波节管强化传热式换热器的开发与应用

波节管强化传热式换热器的开发与应用东北大学郎逵１前言换热器是应用广泛的热设备之一。多年来一直应用的管壳式换热器及板式换热器、旋转式换热器等虽都有不断改进，但也都存在着问题，客观上急需一种换代产品，使换热器有个大的改进与变化。强化传热的理论与实践￣［１...     

间壁式换热器传热的强化

介绍了传热强化的基本原理和有效措施。指出，综合传热系数是换热器的重要经济技术指标，是评价一个换热器性能好坏的决定性参数。要强化换热器的传热，必须同时强化空气侧和烟气侧的传热才会产生最佳的效果，得到较高的综合传热系数。     

容积式换热器的传热强化

本文论述了国内容积式换热器的应用现状，针对其不足提出了强化传热的方向，并建议采用矩形翅片椭圆管作换热元件。     

新型螺旋管换热器的节能效益分析

1 前言 传热是化工过程中的重要过程,换热器的投资往往要占到化工设备总投资的15％。传热的效果和效率直接影响化工设备的生产能力和投资效益,而改进传热的实质则是开发和采用性能优良的传热元件,使传热得到强化。在圆管壁上轧制螺旋槽纹来强化传热就是近期的开发成果之一。国内外的书刊已经对这类轧槽管的传热特性、流体力学特性作了报道。本文综合分析有关资料,对螺旋槽管的传热性能,螺旋管换热器的构造、性能、计算和热效率的评价作简单介绍。     

水平螺旋管式换热器的流热耦合传热特性研究

针对轴封式核主泵的水平螺旋管换热器复杂的结构特点和特殊的运行环境,采用流热耦合的数值模拟方法分析壳侧流体的流量和温度改变对换热器的流场和温度场的影响,探究换热器壳侧进口参数对换热器内流体流动换热特性的影响规律,并采用相关传热准则数分析换热器强化传热性能。结果表明:水平螺旋管流体受曲率的影响产生离心力,形成了有别于直管流动换热的二次流,速度分布呈内凹的圆弧状,会增强换热器传热效率;随壳侧流速的增加,流体的扰动程度加强,湍流程度提高,同时压力损失无明显变化,换热器传热性能增强;在既定结构和尺寸下,由换热器的传热性能曲线可知,壳侧流量和雷诺数的增加对强化螺旋管传热有显著影响。实际工程应用中可采用适当提高换热器的壳侧流量的方法来加强传热。     

换热器节能新途径：螺旋槽管强化传热技术

介绍了螺旋槽管强化传热技术的原理，在锅炉空气预热器及发电厂高压加热器的应用实例。节能效果显著，值得在电力、化等行业推广应用。     

自激振荡管壳式换热器强化传热的可行性分析

脉动流体能够使管壳式换热器换热系数得到提高,而自激振荡腔在一定的结构参数和运行参数下能够使流体产生脉动。在管壳式换热器前安装自激振荡腔,使流体流经自激振荡腔产生脉动流动,从而实现管壳式换热器的强化传热。分析了将自激振荡腔用于管壳式换热器强化传热可行性。     

新型螺旋管换热器的设计

螺旋管式换热器适于处理粘度大的流体或含固体颗粒的泥浆，被广泛应用。文章对一种高效、紧凑型的螺旋管换热器的结构设计作了讨论，对螺旋管换热管等具有过冷情况的热力计算方法作了探讨。     

管壳式换热器壳程强化传热技术研究

介绍了管壳式换热器壳程强化传热方面所展开的研究工作及取得的成果，指出了强化传热技术的研究方向。     

内置螺旋纽带换热器强化传热性能实验分析

换热设备的应用遍布生产、生活的各个领域,随着能源成本的升高和碳排放量的增大,采用简单、高效的方式提高换热设备的传热效率对于节能、增效意义重大。螺旋纽带技术作为一种结构简单,实用性强的强化传热技术,强化传热的同时兼具防垢的性能,非常适用于现有设备的技术改造。采用实验的方法对光管换热器和装有自转螺旋纽带换热器的传热系数k及压降ΔP进行测定,通过实验数据的对比分析表明,在管道流速为1.5 m/s,加装螺旋纽带装置后换热器传热系数和管侧流体压降数值比光管时提高了近1倍。     

