正方形截面直通道内二次流现象的实验研究

郭亚军 1; 2; 毕勤成 1; 何永清 1

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正方形截面直通道内二次流现象的实验研究

更新时间：2025-07-09

- 正方形截面直通道内二次流现象的实验研究
- Experimental Investigation on Secondary Flow of Air-Water Two-Phase Flow in Straight Channel with Square Cross-Section
- 西安交通大学学报 2009年43卷第7期页码：83-87
- 作者机构：
  
  1. 西安交通大学动力工程多相流国家重点实验室,西安,710049
  2. 西安建筑科技大学环境与市政工程学院,西安,710055
- 作者简介：
- 基金信息：
  
  : 2008-10-15. 作者简介: 郭亚军(1966-),女,博士生;毕勤成(联系人),男,教授. 基金项目: 国家自然科学基金资助项目(50176039)
- DOI：
  中图分类号： TL334
- 网络首发：2009-07-10，
  
  纸质出版：2009
- 稿件说明：
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郭亚军 1, 2, 毕勤成 1, 等. 正方形截面直通道内二次流现象的实验研究[J]. 西安交通大学学报, 2009,43(7):83-87.

Experimental Investigation on Secondary Flow of Air-Water Two-Phase Flow in Straight Channel with Square Cross-Section[J]. 2009, 43(7): 83-87.
郭亚军 1, 2, 毕勤成 1, 等. 正方形截面直通道内二次流现象的实验研究[J]. 西安交通大学学报, 2009,43(7):83-87. DOI：

Experimental Investigation on Secondary Flow of Air-Water Two-Phase Flow in Straight Channel with Square Cross-Section[J]. 2009, 43(7): 83-87. DOI：

摘要

以空气-水为介质

通过可视化实验的方法

对边长为10 mm的正方形截面通道内空气-水垂直上升流动的两相流流型进行了实验研究

表观气速为0.04～100 m/s

表观水速为0.001～6 m/s.观察到了正方形截面通道内两相流动的典型流型

通过管外可视化及内视镜伸入管道内拍摄到清晰的环状流和爬动流流型

证实了正方形截面直通道内存在“二次流”现象

且对气-液两相流动的相分布有较大影响.将正方形截面爬动流与圆通道内的溪状流进行了比较

由于其中的作用力不同

它们在发生条件、流动形态及液膜形状上有很多异同点

圆通道内溪状流的液膜是随机出现和分布的

数条液带、液丝的位置不确定

尺寸相差悬殊.利用单能γ射线传感器测量了正方形通道内爬动流及环状流的液膜厚度

得到壁面上液膜厚度的分布图

证明了正方形通道内随着表观气速的增大

二次流作用逐渐增强

使得壁面上液膜分布的不均匀

壁面中心处液膜最厚.

Abstract

An experimental investigation was conducted on the vertically upward flow of air-water two-phase in a channel with a square cross-section. The hydraulic diameter of the channel was 10mm; the superficial air velocity was 0.04-100m/s; the superficial water velocity was 0.001- 6 m/s. The typical flow patterns

creep flow and rivulet flow

were observed by flow visualization with a DV camera and an endoscope

and the flow pattern map and flow pattern transition boundaries were obtained. The thickness of liquid film of the creep flow and the annular flow in the square channel was measured by a γ-ray instrument. The results show that the mechanism to form the creep flow in the square channel is different from that to form the rivulet flow in a circular tube and a secondary flow exits in the square channel. The phase distribution on the inner wall of the noncircular channel indicates that the influence of the channel geometry results in the steeper radial distribution of the phases and velocities

and eventually turbulent secondary flow. With the increase in the gas velocity

the film thickness at center of the wall is greater than that at corner

indicating the significant effect of the secondary flow on the phase distribution in the noncircular channel.

关键词

Keywords

references

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ALY M, TRUPP A, GERRARD A. Measurements and prediction of fully developed turbulent flow in an equilateral triangular duct [J]. J Fluid Mech, 1978, 85(1): 57-83.

HUSER A, BIRINGEN S, HATAY F F. Direct simulation of turbulent flow in a square duct: Reynolds-stress budgets [J]. Phys Fluids, 1994, 6(9): 3144-3152.

HIROTA M, FUJITA H, YOKOSAWA H, et al. Turbulent heat transfer in a square duct [J]. Int J of Heat and Fluid Flow,1997, 18(1): 170-180.

VÁZQUEZ M S, MÉTAIS O. Large eddy simulation of the turbulent flow through a heated square duct [J]. J Fluid Mech,2002, 453: 201-238.

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WÖIK G,DREVER M,RATH H J.Flow patterns in small diameter vertical non-circular channels [J]. Int J of Multiphase Flow,2000, 26(6): 1037-1061.

郭亚军,毕勤成,何永清.空气-水在垂直非圆截面通道内流型研究[J]. 核动力工程,2006, 27(5): 48-52.

GUO Yajun, BI Qincheng, HE Yongqing, et al. Flow patterns of air-water two-phase flow in vertical noncircular channels [J]. Nuclear Power Engineering, 2006, 27(5): 48-52.

BARAJAS A M, PANTON R L. The Effect of contact angle on two-phase flow in capillary tubes [J]. Int J of Multiphase Flow, 1993, 19(2): 337-346.

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