超临界CO2螺旋槽管内冷却换热特性的数值模拟及实验研究

为了研究超临界CO₂螺旋槽管内的流动换热特性,本文首先在入口温度323.15 K、入口压力8.0 MPa、入口雷诺数35 000、总热量4 200 W的条件下对不同结构参数的螺旋槽管进行了数值计算,分析了各参数对换热系数及流动过程的影响,并根据换热评价因子,得到了最优螺旋槽管结构（管槽半径r₁为6.5 mm,管槽圆角r₂半径为2.0 mm,管槽槽深e₁为5.5 mm,套管间距e₂为1.0 mm,螺旋角w为0.70 rad）。在此基础上,实验研究了不同压力、不同入口雷诺数对换热系数的影响,得出其影响机理。分析换热系数的影响因素,并结合数值计算和实验数据,建立了超临界CO₂螺旋槽管内冷却换热关联式,并对实验数据进行了预测计算。结果表明,预测值与实验值的平均绝对值偏差为11.65%,最大绝对值偏差不超过25%,证明了其具有较好的准确性。     

不锈钢螺旋槽管水平强化传热的实验研究

本文对低导热系数的水平不锈钢螺旋槽管进行了凝结换热实验研究，并对不锈钢管的壁温测量进行了探索，通过分析得到了水平单头不锈钢螺旋槽管的水测对流换热系数准则方程。     

基于Fluent螺旋槽管的传热特性数值模拟

根据螺旋槽管的结构特点及传热特性,建立了三种不同槽口形状的螺旋槽管与光滑管换热器的三维模型。以水为工质,运用 Fluent流体分析软件,采用k-ε湍流模型,研究了三种不同槽口形状的螺旋槽管与光滑管换热器在换热过程中的速度场和温度场,得到了不同槽口形状和光滑管的壁面Nusselt数。结果表明。在相同壳程和雷诺数的情况下,螺旋槽管比光滑管的换热能力提高了6．7％-37．6%,其中三角彤槽和矩形槽螺旋槽管的换热能力提高最大,从而强化了传热。为谊产品的理论进一步研究和实验研究奠定了基础,为谊产品的设计和推广应用提供了依据。     

螺旋槽管传热与污垢性能的实验研究

进行了螺旋槽管的传热性能实验，得出了螺旋槽管管内强制对流换热关联式。以硬度800mg／L的人工硬水作为工质，在0．24m／s，管外水浴60℃和相同管内工质入口温度的条件下，进行了螺旋槽管及其对应光管管内污垢的对比实验。结果表明，螺旋槽管有较好的传热性能，但阻垢性能却弱于光管。     

凝结换热下螺旋槽管特性及其节能

本文介绍了凝结换热条件下螺旋槽管特性及试验研究结果，列举了螺旋槽管凝结加热器的应用及其节能效果。     

强化管内沸腾换热实验研究

主要研究在低过热度下微槽对流动沸腾换热特性的影响,分别以单工质甲醇和甲醇与甲苯的混合物为工质对不同流量情况下光管、直槽管和螺旋槽管的流动沸腾换热特性进行了实验研究。研究结果表明：对单工质甲醇来说,螺旋槽管可以明显起到强化传热作用,而且流量越低,强化传热效果越明显。对混合工质来说,当流量较低时,螺旋槽管强化传热效果不明显,而在流量较高时,强化传热效果比较明显。无论是单工质还是混合工质,直槽管在实验所能达到的壁面温度条件下不能起到明显的强化传热效果。还给出了螺旋槽管强化传热的定性解释。     

空气横掠顺列螺旋槽管和光管管束的传热特性

以横向管距、纵向管距以及管子的几何参数为研究对象，对顺列光管和螺旋槽管管束进行了横向冲刷换热及阻力试验研究，得出了换热和阻力关联式，为顺列布置的卧式螺旋槽管空气预热器的应用，尤其是为循环流化床锅炉的空气预热器提供了设计依据。图11表2参8     

在第二类吸收式热泵中对螺旋槽管的换热性能研究

为了提高在以溴化锂为工质的第二类吸收式热泵吸收器的性能,在第二类吸收式热泵吸收器内对不锈钢螺旋槽管,即不锈钢光滑管的传热传质性能进行了实验研究.发现螺旋槽管的传热传质性能约为光滑管3倍,螺旋槽管内热媒工质-水的流体阻力系数是光滑管的17～20倍;应用于第二类吸收式热泵中间大大降低换热面积,促进热泵的高效紧凑化.     

