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首页> 外文期刊>International Journal of Process Systems Engineering >Improving the performance of shell-and-tube heat exchangers by the addition of swirl
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Improving the performance of shell-and-tube heat exchangers by the addition of swirl

机译:通过增加涡流来改善管壳式换热器的性能

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Heat exchanger is a component which is used to transfer the heat from one medium to another efficiently. Generally, they occupy a large space compared to other components and such bulky designs are not attractive in the modern industrial applications due to several constraints. Therefore, it is invaluable to develop compact heat exchangers but with the improved performance. In this work, an investigation was made on the possibility of reducing the size of a shell-and-tube heat exchanger by addition of swirl. Swirl was generated by using a twisted-tape which inserted inside tube and the effects of these tapes on the heat transfer rate and pressure drop were theoretically studied. The results showed that a half-length regular spaced twisted-tape insert gave the lowest Nusselt number while a full-length twisted-tape insert gave the maximum Nusselt number and hence the highest rate of heat transfer. The length of the heat exchanger could be reduced by 13.3% with a full-length twisted tape and this would be result in 6.8% of reduction of the fabrication cost. Therefore, addition of swirl into the fluid flow should help to design compact and low cost heat exchanges with improved performance but the pressure drop increased leading to an increase of the required pumping power. A prototype shell-and-tube heat exchanger was designed and fabricated based on the theoretical results. Studies are underway to experimentally investigate the overall effectiveness of the use of twisted-tape inserts for enhancing the heat transfer rate by considering all the related benefits and drawbacks.
机译:热交换器是用于将热量有效地从一种介质传递到另一种介质的组件。通常,与其他组件相比,它们占据了很大的空间,并且由于一些限制,这种庞大的设计在现代工业应用中没有吸引力。因此,开发紧凑的热交换器但具有改善的性能是无价的。在这项工作中,研究了通过增加涡旋来减小管壳式换热器尺寸的可能性。通过使用插入管内的扭曲带产生旋流,并从理论上研究了这些带对传热速率和压降的影响。结果表明,半长的规则间隔的扭曲带插入物的Nusselt数最低,而全长的扭曲带插入物则具有最大的Nusselt数,因此传热速率最高。使用全长扭曲带可以将热交换器的长度减少13.3%,这将减少6.8%的制造成本。因此,在流体流中增加旋流应有助于设计紧凑且低成本的热交换,从而提高性能,但压降增加,导致所需的泵送功率增加。根据理论结果设计并制造了原型管壳式换热器。考虑到所有相关的利弊,正在进行实验性地研究使用扭曲带插入物以提高传热速率的整体有效性。

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