导热油管内强制对流换热系数的计算

以一种常见导热油为例对有机热载体锅炉的对流受热面传热系数进行计算分析。     

Modeling of Heat Transfer Across the Interface in Two-Fluid Flows

A model is presented in this article to deal with heat transfer across the interface separating two immiscible fluids. It is suitable to be incorporated into interface-tracking methods, such as volume-of-fluid (VOF) methods, because a sharp interface is available in these approaches. The temperature at the interface and the heat flux through it are calculated in such a way that the continuity of the two properties at the contact surface is satisfied explicitly. With use of these values, the temperature either at the centroid or on a face of the interface cell can be estimated, which serves as Dirichlet boundary condition for the energy equation. The temperature field is then calculated by solving the energy equations for the two fluids simultaneously in an implicit way. This method is first assessed via testing on two heat conduction problems in which two solids are in contact. Good agreement between numerical solutions and theory is obtained. To demonstrate its capability, it is applied to two kinds of heat transfer problems, one being the collapse of a heated water column in a cavity, and the other the falling of a molten tin droplet in an oil tank. The effect of fluid flow on the heat transfer is clearly illustrated.     

Coupled Conduction and Intermittent Convective Heat Transfer from a Buried Pipe

An accurate estimate of the heat transfer from a buried pipe to the surrounding ground is essential for the design of the ground-loop portion of a ground-source heat pump. Exact analytical solutions to this problem are complicated by the fact that heat pump systems rarely operate continuously. Complete numerical simulations of system designs can be carried out, but these are unwieldy and difficult to justify for initial scoping calculations, or for preliminary performance estimates. The purpose of this article is to provide insight into the heat transfer mechanisms and to describe the development of simple algebraic correlations that can be used to approximate the intermittent overall heat transfer between a fluid flowing in an isolated buried pipe and the surrounding ground. The correlations described in this article were drawn from results of a numerical finite-difference analysis of a fluid flowing intermittently in a single round pipe and exchanging heat with the surrounding ground. It is found that the cycle average heat transfer is always lower for the intermittent case than for the continuous case, but that the average over just the active part of the cycle is always higher for any intermittent case than for the continuous case. The effect of the ground thermal diffusivity is largest when the heat transfer coefficient is large, and decreases with decreasing heat transfer coefficient. The range of heat transfer coefficients where isothermal wall conditions are approached is illustrated. Correlations for the operating average and cycle average total heat transfer are presented as functions of the thermal diffusivity, intermittence factor, and heat transfer coefficient.     

Methodology for Estimation of Local Convective Heat Transfer Coefficient for Vapor Condensation

This paper aims to present an effective two-dimensional inverse heat conduction technique and an experimental design for accurately estimating the local convective heat transfer coefficient of vapor condensation over a conical surface, given temperature measurements at some interior locations. The functional form for the heat transfer coefficient is not known a priori. The method uses a sequential procedure together with Beck's function specification approach. Solution accuracy and the effects of experimental errors are examined using simulated temperature data. It is concluded that a good estimation of space-variable heat transfer coefficient can be made from the knowledge of transient temperature recordings using the proposed inverse heat conduction problem method. The method is also used in a series of numerical experiments to provide the optimum experimental design for condensation heat transfer investigation.     

联合循环余热锅炉螺旋鳍片管烟气放热系数研究

东南大学建造了1座IGCC余热锅炉鳍片管受热面流动和传热热态试验装置,并先后在其上进行了2个不同螺旋鳍片管组的传热特性研究,通过分析比较实测的烟气侧对流放热系数与无量纲准则式计算的结果,得出了完全热模拟公式更为准确的结论。     

基于遗传算法的交错波纹板换热器表面传热系数的分离

为了获得交错波纹板换热器表面对流换热规律,通过实验测定了典型100 kW微型燃气轮机交错波纹板换热器的传热系数,提出了采用遗传算法将表面传热系数从传热系数中分离出来的方法.该方法以换热准则关系式中4个系数变量作为待寻找最佳值的待求变量,并进行搜索和优化,由此获得关联式系数来预测传热系数,成功分离出表面传热系数.该分离方法具有通用性,可灵活方便地研究各种此类换热器的传热性能.所预测的传热系数与实验获得的传热系数接近,能准确地反映换热的真实规律.     