Heat transfer effectiveness of three-fluid separated heat pipe exchanger

A heat transfer model for three-fluid separated heat pipe exchanger was analyzed,and the temperature transfer matrix for general three-fluid separated heat exchanger working in parallel-flow or counter-flow mode was obtained.It was found that the forms of temperature transfer matrix are similar for heat pipe rows with equal or different heat transfer surface area.Furthermore,by using the temperature transfer matrix of the heat pipe exchanger,the relationship between heat transfer effectiveness θ 1,θ 2 and M,NTU,U,Δt i were derived for the exchanger operating in parallel-flow or counter-flow mode,and a simple special example was adopted to demonstrate the correctness of these relationships.     

Heat transfer of horizontal parallel pipe ground heat exchanger and experimental verification

The ground heat exchangers (GHE) consist of pipes buried in the soil and is used for transferring heat between the soil and the heat exchanger pipes of the ground source heat pump (GSHP). Because of the complexity of the boundary conditions, the heat conduction equation has been solved numerically using alternating direction implicit finite difference formulation. A software was developed in MATLAB environment and the effects of solution parameters on the results were investigated. An experimental study was carried out to test the validity of the model. An experimental GSHP system is installed at Y?ld?z Technical University Davupasa Campus on 800 m² surface area with no special surface cover. Temperature data were collected using thermocouples buried in soil horizontally and vertically at various distances from the pipe center and at the inlet and the outlet of the ground heat exchanger. Experimental and numerical simulation results calculated using experimental water inlet temperatures were compared. The maximum difference between the numerical results and the experimental data is 10.03%. The temperature distribution in the soil was calculated and compared with experimental data also. Both horizontal and vertical temperature profiles matched the experimental data well. Simulation results were compared with the other studies.     

Heat pipe heat exchanger for heat recovery in air conditioning

The heat pipe heat exchangers are used in heat recovery applications to cool the incoming fresh air in air conditioning applications. Two streams of fresh and return air have been connected with heat pipe heat exchanger to investigate the thermal performance and effectiveness of heat recovery system. Ratios of mass flow rate between return and fresh air of 1, 1.5 and 2.3 have been adapted to validate the heat transfer and the temperature change of fresh air. Fresh air inlet temperature of 32–40 °C has been controlled, while the inlet return air temperature is kept constant at about 26 °C. The results showed that the temperature changes of fresh and return air are increased with the increase of inlet temperature of fresh air. The effectiveness and heat transfer for both evaporator and condenser sections are also increased to about 48%, when the inlet fresh air temperature is increased to 40 °C. The effect of mass flow rate ratio on effectiveness is positive for evaporator side and negative for condenser side. The enthalpy ratio between the heat recovery and conventional air mixing is increased to about 85% with increasing fresh air inlet temperature. The optimum effectiveness of heat pipe heat exchanger is estimated and compared with the present experimental data. The results showed that the effectiveness is close to the optimum effectiveness at fresh air inlet temperature near the fluid operating temperature of heat pipes.     

Heat transfer coefficients under dry- and wet-surface conditions for a spirally coiled finned tube heat exchanger

In the present study, the average tube-side and air-side heat transfer coefficients in a spirally coiled finned tube heat exchanger under dry- and wet-surface conditions are experimentally investigated. The test section is a spiral-coil heat exchanger, which consists of six layers of concentric spirally coiled tube. Each tube is fabricated by bending a 9.6-mm outside diameter straight copper tube into a spiral coil of four turns. Aluminium fins with thickness 0.6 mm and outside diameter 28.4 mm are placed helically around the tube. The chilled water and the hot air are used as working fluids. The test runs are done at the air and water mass flow rates ranging between 0.02 and 0.2 kg/s and between 0.04 and 0.25 kg/s, respectively. The inlet-air and -water temperatures are between 35 and 60 °C and between 10 and 35 °C, respectively. The effects of the inlet conditions of both working fluids flowing through the heat exchanger on the heat transfer coefficients are discussed. New correlations based on the data gathered during this work for predicting the tube-side and air-side heat transfer coefficients for the spirally coiled finned tube heat exchanger are proposed.     

