换热管内插组合扭带强化传热的实验研究

以水为介质,对换热管内插入组合扭带的强化传热进行实验研究,分析其阻力和传热特性。实验结果表明,内插入组合扭带管的流动阻力和努塞尔数都得到了提高。其中,组合扭带管的摩擦系数比开孔扭带管的平均提高了10.5%;扭带管的努塞尔数比空管的平均提高了13.01%~20.38%,此外,组合扭带管的努塞尔数比开孔扭带管的平均提高了6.52%。换热管内插入组合扭带的传热综合性能评价因子φ均大于1,最大值达到1.16,这说明了换热管内插入组合扭带后,传热性能确实得到了提高。     

换热管内置开边槽扭带的阻力与传热特性研究＊

将21种不同结构参数的铝制扭带分别置入换热管进行冷态和热态实验,研究并分析了换热管内置开三角形边槽扭带的阻力和传热特性。实验结果表明,插入开边槽扭带后管内的流动阻力和传热系数都有较大的提高。通过多元线性回归分析,得到了相应的阻力系数关联式和换热系数关联式。由强化传热性能评价分析,得到评价因子φ=1．05～1．35,证明了所研究的扭带具有强化传热的应用价值。     

Φ42mm换热管内置铝制扭带强化传热特性的研究

对Ф42mm换热管插入扭带后的阻力特性和传热特性进行了分析,发现插入扭带以后,传热系数和流动阻力均增加,并且二者均随扭带的带宽增大而增大;通过非线性回归分析,得到插入铝制扭带后换热管摩擦阻力系数关联式和给热系数关联式;对插入扭带的换热管进行了强化传热性能评价分析,传热性能评价因子的数值在1．09～1．44范围之间,研究的扭带均具有强化传热的应用价值。     

Ф42mm换热管内置铝制扭带强化传热特性的研究

对Ф42mm换热管插入扭带后的阻力特性和传热特性进行了分析,发现插入扭带以后,传热系数和流动阻力均增加,并且二者均随扭带的带宽增大而增大;通过非线性回归分析,得到插入铝制扭带后换热管摩擦阻力系数关联式和给热系数关联式;对插入扭带的换热管进行了强化传热性能评价分析,传热性能评价因子的数值在1．09～1．44范围之间,研究的扭带均具有强化传热的应用价值。     

管内置梯形波带强化传热实验研究

设计了3种梯形波带内插件并对其强化换热特性进行实验研究,得出管内插入梯形波带扰流组件的传热系数h提高率为126%～220%,并对扰流组件引起的管程阻力进行了分析。通过传热性能评价准则(PEC)对插入梯形波带后的换热管进行传热的综合评价,证明梯形波带内插件确实是一种良好的加强换热能力的组件,并对实验数据线性回归拟合出了传热关系型。     

自旋扭带强化传热及旋转特性

旋转扭带是在固定式扭带基础上发展而来的, 因其特殊结构所以能在管内流体作用下产生自旋效果。本文对自旋式扭带旋转特性及强化传热特性进行研究。通过理论及实验研究管内自旋扭带旋转特性后得出:扭率越小, 扭带克服阻力起始旋转需要的流体速度越小;扭带转速与管内流体流速呈一次线性关系, 且扭带节距不变时线性比例基本保持不变。通过实验研究后得出:自旋扭带能达到很好的强化传热性能, 扭率越小其强化传热性能越明显, 同时阻力特性也越明显, 在雷诺数为4×10³～4×10⁴、扭率为3～8时, 换热管内摩擦因子增至1.7～3.5倍, 努赛尔数增幅为10%～37%。本文使用评估指标η对扭带进行综合评价, 得出扭率为7的自旋扭带具有最佳的综合性能。并分别拟合出摩擦因子及努赛尔数与雷诺数、扭率之间的关联式, 提出一种工程上自旋扭带选型方法。     

扭带结构影响管内传热与熵产的研究进展

随着工业技术不断发展,传统换热管的传热方式已经无法满足高热流密度下的热量输运要求。扭带插入物是一种能够有效提高换热管传热效率的强化传热元件,以其结构简单、加工容易的特点受到了很多学者的关注和研究。管内流体的传热性能及熵产往往作为评价换热管性能的重要参数,因此扭带结构与流动工质对这些参数的影响成为近年来研究的重点。本文主要综述了近十年来不同结构扭带对管内传热与熵产影响的研究进展。首先,将文献中研究的扭带按照几何结构进行分类,阐述和分析了不同类型扭带对换热管的传热、熵产以及综合性能的影响,试图找出几何结构与换热管传热性能以及熵产之间的联系。其次,介绍了扭带与纳米流体复合传热技术的研究进展。最后,归纳了研究人员为达到传热性能最大化以及熵产最小化而建立的传热和熵产模型,并对模型的优缺点进行了评价。     