Modeling for Shell-Side Heat Transfer Coefficient and Pressure Drop of Helical Baffle Heat Exchangers

This study has suitably modified the existing heat transfer and pressure drop correction factors of the modified Bell–Delaware method used for heat exchangers with segmental baffles, taking into consideration the helical baffle geometry. These correction factors are presented in parametric formulas based on the Taborek presented procedure for segmental baffles. These formulas are functions of the geometrical and physical parameters of discontinuous helical baffles. In addition, the parametric formulas are presented graphically based on the Stehlik method. The correction design method proposed by Stehlik for the helical baffle is presented in detail and a theoretical model for shell-side heat transfer and pressure drop is developed. In general, the results show that the present model matches more closely with the graphically proposed correction factors of Stehlik. In order to calculate the shell-side heat transfer coefficient and pressure drop using the present method, a computational code has been developed by the authors. In addition, in order to examine the validity, the results of the code for a case study are compared with the results obtained from EXPRESS software and experimental formulas presented by Zhang. The results of comparison show that the proposed method is accurate and can be used by designers confidently.     

Convective Heat Transfer Coefficients in Concentric Annuli

Abstract

The geometric shape of a passage's cross-section has an effect on its convective heat transfer capabilities. For concentric annuli, the diameter ratio of the annular space plays an important role. The purpose of this study was to determine to what extent research has been done on convective heat transfer in smooth concentric annuli and, if possible, to improve on or contribute to existing theories. It was found that although various correlations exist, they are not in good agreement. For this study, experiments were conducted with a wide range of annular diameter ratios. The Wilson plot method was used to develop a convective heat transfer correlation for annular diameter ratios of 1.7 to 3.2. For Reynolds numbers (based on the hydraulic diameter), in the range of 4000 to 30000, the deduced correlation predicted Nusselt numbers accurately within 3% of experimental values.     

Heat Transfer Coefficient Correlation for Convective Boiling Inside Plain and Microfin Tubes Using Genetic Algorithms

Two-phase flow heat transfer has been exhaustively studied in recent years. However, in this field, several questions remain unanswered. Heat transfer coefficient prediction related to nucleate and convective boiling has been studied using different approaches—numerical, analytical, and experimental. In this study, an experimental analysis, data representation, and heat transfer coefficient prediction of two-phase heat transfer in nucleate and convective boiling are presented. An empirical correlation is obtained, based on a genetic algorithms search engine, of a dimensional analysis of the two-phase flow heat transfer problem.     

Mathematical Modeling of Heat and Mass Transfer during Convective Dehydration of an Anisotropic Cylindrical Foodstuff

Two‐dimensional, unsteady‐state mass transfer was studied for air drying of an anisotropic finite cylindrical body. A mathematical model was developed for predicting the temperature of the drying sample at any time and moisture in any position in the drying sample at any time. The anisotropic nature of the drying material was considered in the mathematical model by taking into account the different moisture diffusivities in the axial and radial directions. A cut fresh green bean was used as an anisotropic material and a pilot‐scaled dryer was set up to investigate the drying behavior of this foodstuff. Several length‐to‐diameter ratios of fresh green beans were considered and the mathematical model was validated by comparison of the predicted values of average moisture content with the experimental data. The model was used to predict the moisture distributions inside the drying samples. Different moisture content distributions in the axial and radial directions during drying confirms the anisotropic nature of cut green bean samples. © 2013 Wiley Periodicals, Inc. Heat Trans Asian Res; Published online in Wiley Online Library ( wileyonlinelibrary.com/journal/htj ). DOI 10.1002/htj.21119     