波节管换热器的强化换热分析

本文分析了波节管的强化换热机理 ,介绍了波节管换热器的性能及其基本计算方法 ,为换热器的使用提供了理论参考。     

Heat transfer enhancement of nanofluids in a double pipe heat exchanger with louvered strip inserts

The effect of using louvered strip inserts placed in a circular double pipe heat exchanger on the thermal and flow fields utilizing various types of nanofluids is studied numerically. The continuity, momentum and energy equations are solved by means of a finite volume method (FVM). The top and the bottom walls of the pipe are heated with a uniform heat flux boundary condition. Two different louvered strip insert arrangements (forward and backward) are used in this study with a Reynolds number range of 10,000 to 50,000. The effects of various louvered strip slant angles and pitches are also investigated. Four different types of nanoparticles, Al₂O₃, CuO, SiO₂, and ZnO with different volume fractions in the range of 1% to 4% and different nanoparticle diameters in the range of 20 nm to 50 nm, dispersed in a base fluid (water) are used. The numerical results indicate that the forward louvered strip arrangement can promote the heat transfer by approximately 367% to 411% at the highest slant angle of α = 30° and lowest pitch of S = 30 mm. The maximal skin friction coefficient of the enhanced tube is around 10 times than that of the smooth tube and the value of performance evaluation criterion (PEC) lies in the range of 1.28–1.56. It is found that SiO₂ nanofluid has the highest Nusselt number value, followed by Al₂O₃, ZnO, and CuO while pure water has the lowest Nusselt number. The results show that the Nusselt number increases with decreasing the nanoparticle diameter and it increases slightly with increasing the volume fraction of nanoparticles. The results reveal that there is a slight change in the skin friction coefficient when nanoparticle diameters of SiO₂ nanofluid are varied.     

Heat transfer characteristics of the evaporator section using small helical coiled pipes in a looped heat pipe

An experimental study was carried out for the heat transfer characteristics and the flow patterns of the evaporator section using small diameter coiled pipes in a looped heat pipe (LHP). Two coiled pipes: the glass pipe and the stainless steel pipes were used as evaporator section in the LHP, respectively. Flow and heat transfer characteristics in the coiled tubes of the evaporator section were investigated under the different filling ratios and heat fluxes. The experimental results show that the combined effect of the evaporation of the thin liquid film, the disturbance caused by pulsation and the secondary flow enhanced greatly the heat transfer and the critical heat flux of the evaporator section. In final, two dimensionless empirical correlations were proposed for predicting the heat transfer coefficients of the evaporator section before and after dryout occurs.     

地源热泵竖直地埋管换热量的计算

按照《地源热泵系统设计技术规范》中附录B提供的依据,对竖直地埋管换热器的各项热阻进行了详细计算,得出每米换热量,用于指导设计,并通过对结论的分析指出了应用《地源热泵系统设计技术规范》应注意的问题.     

蓄热式管壳换热器传热特性研究

针对热电联产机组供热期发电负荷受供热量限制,机组调峰能力下降、电力系统弃风弃光现象严重的问题,设计了一种新型蓄热式管壳换热器.利用相变材料蓄/放热过程中温度接近恒定、释放潜热量大等优点,选取石蜡为相交材料,换热器相交区作为换热单元,采用控制变量法,针对传热流体流速、相变材料导热系数及相变层厚度等关键因素,对换热单元的蓄...     

Experimental investigation of heat transfer in a triple tube heat exchanger with coiled spring inserts

Experiments have been performed to investigate the effect of coiled spring inserts on heat transfer, pressure drop, and performance parameters of a triple tube heat exchanger (TTHX). Three different spring inserts having a pitch of 5, 10, and 15 mm are used and the diameter of the spring wire is taken as 1 mm. The experiments were carried out under a turbulent flow regime, with water as a working medium in parallel and counter flow configurations. The variation in different performance characteristics like heat transfer coefficient, Nusselt number, and effectiveness have been compared at various Reynolds numbers ranging between 4000 and 16,000 in the considered flow patterns. The Nusselt number of TTHX with the lowest pitch spring is found to be higher than that of the plain TTHX by 57.27% at Re = 4000 for the counter flow configuration. Both the thermal performance factor and effectiveness increased as the pitch of the spring insert was decreased. The effectiveness of TTHX with the lowest pitch spring insert is found higher than that of the plain TTHX by 43.84% in the counter flow pattern.