油水处理凝聚柱倾角影响的计算流体力学分析

R. D. A. Albuquerque, M. C. Souza, J. G. O. Marinho, L. M. T. D. Oliveira
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引用次数: 0

摘要

在用于油水分离的设备中,床层聚结器是最引人注目的。即使经过数十年的地层聚结剂开发,一些变量(如仪器倾角)在其行为中的作用仍未在现场得到充分探讨。因此,利用ANSYS CFX 13.0软件,建立了床层凝聚器倾角对采出水油分离速率影响的模型。该软件分析相对于水平轴的四种倾角(0°,15°,30°和60°)。模拟结果确定了油气聚集带和再循环带的存在。研究人员还比较了整个设备在所有倾角下的压降,注意到当床层处于水平状态时,会出现更有利的状态,表现出更高的油藏、更小的涡度和更低的压降。当倾角为60°时,分离效率较低,压降较大,湍流效应较强。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
ANALYSIS OF THE INCLINATION INFLUENCE IN A COALESCER COLUMN FOR OIL/WATER TREATMENT VIA COMPUTATIONAL FLUID DYNAMICS
Among the equipments used in the separation of water from oil, bed coalescers stands out. Even after decades of bed coalescer development, the role of some variables, such as apparatus inclination, in its behavior remains underexplored within the field. Thus, using the ANSYS CFX 13.0 software, a modeling was proposed to determine the influence of bed coalescer inclination in the separation rate of oil from produced water. The software analyzes four inclinations relative to the horizontal axis (0°, 15°, 30° and 60°). The results from simulations identified oil accumulating zones and presence of recirculation zones. It also compared the pressure drop throughout the apparatus in all inclinations established, noting that a more favorable state occurs when the bed is at horizontal, presenting higher oil accumulation, fewer vorticity, and lower pressure drop. The less desirable scenario occurs with 60° inclination, displaying a lower separation efficiency, greater pressure drop, and higher turbulence effect.
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