4.7 Article

Mechanistic CHF model development for subcooled flow boiling in a vertical rectangular channel under low pressure

Journal

Publisher

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.ijheatmasstransfer.2021.121328

Keywords

CHF; Rectangular channel; Subcooled flow boiling; Mechanistic model; Liquid sublayer dryout

Funding

  1. Nuclear Safety Research Program through the Korea Foundation Of Nuclear Safety (KoFONS) from the Nuclear Safety and Security Commission (NSSC), Republic of Korea [20030 04]
  2. KAINEET Institute, KAIST, South Korea [N11200045]
  3. National Research Foundation of Korea [N11200045] Funding Source: Korea Institute of Science & Technology Information (KISTI), National Science & Technology Information Service (NTIS)

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A new mechanistic model was developed in this study to predict the subcooled flow boiling CHF in a rectangular channel for turbulent upward flow under low pressure. The model considers the growth of coalesced vapor clot due to bubble coalescence in both the flow direction and radial direction, as well as the thinning of the liquid sublayer due to vapor clot growth. The proposed model showed good prediction performance with the lowest error compared to existing models.
Research reactors are recommended to be designed with sufficient safety margin for critical heat flux (CHF) in both normal and transient operation, which requires the development of predictive CHF models for both subcooled and saturated flow boiling conditions. While models exist for saturated flow boiling conditions, to date, no mechanistic CHF approach has been developed for subcooled flow boiling in a rectangular channel. In this paper, a new mechanistic model is derived to predict the subcooled flow boiling CHF in a rectangular channel for turbulent upward flow under low pressure. The proposed model is characterized by its consideration of coalesced vapor clot growth due to bubble coalescence not only in the flow direction, but also in the radial direction. In addition, existing liquid sublayer thickness calculation methods were compared to account for the thinning of the liquid sublayer due to the vapor clot growth. The proposed model was verified with a dataset consisting of 126 data points covering the following operational ranges: pressure 1.01-1.13 bar, mass flux 853-15,120 kg/m(2)s, exit quality -0.125 to -0.006, inlet subcooling 8-80 K, channel width 4-22 mm, channel gap 1-6.35 mm, heated length 50-305 mm, and turbulent upward flow. The developed model showed good prediction performance with a 32.47% RMS error, which is the lowest error compared to existing liquid sublayer dryout models developed for circular channels. (C) 2021 Elsevier Ltd. All rights reserved.

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