石油化工高等学校学报

石油化工高等学校学报 ›› 2015, Vol. 28 ›› Issue (4): 86-90.DOI: 10.3969/j.issn.1006-396X.2015.04.018

• 油气储运 • 上一篇    下一篇

一种改进的水平管气液两相流截面含气率预测模型

陈 婧郑洪峰于英民   

  1.     
    ( 中国石油大学( 华东) 储运与建筑工程学院, 山东青岛2 6 6 5 8 0)
  • 收稿日期:2014-05-25 修回日期:2015-04-28 出版日期:2015-08-25 发布日期:2015-08-25
  • 作者简介:陈婧( 1 9 7 7 - ) , 女, 硕士, 实验师, 从事油气储运实验测量方向研究; E - m a i l : C h e n j i n g_3 2@1 6 3. c o m。
  • 基金资助:
    国家自然科学基金资助项目( 5 1 0 0 6 1 2 3) ; 中央高校基本科研业务费专项基金项目( 1 4 C X 0 5 0 2 8 A) ; 山东省优秀中青
    年科学家奖励基金( B S 2 0 1 1HZ 0 2 4) 。

A Modified Model for Void Fraction Prediction in Horizontal GasLiquid Pipe

  1. College of Pipeline and Civil Engineering, China University of Petroleum,Qingdao Shandong 266580, China
  • Received:2014-05-25 Revised:2015-04-28 Published:2015-08-25 Online:2015-08-25

摘要: 考虑了环状流液膜中含有气泡, 气芯中夹带液滴的情况, 根据S m i t h的环状流液膜动能与中间气芯动 能相等的假设, 提出了一个改进的截面含气率预测模型。实验结果表明, 对于水平管空气 - 水两相流, 在质量含气率 为0. 0 4 85~0. 7 9 60, S m i t h模型对于分层流误差为2 9. 2%, 环状流误差为1 8. 6%, 而改进模型对于分层流预测误差 1 0. 8 9%, 环状流误差为1 3. 3%, 大大提高了S m i t h模型的预测精度。

关键词: 含气率, 改进模型, 水平管, 气液两相流

Abstract: In consideration of the bubble in the film of annular flow and the droplet in the gas core, the previous model of Smith has been modified in order to predict the void fraction in horizontal pipes more accurately. During the gas quality range of 0.048 5~0.796 0, as to Smith model, the void fraction prediction error of stratified flow and annular flow was 29.2% and 18.6% respectively. On the contrary, as to stratified flow, the corresponding prediction error of the modified model was 10.89% and in annular flow the prediction error was 13.3%. The experimental results showed that the prediction accuracy was improved greatly compared with Smith model.

Key words: Void fraction,    , Modified model,    ,  Horizontal pipe,   , Gasliquid twophase flow

引用本文

陈 婧, 郑洪峰, 于英民. 一种改进的水平管气液两相流截面含气率预测模型[J]. 石油化工高等学校学报, 2015, 28(4): 86-90.

Chen Jing, Zheng Hongfeng, Yu Yingmin. A Modified Model for Void Fraction Prediction in Horizontal GasLiquid Pipe[J]. Journal of Petrochemical Universities, 2015, 28(4): 86-90.

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