Free Convective Heat Transfer in Tilted Longitudinal Open Cavity

Heat transfer experiments were performed to investigate the effects of inclination and channel height-to-gap ratio on free convection in a simulated fin-passage with a strategic aim of devising a criterion for selecting the optimal fin length that could provide the maximum free convective capability. The ranges of parameters investigated include the Grashof number, up to 500,000; channel height-to-gap ratios of 1, 2, and 3; and tilt angles of 0°, 30°, 60°, 90°, 120°, 150°, and 180°. Selections of local and spatially averaged Nusselt number results demonstrate the manner by which the Grashof number, tilt angle, and channel height-to-gap ratio interactively affect the heat transfer. In conformity with the experimentally revealed heat transfer physics, the correlation of a spatially-averaged Nusselt number over two parallel walls and the bottom surface of an open-ended channel is derived that permits the individual and interactive effects of the Grashof number, tilt angle, and channel height-to-gap ratio on heat transfers to be evaluated. A criterion for selecting the optimal height-to-gap ratio of the fin channel is subsequently formulated as a design tool for maximizing the convective capability of a free convective fin assembly.     

填充床内对流换热的数值研究

为研究空气流入高温填充床时小球直径和空气流速变化对填充床内对流换热和压力损失等的影响,利用孔隙尺度介观方法对顺序排列多孔介质小球的三维填充床进行数值计算,数值计算与实验结果吻合较好。结果表明:填充床内固相和气相间存在热的非平衡性;当小球直径从2.8增大到5.6 mm时,在最高温度上游对流换热强度减小,在最高温度下游对流换热强度增大,同时,压力损失和最大无量纲速度减小;气体流速增大时,填充床内产生湍流运动。     

对流传热计算中的烟气辐射放热系数α_1

本文提出锅炉对流传热计算中用到的烟气辐射放热系数α_(?)袭用炉内辐射传热的计算公式有误差,因为所对应的温压不同,应予改正。     

Heat Transfer Characteristics of Gaseous Flows in Micro-Channel with Negative Heat Flux

Two-dimensional compressible momentum and energy equations are solved to obtain the heat transfer characteristics of gaseous flows in micro-channels with constant heat flux for which the value is negative for no-slip flow. The numerical methodology is based on the Arbitrary-Lagrangian-Eulerian method. The computations are performed for channels with constant heat flux ranging from ?10⁴ to ?10² W/m². The channel height ranges from 10 to 100 μ m and the aspect ratio of the channel height and length is 200. The stagnation pressure is chosen such that the exit Mach number ranges from 0.1 to 0.7. The outlet pressure is fixed at the atmosphere. The wall and bulk temperatures in micro-channels with negative heat flux are compared with those of positive heat flux cases obtained in our previous work and also those of the incompressible flow in a conventional sized channel. In the case of fast flow, temperatures normalized by heat flux have different trends whether heat flux value is positive or negative. A correlation for the prediction of the wall temperature of the gaseous flow in the micro-channel is proposed. The rarefaction effect is investigated for the cases of channel height of 10 μ m with slip boundary conditions. The magnitudes of viscous dissipation term and compressibility term are also investigated. The effect of each term on heat transfer characteristics is discussed.     

Numerical Study of Nanofluid Convective Heat Transfer in Sinusoidal Tubes

ABSTRACT

The waviness of tube wall and adding nanoparticles to fluid as two passive enhanced heat-transfer techniques are dully accepted; however, the combined effect of their simultaneous usage has not been dealt with, yet. Therefore in the present study, the convective heat transfer of nanofluid laminar flow inside straight tube and sinusoidal tubes under constant heat flux boundary condition was documented. The nanofluid used in this study was Al₂O₃/water with volume fractions from 0 to 4%. The effects of Reynolds number, volume fractions of nanoparticles, and the geometry of sinusoidal tubes upon the heat-transfer coefficient were investigated. The results showed that using sinusoidal tubes enhances heat-transfer coefficients. Also, it was observed that increasing Reynolds number leads to higher heat-transfer coefficients in the convergent section. Moreover, it was observed that increasing the sinusoidal wave amplitude augments the convective heat-transfer coefficients; however, the increase in Nusselt number was slight. Furthermore, adding nanoparticles enhances heat transfer especially in large wave amplitude sinusoidal tubes.     