含固体粒子旋转流强化流体传热的实验及模拟研究

针对管内除垢与防垢及强化传热问题,对工程上应用较广的扭曲管、扭带管中旋流场内低浓度液固流场综合性能进行实验及模拟研究. 结果表明,含粒子旋流场可提高流体湍流强度,与圆管相比,扭曲管和内插扭带圆管均有较好的旋流效果,相同Re下扭曲管的换热系数提高18.7%~30.1%,阻力系数提高13.1%~181.8%,综合性能评价因子平均提高15.5%,高于圆管和扭带管;而扭带管的换热系数比圆管提高5.6%~32.9%,阻力系数最高. 对扭曲管内粒子传热性能进一步优化,模拟值与实验值的误差为10.7%~12%. 旋流作用有利于提高液固流场的综合性能,但较高流速下该综合性能则逐渐降低.     

换热管内置开边槽扭带的阻力及转动特性研究

将18种不同结构参数的铝制扭带分别置入换热管进行实验,研究并分析了换热管内置开三角形边槽扭带的阻力和转动特性。实验结果表明,插入开边槽扭带后管内的流动阻力和转动性能都有较大的提高,扭带的扭转比Y、扭带宽度D和边槽结构是影响压降和转速的主要因素。通过多元线性回归分析,得到了相应的压降Δp关联式和转速n关联式。实验表明,开边槽结构具有强化扭带转动特性的应用价值。     

齿边穿孔扭带对管内强化传热的实验研究

研究新型扰流元件--齿边穿孔扭带插入换热管中强化传热的情况,考察影响传热效果的三个因素:孔径、孔距、扭矩。并通过对比实验,分析在换热管中分别插入齿边穿孔扭带、穿孔扭带与无孔扭带时,强化传热的效果。     

换热管内插入间隔自旋扭带流阻与传热特性的实验研究

通过实验研究了内置间隔自旋扭带的换热管的传热和流阻特性。实验结果表明,间隔扭带的换热系数和摩擦系数都低于全长扭带;扭转比越大,间距对换热管阻力和传热特性的影响越小。此外,作者还建立了包含间隔扭带结构参数在内的流阻与传热特性的经验关联式。     

Experimental studies on heat transfer and friction factor characteristics of turbulent flow through a circular tube fitted with helical screw-tape inserts

Experimental investigation of heat transfer and friction factor characteristics of circular tube fitted with full-length helical screw element of different twist ratio, and increasing and decreasing order of twist ratio set have been studied with uniform heat flux under turbulent flow conditions. The Reynolds number was varied from 2700 to 13 500. The experimental data obtained are compared with those obtained from plain tube published data. The maximum Nusselt number for the twist of 1.95 was obtained. The performance of the helical twist insert was compared with the twisted tape performance reported in the literature and found that it is better than twisted tape performance. The heat transfer augmentation for helical twist of increasing and decreasing order twist were also presented. The empirical correlations developed relating twist ratio and Reynolds number, are fitting the experimental data within ±13% and ±15% for Nusselt number and friction factor, respectively. The performance evaluation study has been presented to check the potential of using the helical twist insert.     

扭曲管强化传热性能实验研究

在设计的蒸汽-水换热实验台上测试了5种不同导程的椭圆扭曲管和圆管的传热和流动阻力性能.分别对5种不同导程的扭曲管和圆管管内流体努赛尔数,摩擦系数和管内综合评价因子随雷诺数变化情况进行了对比.实验结果表明:扭曲管的强化传热性能明显,且导程越小,强化传热效果越好.在实验测试的雷诺数范围内,扭曲管的努塞尔数为光滑圆管的1.0...     

INFLUENCE OF NONUNIFORM TWISTED TAPE ON HEAT TRANSFER ENHANCEMENT CHARACTERISTICS

An experimental study of heat transfer and friction factor characteristics in a circular tube fitted by twisted tapes with nonuniform twist ratios is reported. The twisted tapes are used as swirl generators playing roles as heat transfer enhancers. The nonuniform twisted tapes examined in the present work have (1) sequentially increasing twist ratios (SL), (2) sequentially decreasing twist ratios (LS), (3) repeatedly increasing-decreasing twist ratios (SL/SL), (4) repeatedly decreasing-increasing twist ratios (LS/LS), (5) intermittently increasing-decreasing twist ratios (SL→LS), and (6) intermittently decreasing-increasing twist ratios (LS→SL). In addition, three different typical twisted tapes with twist ratios of 3.0, 4.0, and 5.0 (TT) were also evaluated. Apparently, LS yields monotonically increasing swirling intensity and SL decreasing swirling intensity, resulting in lower heat transfer rate and friction factor than the other four nonuniform twisted tapes, which possess extra fluid fluctuation. However, among the tapes tested, the SL/SL offers the maximum thermal performance factor of around 1.03, which corresponds to Nusselt number of around 36% and friction factor of 3.57 times over those of the plain tube.     

