却扁管管内传热及流阻性能研究

为解决汽车空-空中冷器冷却扁管最优换热性能的问题,运用FLUENT软件,建立了4种不同断面结构的冷却扁管导热和管内流动换热耦合数学模型,采用CFD方法对该传热问题进行了数值模拟计算.将数值计算的传热努塞尔特数与Gnielinski传热关联式、摩擦因子f与Webb实验关联式、Filonenko经验公式、Blasius关联式进行了对比;良好的结果吻合性验证了数值计算方法的正确性;通过4种冷却扁管换热因子j和流动摩擦因子f的对比分析,提出了冷却扁管综合性能的评价方法(jlf)1/3.研究结果表明,采用无量纲因子(jlf)1/3方法评价口琴式冷却扁管具有最优换热性能,斜撑式冷却扁管次之,从而可为汽车空-空中冷器结构设计或匹配选型提供重要的理论依据.     

逆流冷凝塔热泵系统热质交换过程数值模拟研究

冷凝塔作为冷凝式热泵系统的重要组成部分,其热质交换过程对于降低能耗及热泵系统设计具有重要意义.以逆流冷凝塔热泵系统形式为基础,通过建立冷凝塔内热质交换过程的数学模型,推导出热质交换过程的通用计算方程组,并以贵阳地区的气象参数为参考,对不同工况下塔内热质交换情况进行模拟计算及具体分析.研究结果表明,不同入口空气参数对溶液...     

波纹管内流动与换热的数值模拟研究

利用计算流体力学软件Fluent,采用数值模拟方法究了幅值不同的两种波纹管传热状况,发现幅值为4mm的波纹管的传热状况优于幅值3mm波纹管的传热状况,这是由前者管内湍流强度高于后者所致.同时,回归了两波纹管的换热准则方程,为波纹管的校核计算及工程应用提供依据.     

Measurement and correlation of boiling heat transfer coefficient of R-1234yf in horizontal small tubes

We report experimental data of boiling heat transfer of R-1234yf in horizontal small tubes. The experimental data obtained in the horizontal circular small tubes of 1.5 and 3.0 mm inner diameter, the lengths of 1000 and 2000 mm, the mass flux range from 200–650 kg/m²s, the heat flux range from 5–40 kW/m² and saturation temperature of 10 and 15°C, was used to develop a modified correlation for the heat transfer coefficient. The flow pattern of the experimental data was mapped and analyzed with existing flow pattern maps. The heat transfer coefficient was also compared with some well-known correlations.     

Nanofluids transport model based on Fokker-Planck equation and the convection heat transfer calculation

In current research about nanofluid convection heat transfer, random motion of nanoparticles in the liquid distribution problem mostly was not considered. In order to study on the distribution of nanoparticles in liquid, nanofluid transport model in pipe is established by using the continuity equation, momentum equation and Fokker-Planck equation. The velocity distribution and the nanoparticles distribution in liquid are obtained by numerical calculation, and the effect of particle size and particle volume fraction on convection heat transfer coefficient of nanofluids is analyzed. The result shows that in high volume fraction （ 0 _-- 0.8% ）, the velocity distribution of nanofluids characterizes as a ＂cork-shaped＂ structure, which is significantly different from viscous fluid with a parabolic distribution. The convection heat transfer coefficient increases while the particle size of nanoparticle in nanofluids decreases. And the convection heat transfer coefficient of nanofluids is in good agreement with the experimental result both in low （0 ~〈 0.1% ） and high （ q = 0.6% ） volume fractions. In presented model, Brown motion, the effect of interactions between nanoparticles and fluid coupling, is also considered, but any phenomenological parameter is not introduced. Nanoparticles in liquid transport distribution can be quantitatively calculated by this model.     

斜截半椭圆柱面涡发生器在管道中的传热数值模拟研究

管内设置一种斜截半椭圆柱面涡发生器,利用计算软件F luent进行数值模拟研究,研究以烟气为加热介质,冷空气为冷却介质的换热方式在不同Re数下不同攻角和倾角的传热及阻力特性,并与光管进行了对比。结果表明:斜截半椭圆柱面涡发生器能明显提高换热性能,在所研究的纵向涡发生器中,攻角为60°,倾角为15°时,涡发生器强化传热综合效果最佳。