改进型波节管式换热器及其应用

改进型波节管式换热器及其应用沈阳新能源联合开发公司（沈阳１１００１５）郎逵１前言波节管型换热器是一种新型的换热器，它是由国内首创并走向国内外市场的一种高效安全可靠的换热器。这种换热器采用波节型强化传热管代替壳管式换热器中的直管，将波节管的优点与壳管结...     

螺旋板换热器在节能技术改造中的应用

<正> 1 前言螺旋板换热器是一种表面式用于汽—水、水—水或其它流质热交换的一种较新型高效换热器,与平板式换热器、管壳式换热器及其它换热器相比有着较突出的多种优点。下面就几年来汽改水技术的经验谈一下螺旋板换热器的应用及其节能效果。几年来,在国家有关能源政策的指导下,在市有关部门的领导下,我们重点抓了市地方企业的采暖汽改水工作,先后为市合成纤维厂、化     

两种用于HCPV/T的水冷换热器传热特性的对比实验研究

本文对两种适用于高倍聚光发电供热（HCPV/T）系统的多槽道和微通道水冷换热器进行了实验研究。利用模拟热源模拟了HCPV/T系统中光伏电池工作时的热流密度,分别研究了流量、壁面温度和输入电压对两种换热器传热特性的影响,并利用传热学理论对两种换热器的特点进行分析,获得了两种换热器努赛尔数Nu与雷诺数Re的拟合经验公式。实验结果表明,微通道换热器在低流量下有较强的换热能力,但在高流量下,换热能力无法随流量增大继续提高;多槽道换热器在低流量下换热能力不佳,但在高流量下仍可随流量增大继续提高。     

地表水源热泵系统的设计

介绍了地表水源热泵系统的2种形式及其特点；研究了湖水传热的方式，并给出了湖水换热器的设计方法，包括循环介质流量、换热器类型、换热器的长度、换热器管径的确定。     

换热器在摩托车催化器性能台架中的应用

为满足摩托车催化器性能考核台架对催化器入口温度控制的要求,设计了冷轧翅片管和单程管壳式两种换热器,并分析对比了这两种换热器的优缺点,根据对温度控制的要求和试验台架的空间布置特点,选定冷轧翅片管换热器控制催化器入口温度,试验结果表明该换热器能够连续调节催化器入口温度,控制温度波动在±2°C之间,可以满足试验要求。     

板翅式换热器在燃气轮机进气冷却系统中的应用

将板翅式换热器应用于吸收式燃气轮机进气冷却系统中，降低燃气轮机压缩机进口温度，提高燃气轮机高温条件下的出力，在国内尚无先例。针对板翅式换热器，简要介绍了结构、布置形式和性能。通过实测的运行数据，对板翅式换热器和管式换热器的性能进行了对比。结果表明：板翅式换热器在传热系数、体积、进气阻力等方面，性能优于管式换热器，是一种值得发展的换热设备。最后提出了该板翅式换热器在实际应用中存在的一些问题及对应的处理方法。     

椭圆管与扁管管板式换热器换热性能的分析比较

本文对椭圆管与扁管管板式换热器的充分发展的周期性层流流动与换热特性进行了数值计算分析,给出了在400相似文献   

多管型套管式换热器传热与流阻性能试验研究

多管型套管式换热器是在大尺寸外管的内部布置多根内管所构成的换热设备 ,与单根内管的套管式换热器相比 ,流量大幅增加 ,选用螺纹内管和管间折流板可以强化传热。对于多管型套管式换热器的传热性能试验 ,采用修正威尔逊法进行试验计算 ,得出了两种多管型套管式换热器的传热与流动阻力性能试验结果。     

热管式空调换气换热器的设计与研究

本文提出了一种以热管为传热元件的全气候使用的空调换气换热器，就其设计特点、结构型式及性能评价和效益分析作了叙述。换热器中的热管采用氨－铝热管，分重力式热管和吸液芯式换管两种。重力式热管空调换气换热器采用了随电机正反转改变进排气方向的轴流式风机；吸液芯式换热器采用了特殊结构设计，解决了吸液芯热管受安装误差带来的热管半失效问题。     

石墨烯-PFA复合材料换热器与金属换热器的传热性能对比

氟塑料换热器以其耐腐蚀、耐磨损等优点而备受关注,但氟塑料热导率较低,换热能力差,限制了其广泛应用。石墨烯-PFA复合材料兼具石墨烯优异的导热性和可熔性聚四氟乙烯(PFA)良好的耐酸碱腐蚀性,是新一代的换热器材料。搭建了余热回收测试实验台,对石墨烯-PFA复合材料换热器和金属换热器的传热性能进行对比。研究了不同烟气流速、不同进口烟气温度以及不同石墨烯配比对复合材料传热性能的影响。结果表明:对于金属换热器和复合材料换热器,当烟气流速从2.0增加到4.0 m/s时,传热系数分别增加到原来的1.19和1.34倍;随着进口烟温的升高,两种材质的传热系数分别降低了15.6%和14.7%;随着石墨烯含量增加,复合材料的导热系数以及传热系数均增加。     

预测多股流板翅式换热器动态特性的网络法

提出了一种基于两股流换热器网络动态特性预测多股流换器动态性能的网络法。经与实验对比，表明这是一种简便，正确描述多股流换热器动态性能的方法。     

The Thermal Behavior of Coal—Ash Deposits on Heat Exchangers

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Advances of nanofluids in heat exchangers—A review

Recently, many researchers have focused on their studies on the analysis of nanofluid flows due to their participation in the enhancement of heat transfer rates in industrial processes. The ordinary fluids, such as water, mineral oils, and so on, are known for their low thermal conductivity in heat transfer processes. A significant enhancement in the thermal properties of ordinary fluid may be obtained by adding nanoparticles having a diameter of less than 100 nm or suspension of fibers. Better spreading, wetting, dispersion, and stability and with acceptable viscosity are the main advantageous properties of nanofluids on a solid surface. The nanofluids are encountered in various thermal engineering systems such as in heat exchangers, refrigeration, thermal management of fuel cells, cooling of nuclear reactors, microelectromechanical systems, and others. In particular, the thermal conversion is known as a great application of nanotechnology, and many studies have been achieved with such fluids in heat exchangers. Therefore, this paper aims to present a global insight into the different applications of nanofluids in various heat exchangers, that is, heat pipe and plate-fin heat exchangers. All research works have been summarized into three main parts: laminar, transition, and turbulent nanofluid flow regimes.     