对流受热面传热强化研究进展

文章介绍了工业锅炉和其它换热设备中对流受热面传热强化的发展及西安交通大学动力工程多相流国家重点实验室在传热强化方面的研究进展。     

Experimental Determination of the Heat Transfer Coefficient of a Plate-Fin Heat Exchanger

Heat transfer in compact plate-fin heat exchangers is augmented by the introduction of complex fin patterns in the channels. Kays and London presented a lot of experimental data for several types of fin configurations, and many authors followed their example with other types of fins. For some fin types, the heat transfer correlation for the Nusselt number cannot be found in literature. Most of the data are given for large scale model fins in good controlled laboratory environments—little data is available for real heat exchangers.

A test rig was constructed at Ghent University to verify the performance of several fin types. Measurements were done on a real heat exchanger and not on a large scale model in order to determine the performance under real operational conditions.

The measurement setup consists of a hot water circuit and an air circuit with a fan. In the heat exchanger, 40 thermocouples are introduced on the air side and the wall. This way, the convection coefficient of the fins can be determined for a broad range of Reynolds numbers.

In the paper the measurement set-up is discussed and the measurements are presented. An in depth error analysis is performed on the measurements. This way a heat transfer correlation is provided with a tight error margin for compact plate-fin air coolers.     

自激振荡脉冲对流换热的实验研究

将Helmhotz共振腔应用于换热器来增强换热是一种新的强化换热方法。设计了一种换热效果较好的Helmhotz共振腔，并通过实验研究了Helmhotz共振腔对换热器的换热强化效果，分析了水力参数和结构参数对换热效果的影响，结果发现：对一定结构的共振腔，配以适当的水力参数，就可以产生自激振荡；对于同一结构的共振腔，水力参数不同，产生自激振荡的强弱也不同，随着压力的增加，自激振荡的强度也增加；将共振腔产生的自激振荡流引入换热器后，当自激振荡达到一定的强度时，能够破坏层流底层，从而可以强化换热；Helmhotz共振腔在绝大多数工况下能将管内换热系数提高10%-30%。     

O_2/CO_2燃烧方式下锅炉对流传热系数的修正算法和数值研究

采用热力计算与数值模拟相结合的方法,对富氧燃烧方式下锅炉对流受热面的传热特性进行研究,荻得了富氧气氛受热面对流传热系数的变化规律,由此提出了对流传热系数的修正算法.采用该算法,以某电厂300 MW锅炉为例,分别对空气燃烧方式和O2/CO2:燃烧方式下的各受热面进行了热力计算,并将计算结果与模拟结果进行了对比分析,结果两者相吻合,表明修正算法是可行的.分析结果还表明:富氧气氛下烟气的传热能力增强,即相同的受热面积传热量增加.     

Laminar Heat Transfer in a Pipe Subjected to a Circumferentially Varying External Heat Transfer Coefficient

Abstract

Numerical techniques have been used to solve the thermally developed regime for a laminar pipe flow that exchanges heat with a fluid environment in the presence of a circumferentially varying external heat transfer coefficient. By making use of the fact that the temperature distributions have similar shapes at successive streamwise locations, the three-dimensional temperature field was scaled to two dimensions. The resulting two-dimensional eigenvalue problem was solved by a rapidly converging automated scheme that successively refines an initial guess. Solutions were obtained for two circumferential distributions of the external heat transfer coefficient respectively intended to model forced and natural convection cross flows. The circumferential average heat transfer coefficient was found to be quite insensitive to the imposed circumferential variations. The local wall heat flux is nearly circumferentially uniform when the mean value of the external coefficient is high. On the other hand, at low mean values of the external coefficient, the local wall heat flux tends to follow the imposed circumferential variations.