CFD evaluations on bundle effects for steam condensation in the presence of air under natural convection conditions. (November 2018)

• Record Type: Journal Article
• Authors: Bian, Haozhi; Sun, Zhongning; Cheng, Xiang; Zhang, Nan; Meng, Zhaoming; Ding, Ming
• Is Part Of: International communications in heat and mass transfer. Volume 98(2018:Nov.)
• Page Start: 200
• Page End: 208
• Publication Date: 2018-11
• Subjects: Steam condensation -- Non-condensable gas -- CFD -- Inhibition effect -- Stack effect; Heat -- Transmission -- Periodicals; Mass transfer -- Periodicals; Chaleur -- Transmission -- Périodiques; Transfert de masse -- Périodiques; Heat -- Transmission; Mass transfer; Periodicals; 621.4022
• DOI: 10.1016/j.icheatmasstransfer.2018.09.003
• Languages: English
• ISSNs: 0735-1933

Abstract

Abstract: Steam condensation in the presence of air is a relevant phenomenon in various industrial applications. Its heat transfer property has been broadly revealed by experimental and numerical investigations on vertical plates or single tubes. However, these results may not be directly applied to tube bundle cases, since there may exist mutual interactions among adjacent tubes. To have an insight on this problem, the present work conducted numerical simulations on various tube bundles with a tube pitch 1.5 times of the tube diameter. The cases evaluated were classified into three categories including the single row, double row, and triple row. In each category, structures with various tube columns were assessed. The results indicate that tube bundles will thicken the near-wall high concentration air layer, resulting in inhibited condensation heat transfer. This phenomenon is defined as the inhibition effect. On the other hand, a heat transfer enhancement effect caused by a strengthened natural circulation driven by the density difference between the mainstream and the high concentration air region is found and defined as the stack effect. The average condensation heat transfer for tube bundles is determined by the relative magnitude between the inhibition effect and the stack effect. The stack effect becomes much intensive with the increase of tube rows and columns, which can enhance condensation heat transfer. Typically, the results in the triple row categories show that the maximum average heat transfer coefficient can be 14% greater than that of the single tube.