为霍尔果斯天然气凝析油加工厂的三相卧式智能分离器选择最佳尺寸

Fenk A. Sulaiman, H. Sidiq
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引用次数: 0

摘要

伊拉克 Khor Mor 天然气凝析油加工厂目前正面临运营挑战,原因是高溶解性碳氢化合物液体进入甜化塔,导致塔内出现泡沫问题。问题的根本原因可能是由于工厂内的分离容器无法从气相中去除液滴而导致的液体携带。本研究采用 Aspen HYSYS v.11 软件来研究 Khor Mor 甜化塔上游的 Bravo #2 工业三相卧式分离器在当前和未来运行条件下的性能。关于气体产品中液滴大小分布和气液分离效率的模拟结果表明,无论是否使用除雾器,分离器都无法消除气相中所有特定大小的液滴,从而满足效率要求。因此,对容器的各种结构参数进行了分析,以确定它们对携带液体质量流量和容器气/液效率的影响。研究结果为 Bravo #2 推荐了一种新的设计概念,称为 "智能分离器",适用于当前和预期的运行情况。智能分离器显著提高了气/液分离效率,在现有和未来运行条件下分别提高了 21.31% 和 24.02%。事实证明,这种创新设计能有效控制液体带入并保持高效率水平,即使容器入口流速随着时间的推移而增加也是如此,从而防止了下游工艺中因液体带入而产生的起泡现象。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Selecting Optimum Dimensions for a Three-Phase Horizontal Smart Separator for Khor Mor Gas-Condensate Processing Plant
The Khor Mor gas-condensate processing plant in Iraq is currently facing operational challenges due to foaming issues in the sweetening tower caused by high-soluble hydrocarbon liquids entering the tower. The root cause of the problem could be liquid carry-over as the separation vessels within the plant fail to remove liquid droplets from the gas phase. This study employs Aspen HYSYS v.11 software to investigate the performance of the industrial three-phase horizontal separator, Bravo #2, located upstream of the Khor Mor sweetening tower, under both current and future operational conditions. The simulation results, regarding the size distribution of liquid droplets in the gas product and the efficiency gas/liquid separation, reveal that the separator falls short of eliminating all liquid droplets of specified sizes from the gas phase to meet efficiency requirements, weather with or without a mist extractor. Consequently, an analysis of various structural parameters of the vessel is undertaken to determine their impact on the carried-over liquid mass flow rate and the vessel’s gas/liquid efficiency. The findings recommend a new design concept termed the "smart separator" for Bravo #2, applicable to both current and anticipated operational scenarios. The smart separator demonstrates a remarkable enhancement in gas/liquid separation efficiency, showcasing improvements of 21.31% and 24.02% under existing and future operating conditions, respectively. This innovative design proves effective in controlling liquid carry-over and maintaining high-efficiency levels, even as vessel inlet flow rates increase over time, thus preventing foaming phenomena in downstream processes caused carried-over liquids.
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