汽轮发电机定子水冷器传热与阻力特性的实验研究

为实现汽轮发电机定子水冷器的优化设计，以折流栅-螺旋槽管为强化换热元件，对水冷器进行了传热和阻力特性模化实验研究。获得了管、壳程流速及折流栅间距对传热和阻力特性的影响规律，并采用壳程单位压降的传热系数K／△P。对水冷器综合性能作了评价，将实验结果与前人研究成果作了比较。     

高压给水加热器采用小螺旋角的内外螺旋三角翅片管强化传热的试验研究

通过确切了解电站高压加热器的传热性能和特殊的设备要求，设计并加工出小螺旋角的内外螺旋三角翅片管用于强化其传热性能。基础实验表明，在实验的条件下，立式小螺旋角的内外螺旋三角翅片管的总传热系数比光滑管提高６３％－９５％，其中管外冷凝换热系数是同条件下光滑管的３．５－４倍，管内的对流换热系数也比光滑管提高了１８％。同螺旋槽等比较可知，立式小螺旋角的内餐螺旋三角翅片管的总换热系数比螺旋槽提高４％－２７％，     

螺纹槽管错排管束的传热特性及流动阻力特性研究

1引言近年来,随着市场经济的发展,换热设备迫切需要节约能源、节省材料和降低成本的优化设计,因此强化传热技术受到了国内外的广泛重视。螺纹槽管是一种有效的强化换热管型,由于螺纹槽管的粗糙表面,可以有效地防止烟气在管内积灰而造成换热能力的下降,可以提高壁温以避免低温腐     

Experimental studies on heat transfer enhancement of the inside and outside spirally triangle finned tube with small spiral angles for high‐pressure preheaters

A new heat transfer enhanced tube—the inside and outside spirally triangle finned tube with small spiral angles (IOSTF tube)—was developed and manufactured for improving the performance of high‐pressure preheaters. The triangle flutes with small spiral angle on the outside surface of the IOSTF tube perform like the vertically fluted tube, and the triangle flutes with small spiral angle on the inside surface of the IOSTF tube perform like the spirally fluted tube. The experiments show that the total heat transfer coefficient of the vertical IOSTF tube is 63–95 per cent larger than that of the smooth tube with only a slight increase in the inside flowing friction and the field results show that a 43 per cent increase in the total heat transfer coefficient of the high‐pressure preheater with the IOSTF tubes can be obtained. Copyright © 2000 John Wiley & Sons, Ltd.     

螺旋槽管凝结换热器的研究与应用

通过对螺旋槽管凝结换热器的试验研究,得到了螺旋槽管涉及相变时管内对流换热、管外凝结换热准则关联式以及管内流动阻力关联式,并依据试验结果,将螺旋槽管应用于电站凝结换热器,取得了满意的效果。     

A geometric study on shell side heat transfer and flow resistance of a six-start spirally corrugated tube

Heat transfer enhancement is of great importance for energy efficiency improvement. The utilization of spirally corrugated tubes is one of the efficient ways to strengthen heat transfer. In this article, based on a validated numerical model, the effects of geometric parameters of a six-start spirally corrugated tube, including the pitch p and the corrugation depth e, on the shell side heat transfer and flow resistance performance are numerically investigated, in high Reynolds number conditions ranging from 10,000 to 60,000. The shell side secondary flow velocity distribution, longitudinal vortex distribution, and temperature distribution of a six-start spirally corrugated tube are presented, respectively. In addition, the heat transfer and flow resistance characteristics are evaluated by comparing the Nusselt number and the flow resistance coefficient with these of smooth tubes. Results show that the utilization of six-start spirally corrugated tubes can enhance the heat transfer performance at the expense of an increase of the flow resistance. However, with the same geometric parameters, the Nusselt number increases and the flow resistance coefficient decreases as Reynolds number increases. With the pitch increasing, the Nusselt number and the flow resistance coefficient decrease at a fixed Reynolds number. In contrast, as the corrugation depth increasing, the Nusselt number changes irregularly, and the flow resistance coefficient increases. Finally, correlations for the shell side Nusselt number and flow resistance coefficient of the six-start spirally corrugated tube are established. This work is of significance for engineers and scientists focusing on the heat transfer and the flow resistance characteristics of spirally corrugated tubes and their applications.     

