400t/h锅炉的两项改造

将燃烧器下层一次风咳喘改成谈、稀相燃烧，降低了助燃油耗量和飞灰可燃物含量，用鳍片管式省煤器替换原光管式省煤器，降低了排烟温度并改善了管壁磨损，两项改造后取得发电量增加，锅炉热效率提高1％的效果。     

Experimental study on heat and mass transfer characteristics of louvered fin-tube heat exchangers under wet condition

An experimental study was conducted to investigate the effect of a tube row, a fin pitch and an inlet humidity on air-side heat and mass transfer performance of louvered fin-tube heat exchangers under wet condition. Experimental conditions were varied by three fin pitches, two rows, and two inlet relative humidities. From the experimental results, it was found that the heat transfer performance decreased and the friction increased with the decrease of a fin pitch, for 2 row heat exchanger. The effect of a fin pitch on heat transfer performance was negligible with 3 row heat exchanger. The change in a relative humidity was not affected heat transfer and friction. However, the mass transfer performance was slightly decreased with the increase of a relative humidity and with the decrease of a fin pitch. The mass transfer performance decreased with the decrease of a fin pitch. The mass transfer performance of the louvered fin-and-tube heat exchanger was different according to the number of a tube row.     

Experimental investigation and analysis of composite silica-gel coated fin-tube heat exchangers

Desiccant coated heat exchanger provides a promising option for desiccant cooling system, since it can handle sensible load and latent load simultaneously within one component. It is fabricated by coating desiccant material on the surface of conventional fin-tube heat exchanger. In order to enhance the performance of conventional silica gel coated heat exchanger (SGCHE), a novel composite silica gel coated heat exchanger (CCHE) is proposed and fabricated. An experimental setup is built to test and compare the dynamic performance of SGCHE and CCHE. Influences of main operation parameters including water temperatures and inlet air conditions on system performance are analyzed in terms of average dehumidification capacity (D_avg) and thermal coefficient of performance (COP_th). Optimization of cycle switch modes is also discussed. Experimental results show that CCHE has better dehumidification performance compared with SGCHE. In addition, pre-cooling before dehumidification process is found to be advantageous to both D_avg and COP_th.     

基于ANSYS的翅片管式换热器端板的应力分析

应用ANSYS有限元分析软件对翅片管式换热器壳体端板进行应力分析,分析结果满足使用要求,为保证设备的安全性提供了理论依据。     

强化翅片管式换热器换热性能的方法及应用

通过两种不同的方法改进应用在不同场合的翅片管式换热器的结构,进而提高其换热性能:一种是将低温工况下易结霜的换热器设计成变翅片间距,一种是将空调工况下的换热器设计成变螺距内螺纹管.通过热力计算及实际系统使用,得出传热系数分别提高了9.8%和3.82%.     

Novel structural designs of fin-tube heat exchanger for PEMFC systems based on wavy-louvered fin and vortex generator by a 3D model in OpenFOAM

Heat management is crucial to the stable and high-efficiency operation of proton exchange membrane fuel cell (PEMFC) system. However, fin-tube heat exchangers (FTHE) of traditional internal combustion engine vehicles require further optimizations to be applicable to PEMFC vehicles. In the paper, a three-dimensional steady-state radiator model is developed in OpenFOAM to investigate three novel structural designs based on wavy-louvred (WL) fin and vortex generators (VGs). The established model has been carefully validated against experimental data and correlation reference. To comprehensively evaluate radiator performances, the air side heat transfer coefficient, pressure drop, outlet air temperature, heat flux, and JF factor are adopted. It is found that the FTHE with L-VGs has the highest heat transfer coefficient while the FTHE with WL-VGs has the highest pressure drop. The temperature, velocity, and pressure distribution are further demonstrated to reveal performance enhancement mechanisms. It is seen that the heat exchangers with additional VGs produce two sections of high-temperature wakes near the wall, which not only promotes the heat convection but also contributes to the heat exchange in the nearby area. Meanwhile, a low-speed vortex zone behind VGs appears and generates longitude vortex, making the air stream stay longer at fin surfaces. The air flow in FTHE with WL is not as much separated as the conventional FTHE since the zigzag wavy louver restricts flow separation. The paper gives valuable suggestions for cooling capability improvement and radiator volume diminution.     

水-空气翅片管换热器变工况、变结构特性模型分析

翅片管换热器变工况、变结构特性,是指其性能不仅受到工况参数的影响,而且也随结构参数的改变而变化的特性.因此,为深入研究此换热器特性,建立了相关的分析模型.当任一工况或结构参数在其最大可变范围内变化时,该模型可分析预测翅片管换热器相应的性能变化规律.利用实验数据对模型计算结果进行了对比验证:干工况下,模型计算所得的各性能参数值与实测值吻合良好,其平均相对误差均小于6％;湿工况下,计算值与实验值的平均相对误差也在20％内,且其变化趋势一致,从而证明了模型的正确性及有效性.分析模拟所得的变工况、变结构特性,不仅有利于优化产品的结构设计,可辅助换热器的选型,而且还为换热器运行调节方法的选取提供了依据.     

回路设计对冷风机性能影响的研究

本文对强制循环空气冷却器（简称冷风机）的盘管设计中对冷风机换热性能影响较大的一个因素———回路设计进行了研究。研究得出对于给定的翅片管换热器存在一个最佳的回路数,使该换热器发挥最大的换热性能,同时,每个回路的排布方式对换热性能也有影响。本文的研究结果希望能对冷风机的优化设计提供一定的参考。     

翅片管式CO2气体冷却器模拟与优化

为了研究CO2在翅片管式气体冷却器内的流动特性,建立了稳态分布参数模型,并进行了实验验证。结果表明:CO2侧换热系数受入口压力和质量流量的影响较大,但入口温度对其影响很小。换热量随着入口压力的变化有一个最大值;且随着流量的增大,最大换热量所对应的入口压力值逐渐增大。压降和换热量均随入口温度的增加而线性增加。适当增加管程数,采用较小管径的气冷器性能更高。