基于数值计算的U型地埋管井群换热器计算模型研究

针对U型地埋管换热器的特点,在分析单井换热器换热量的基础上,考虑到多井换热器井与井之间传热的相互干扰,提出了一种用于U型地埋管井群换热器数值计算的9井模型,这种模型在数值计算时既能代表一般井群换热的规律,又便于计算机处理,为实际工程中分析井群换热规律提供了很好的理论依据。     

两股流板翅式换热器的精确数学控制

两股流板翅式换热器因具有良好的换热性能,在许多工业领域备受青眯.但因换热器在工作过程中受到各种因素的干扰,加之复杂的换热过程,使得很难获得良好的控制品质.所以本文在传统控制方法的基础上提出了精确数学控制方法,其核心技术是引入反问题算法,并通过对两股流板翅式换热器的实验,取得良好的控制效果,证实了精确数学控制是实现板翅式换热器高质量控制的一种新型、高效的控制方法.     

Maximum entropy generation of in‐series connected heat exchangers

Theoretical analysis of entropy generation and availability destruction of “n” similar cocurrent or counter‐current heat exchangers connected in series are presented. A criterion for comparing the relative performance of any number of in‐series connected similar heat exchangers is developed. The effect of different influencing parameters such as the number of connected heat exchangers, the individual effectiveness of each unit, the heat capacity rate ratio and flow arrangement on the quality of heat exchange are presented. It is found that, the maximum of availability destruction (maximum entropy generation) for in‐series‐connected similar cocurrent heat exchangers is obtained at ϵ^*=1/(1+δ). However, for counter‐current heat exchangers connected in‐series; ϵ=1/(∑δ^i/n). This analysis might be useful for a proper choice of the number of heat exchangers to be connected together and the choice for the best operating conditions. Copyright © 2000 John Wiley & Sons, Ltd.     

Dynamic behaviour of one-dimensional flow multistream heat exchangers and their networks

The dynamic behaviour of one-dimensional flow (cocurrent and countercurrent) multistream heat exchangers and their networks is modelled and simulated. The problems can be classified into two types: (1) dynamic responses to arbitrary temperature transients and to sudden flow rate transients from a uniform temperature initial condition or a steady-state condition, which yield a linear mathematical model; (2) dynamic responses to disturbances in thermal flow rates, heat transfer coefficients or flow distributions, which are non-linear problems and should be solved numerically. A linearized model is developed to solve the non-linear problems with small disturbances. The linear model and the linearized model for small disturbances are solved by means of Laplace transform and numerical inverse algorithm. Introducing four matching matrices, the general solution can be applied to various types of one-dimensional flow multistream heat exchangers such as shell-and-tube heat exchangers and plate heat exchangers as well as their networks. The time delays in connecting and bypass pipes are included in the models. The software TAIHE (transient analysis in heat exchangers) is further developed to include the present general solution and is applied to the simulation of fluid temperature responses of multistream heat exchangers. Examples are given to illustrate the procedures in detail.     

Numerical study of horizontal ground heat exchangers for design optimization

Despite ground source heat pump has been proven as highly efficient, high initial cost discourages homeowners and small-medium enterprises to opt for such systems. Horizontal ground heat exchangers offer relatively low-cost solution that may help promoting these systems usage worldwide. This study examines ways to optimize the designs for horizontal ground heat exchangers by using different layouts and pipe materials. CFD simulation of three dimensional models was performed to achieve this objective. All cases tested are able to yield comparable heat exchange rate for an equal trench length. However, the effective period differs one from the other. Additional initial and overhead costs are worthy as slinky ground heat exchangers prolongs heat transfer process when compared against straight configuration. Pipe materials with superior thermal conductivity also promote longer high efficiency operation. An improvement of 16% is reported when copper pipe is used instead of the conventional HDPE pipes. Effective period can be extended by 14% when ground heat exchangers are installed in vertical orientation. Thermal interference in slinky configuration is prevalent during initial operation. In a long run, the effect is observed to be minimal except in vertical orientation. However, it is avoidable beforehand at design stage.     

The interaction of mercury and aluminium in heat exchangers in a natural gas plants

This paper reviews current understanding of mercury induced liquid metal embrittlement (LME) and the mechanism of failure in aluminium heat exchangers. Natural gas can be contaminated with low levels of mercury, which can concentrate in cryogenic heat exchangers. There have been several instances where LME has led to major failures and gas leakage in gas processing plant.     

A new approach for thermal performance calculation of cross-flow heat exchangers

A new numerical methodology for thermal performance calculation in cross-flow heat exchangers is developed. Effectiveness-number of transfer units (ε-NTU) data for several standard and complex flow arrangements are obtained using this methodology. The results are validated through comparison with analytical solutions for one-pass cross-flow heat exchangers with one to four rows and with approximate series solution for an unmixed-unmixed heat exchanger, obtaining in all cases very small errors. New effectiveness data for some complex configurations are provided.