插入双面有三角形翅片的金属带对热交换管中流动和传热特性的影响

The convective heat transfer and friction behaviors of turbulent tube flow through a straight tape with double-sided delta wings(T-W)have been studied experimentally.In the current work,the T-W formed on the tape was used as vortex generators for enhancing the heat transfer coefficient by breakdown of thermal boundary layer and by mixing of fluid flow in tubes.The T-W characteristics are(1)T-W with forward/backward-wing arrangement,(2)T-W with alternate axis(T-WA),(3)three wing-width ratios and(4)wing-pitch ratios.The experimental result reveals that for using the T-W,the increases in the mean Nusselt number(Nu)and friction factor are,respectively,up to 165%and 14.8 times of the plain tube and the maximum thermal performance factor is 1.19.It is also obvious that the T-W with forward-wing gives higher heat transfer rate than one with backward-wing around 7%. The present investigation also shows that the heat transfer rate and friction factor obtained from the T-WA is higher than that from the T-W.In addition,the flow pattern and temperature fields in the T-W tube with both backward and forward wings were also examined numerically.     

装填有矩形切口螺旋带的管中的湍动传热和压降(英文)

Heat transfer, friction factor and thermal enhancement factor characteristics of a double pipe heat exchanger fitted with square-cut twisted tapes (STT) and plain twisted tapes (PTT) are investigated experimentally using the water as working fluid. The tapes (STT and PTT) have three twist ratios ( , 4.4 and 6.0) and the Reynolds number ranges from 2000 to 12000. The experimental results reveal that heat transfer rate, friction factor and thermal enhancement factor in the tube equipped with STT are significantly higher than those fitted with PTT. The additional disturbance and secondary flow in the vicinity of the tube wall generated by STT are higher compared to that induced by the PTT is referred as the reason for better performance. Over the range considered, the Nusselt number, friction factor and thermal enhancement factor in a tube with STT are respectively, 1.03 to 1.14, 1.05 to 1.25 and 1.02 to 1.06 times of those in tube with PTT. An empirical correlation is also formulated to match with experimental data of Nusselt number and friction factor for STT and PTT.     

高黏介质中内插扭带对换热管换热性能影响

某石化公司炼油厂第二套常减压装置中换热器的热交换介质为高黏度的原油及其附属产品,在对流换热过程中传热系数低,动能消耗大。针对这一现状,本文设计了一种换热管内插间歇半扭带,利用计算流体力学软件Fluent对内插间歇半扭带换热管在实际工况下的换热过程进行数值模拟,与光滑管、内插连续扭带换热管进行了对比,并给出了间歇半扭带传热元件的优化设计参数。结果表明:内插间歇半扭带大幅提高了换热管内流体的努塞尔数Nu,同时也使换热管内摩擦阻力系数f增大;间歇半扭带换热管的换热效率η比内插连续扭带换热管提高8%~12%;当间歇半扭带的扭曲率y为10、连接杆长度s为345mm时,换热效率η最高,达到2.06。研究结果为该常减压装置换热器强化传热的研究提供了理论依据。     

内置交替轴扭带的管内层流换热特性

为了提高管内层流换热性能,开发了三种不同的交替轴扭带作为强化换热的扰流元件。通过数值模拟对内置这些扰流元件的管内换热与流动特性进行了研究,结果表明：（1）对于交替轴窄边扭带,在较低Reynolds数下Nusselt数随错位角的增大而增大;而Re较高时,错位角的影响较小。阻力系数f随错位角的变化不大,90°对应的综合性能指标PEC最高。（2）对于交替轴中空扭带,Nu在60°时达到最大值,f随错位角的增加而有较明显的增加,PEC在60°时最好。（3）对于交替轴窄边中空扭带,Re较低时,Nu随错位角增大而增加;而Re较高时,错位角的影响较小。f的最大值出现在错位角为60°时,但错位角的影响并不明显,而且比交替轴窄边扭带的f降低很多。90°错位角对应的PEC最好。（4）总体来看,采用交替轴窄边中空扭带能全面获得优良的热-水力学综合性能。