水力旋流器
入口
计算流体力学
分离(统计)
石油工程
上游(联网)
雷诺应力
湍流
环境科学
工程类
海洋工程
重力分离
压力降
计算机模拟
工艺工程
机械
油井
吞吐量
石油
压力梯度
雷诺数
原油
作者
Yuvanesh Jeva,Mohammad Shakir Nasif
出处
期刊:
[Universiti Teknologi Petronas]
日期:2026-03-31
卷期号:8 (1): 20-20
标识
DOI:10.61762/pajevol10iss1art003
摘要
In the wide landscape of upstream oil production, an essential challenge engineers often face is the contamination of crude oil with impurities such as sand. The inevitable drawbacks of sand contamination, such as pig blockages and control valve failures, reinforce the necessity of separators. Various types of separators are used in industry to remove impurities, including three-phase separators, gravity separators, and hydrocyclone separators. Hydrocyclone is a very efficient alternative, with a simpler design and higher throughput capacity than its competitors. A computational fluid dynamics (CFD) analysis of the hydrocyclone solid separation efficiency is presented in this work. A research gap was identified: among the several structural parameters that affect a hydrocyclone’s separation efficiency, prior research on inlet angles is limited. This study investigates the effects of inlet angles on the performance of a hydrocyclone handling a crude oil–sand mixture, in contrast to previous studies that focused on other solid–liquid systems, such as water-based slurries. It aims to examine the effects of varying inlet angles on velocity and pressure distributions, pressure drop, and overall solid separation efficiency using the Reynolds Stress Model (RSM) turbulence model. The results compare different inlet angles and identify the optimal configuration that balances high sand separation efficiency with a stable pressure drop.
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