Separation efficiency theoretical model of swirl-vane separator based on bidirectional vortex

Shuo Ouyang, Zhenqin Xiong*, Jiyun Zhao*, Ruiqi Kang

*Corresponding author for this work

Research output: Journal Publications and ReviewsRGC 21 - Publication in refereed journalpeer-review

13 Citations (Scopus)

Abstract

Swirl vane separator is a vital component to separate liquid water from gas to provide high quality steam to turbines in liquid water reactors. The gas rotating flow in the riser of a swirl vane separator is a bidirectional vortex. Its tangential velocity is similar with Rankine vortex. Its axial velocity is bidirectional. The gas bidirectional vortex is solved by constructing a Bragg-Hawthorne equation for the stream function. The gas flow velocity predicted by new method agrees quite well with CFD. The maximum velocity differences in axial direction are 6.2%. Based on this model, the droplet trajectory is obtained and a new separation efficiency model has been developed. The average difference between experiment results and the predicted separation efficiency is reduced from 14.7% to 3.1%. Moreover, parametric analysis using new model has been carried out to discuss the effect of inlet velocity, droplet diameter, swirl vane angle and hub diameter.
Original languageEnglish
Article number108984
JournalAnnals of Nuclear Energy
Volume170
Online published8 Feb 2022
DOIs
Publication statusPublished - 1 Jun 2022

Research Keywords

  • Bragg-Hawthorne equation
  • Rotating bidirectional flow field
  • Separation efficiency
  • Swirl vane separator
  • Theoretical analysis model

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