• CN：11-2187/TH
• ISSN：0577-6686

• 交叉与前沿 •

### 基于单V锥节流装置的湿气气液流量在线测量

1. 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. 中国石油新疆油田分公司采气一厂 克拉玛依 834007
• 出版日期:2016-04-15 发布日期:2016-04-15
• 作者简介:贺登辉,男,1986年出生,博士研究生。主要研究方向为多相流流动与测量。E-mail：hedhui@foxmail.com ;白博峰(通信作者),男,1971年出生,博士,教授,博士研究生导师。主要研究方向为石油工程多相流、多相流动与传热传质。E-mail：bfbai@mail.xjtu.edu.cn
• 基金资助:
国家自然科学基金资助项目(51276140)

### Online Measurement of Gas and Liquid Flow Rate in Wet Gas Base on Single V-cone Throttle

HE Denghui1, ZHANG Feng2, CAO Honggui2, YANG Yuanyuan2, BAI Bofeng1

1. 1. State Key Laboratory of Multiphase Flow in Power Engineering, Xi’an Jiaotong University, Xi’an 710049;
2. Frist Gas Production Factory, PetroChina Xinjiang Oilfield Branch Company, Karamay 834007
• Online:2016-04-15 Published:2016-04-15

Abstract: The two-phase mass flow coefficient is proposed to correct the deviation of the V-Cone meter when it is used to measure the wet gas. The effects of the Lockhart-Martinelli parameter, the gas densiometric Froude number and the gas to liquid density ratio on the two-phase flow coefficient are experimentally investigated. The diameter ratio of the V-Cone meter is 0.55. The experimental fluids are air and tap water. The gas to liquid density ratio, the gas densiometric Froude number and the Lockhart-Martinelli parameter range from 0.002 445 to 0.006 083, from 0.3 to 2.0 and from 0.01 to 0.34, respectively. The results show that the two-phase mass flow coefficient linearly increases with the Lockhart-Martinelli parameter and is affected by the gas densiometric Froude number and the gas to liquid density ratio. Then the quantitative relationship between the two-phase mass flow coefficient and the Lockhart-Martinelli parameter, the gas densiometric Froude number and the gas to liquid density ratio is obtained, based on which the correlation for the wet gas flow measurement is developed. The differential pressure response of the front and back cone of the V-Cone to the wet gas is investigated and the parameters affecting the different responses are also discussed, and finally the wet gas correlation to meter the gas and liquid mass flow rate is concluded. In the present cases, the relative error of the gas mass flow rate predicted by the correlation is within ±5.0% and the average relative error is 2.2%; the relative error of the liquid mass flow rate predicted by the correlation is within ±20.0% and the average relative error is 9.8%. The method proposed in this study possesses some remarkable performances, including simple structure, low cost and high accuracy.