Experimental Investigation of Frictional Pressure Drop for Two-Phase Flow Inside Spirally Fluted Tubes

This article reports the results of an experimental study of frictional pressure drop for two-phase flow (air and water) inside horizontal spirally fluted tubes. Nine spirally fluted tubes, representing a wide range of geometric parameters, were tested adiabatically with various flow rates of air and water. Average pressure drop enhancement levels (over predicted smooth tube values) in the range of 1,4 to 3.9 were observed. A design correlation was developed based on modifications to an existing smooth-tube model. The proposed correlation predicts 84% of the database (581 experiment data points) within ±20%.     

水平螺旋槽管降膜流动和传热特性研究

对水平螺旋槽管壁面降膜形成及传热特性进行了理论和实验研究,得到了液膜厚度及速度的解析及数值解.结果表明,降膜液膜特性主要受槽道结构和液膜表面张力控制.管壁温度沿周向向下逐渐升高,而且在定热流密度下保持不变,而液膜温度则沿周向逐渐上升.相比光管,螺旋槽管降膜具有更高的传热系数.     

Effect of helix angle of spirally corrugated tube on condensation heat transfer characteristics

Spirally corrugated tubes with different helix angles have been used in experiments on the characteristics of condensation heat transfer and flow resistance. The result of the experimentation shows that the helix angle plays a vital part in the spirally corrugated tube during the process of condensation heat transfer. This paper analyzes the mechanism of how the helix angle influences the characteristics of condensation heat transfer and flow resistance, and presents an experimental correlation formula of condensation heat transfer which takes the helix angle into account as a factor. ©2008 Wiley Periodicals, Inc. Heat Trans Asian Res, 37(5): 275–282, 2008; Published online in Wiley InterScience ( www.interscience.wiley.com ). DOI 10.1002/htj.20208     

Heat Transfer Coefficient and Friction Factor Prediction of Corrugated Tubes Combined With Twisted Tape Inserts Using Artificial Neural Network

In the research described here, artificial neural network (ANN) approach has been utilized to characterize the thermohydraulic behavior of corrugated tubes combined with twisted tape inserts in a turbulent flow regime. The experimental data sets were extracted from 57 tubes, 9 and 3 spirally corrugated tubes with varying geometries combined with 5 and 4 twisted tapes with different pitches. The tests were carried out with Reynolds numbers ranging from 3000 to 60,000. The experimental data sets have been utilized in training and validation of the ANN in order to predict the heat transfer coefficients and friction factors inside the corrugated tubes combined with twisted tape inserts, and the results were compared to the experimental data. The mean relative errors between the predicted results and experimental data were less than 2.9% for the heat transfer coefficients and less than 0.36% for the friction factor. The performance of the neural networks was found to be superior in comparison with the models correlated in the form of mathematical functions with their own assumptions. The results of this study suggested that ANN can be considered as a powerful tool and can be easily utilized to predict the performance of thermal systems in engineering applications.     

光管内插入扭带传热与流动阻力的试验研究

为了研究管内强化换热技术,对三根不同结构参数的扭带插入光管的换热特性和流体动力学特性进行了试验研究。试验以空气为工质,Re在8000～10^5之间,管外被水冷却。对大量实验数据用多元线性回归法得到了具有较高精度的扭带管的传热系数和摩擦系数的统计关联式,分析了扭带管的传热与流阻性能,为换热器的设计及改造提供了理论依据。     

Effect of outline curvature degree on heat transfer and flow characteristics inside dimpled tubes and spirally grooved tubes

The flow behaviors and heat transfer characteristics have been studied inside the dimpled tubes and spirally grooved tubes with different curvature degrees, which is considered for the first time within the influence factors. A three-dimensional numerical simulation by periodic boundary conditions is performed to model the fully developed flow of dimpled and grooved sections to acquire the finer mesh and more accurate results. In addition, the dimple and groove outlines with different curvature degrees are generated by polynomial functions. Effects of curvature degrees for dimpled tubes and spirally grooved tubes on flow, heat transfer, and comprehensive performances are discussed. The results indicate that the influence of curvature degrees for dimpled tubes exhibit an opposite behavior when compared with those for spirally grooved tubes. On the whole, all performance factors increase with the growing curvature degree for dimpled tubes but decrease with the increasing curvature degree for spirally grooved tubes. By comparing different curvature degrees, the maximum ranges of heat transfer enhancement are 1.50–2.22 and 2.54–2.82, respectively, for dimpled and grooved tubes with respect to Re. Thermal and hydraulic fields are considered to analyze the mechanism of heat transfer enhancement. The analysis shows that the way the dimple changes thermohydraulic properties differs from the way the groove changes the properties.