A study of heat transfer scaling of supercritical pressure water in horizontal tubes. (November 2017)

• Record Type: Journal Article
• Authors: Lei, Xianliang; Li, Huixiong; Dinh, Nam; Zhang, Weiqiang
• Is Part Of: International journal of heat and mass transfer. Volume 114(2017)
• Page Start: 923
• Page End: 933
• Publication Date: 2017-11
• Subjects: Supercritical water -- Heat transfer -- Scaling -- Horizontal flow; Heat -- Transmission -- Periodicals; Mass transfer -- Periodicals; Chaleur -- Transmission -- Périodiques; Transfert de masse -- Périodiques; Electronic journals; 621.4022
• DOI: 10.1016/j.ijheatmasstransfer.2017.06.052
• Languages: English
• ISSNs: 0017-9310

Abstract

Highlights: The heat transfer behaviors of the horizontal flow of supercritical pressure fluid are experimental investigated. Effect of diameters to the severity of heat transfer deterioration in circular top surfaces have been discussed. Buoyancy effect is larger than that of the thermal acceleration in the horizontal tube. Two differential correlations are proposed to the top and bottom surface respectively for horizontal flow. Abstract: Understanding the role of the heat transfer scaling in supercritical utilities can help us obtain a better design for supercritical single phase thermosiphons. In this paper, heat transfer scaling analysis of supercritical pressure water in horizontal tubes with differential inside diameters are experimentally investigated. The operating conditions included mass flux of 100–600 kg/m 2 s and heat flux of up to 400 kW/m 2 . The uneven circumferential temperature distributions are discussed firstly over a broad range of heat fluxes. A significant temperature discrepancy exists between the top and bottom surface in each pipe, deteriorated heat transfer occurs on the top surface but enhanced heat transfer happens in the bottom region. With the rise of heat flux, more severe deterioration appears on the higher domain. Then a qualitatively comparison on the heat transfer characteristic of supercritical flow in different pipes are implemented. Evidently, with the increase of tube diameter, the inner-wall temperature peak is much pronounced and the degree of deterioration at the top surface much severe due to the intensification of buoyancy force. The heat transfer mechanism of horizontal pipes is further discussed by comparing the effect of buoyancy and thermal acceleration. With the augment of diameter, free convection gradually intensifies due to its steeper density variation and expanded flow space, which leads to larger temperature deviation between the bottom and top region along the circumferential direction. On the contrary, thermal acceleration plays a relatively minor role in deteriorated heat transfer. Considering the scaling effect in various pipes, two heat transfer correlations are proposed respectively in both the bottom and top region of the horizontal flows.