Modeling the pressure drop of wet gas in horizontal pipe

Peining Yu; Yi Li; Jing Wei; Ying Xu; Tao Zhang

doi:10.1016/j.cjche.2016.10.024

Your Location：

Home >

Browse articles >

Modeling the pressure drop of wet gas in horizontal pipe

Fluid Dynamics and Transport Phenomena | Updated：2026-01-06

- Modeling the pressure drop of wet gas in horizontal pipe
- Chinese Journal of Chemical Engineering Vol. 25, Issue 7, Pages: 829-837(2017)
- Affiliations：
  
  1. Graduate School at Shenzhen, Tsinghua University,Shenzhen,China,518055
  2. CFHI Tianjin C-E Electrical Automation Co. Ltd,Tianjin,China,300457
  3. School of Electrical Engineering and Automation, Tianjin University,Tianjin,China,300072
- Author bio：
- Funds：
- DOI：10.1016/j.cjche.2016.10.024
  CLC：
- Published：2017
- Accepted：
Scan QR Code
Peining Yu, Yi Li, Jing Wei, Ying Xu, Tao Zhang. Modeling the pressure drop of wet gas in horizontal pipe[J]. , 2017, 25(7): 829-837.
DOI：

Peining Yu, Yi Li, Jing Wei, Ying Xu, Tao Zhang. Modeling the pressure drop of wet gas in horizontal pipe[J]. , 2017, 25(7): 829-837. DOI： 10.1016/j.cjche.2016.10.024.

摘要

Abstract

A model for gas-liquid annular and stratified flow through a horizontal pipe is investigated

using the two-phase hydrokinetics theory. Taking into consideration the flow factors including the void fraction

the friction between the two phases and the entrainment in the gas core

the one-dimensional momentum equation for gas has been solved. The differential pressure of the wet gas between the two tapings in the straight pipe has been modeled in the pressure range of 0.1-0.8 MPa. In addition a more objective iteration approach to determine the local void fraction is proposed. Compared with the experimental data

more than 83% deviation of the test data distributed evenly within the band of ±10%. Since the model is less dependent on the specific empirical apparatus and data

it forms the foundation for further establishing a flow measurement model of wet gas which will produce fewer biases in results when it is extrapolated.

关键词

Keywords

references

Views

169

Downloads

CSCD

Alert me when the article has been cited

Submit

Tools

Publicity Resources

A general pressure drop model based on liquid holdup of gas-liquid flow in micro-packed beds

Viscous behavior of 1-hexyl-methylimidazolium bis(trifluoromethylsulfonyl)imide/titanium dioxide/polyethylene glycol

Experimental study on prediction model of wet gas pressure drop across single-orifice plate in horizontal pipes in the low gas phase Froude number region

Bubble dispersion intensification via flow guidance and drainage in a bubble column with internals

Variable pseudo-particle modeling for molecular dynamics simulation

Related Author

Junjie Wang

Lin Sheng

Jiang Deng

Guangsheng Luo

Yifeng Chen

Hang Yu

Jingjing Chen

Xiaohua Lu

Related Institution

The State Key Laboratory of Chemical Engineering, Department of Chemical Engineering, Tsinghua University

State Key Laboratory of Materials-Oriented Chemical Engineering, Nanjing Tech University

Energy Engineering, Division of Energy Science, Luleå University of Technology, Luleå

Shanghai Key Laboratory of Multiphase Flow and Heat Transfer in Power Engineering, School of Energy and Power Engineering, University of Shanghai for Science and Technology

Key Laboratory for Thermal Science and Power Engineering of Ministry of Education, Department of Energy and Power Engineering, Tsinghua University

⁰