海底油水散装分离新型并联管式分离器设计试验研究

H. S. Skjefstad, M. Stanko
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引用次数: 5

摘要

随着油田的成熟,生产流的采出水含量往往会随着时间的推移而增加,采出水管理最终将成为生产的瓶颈。采出水的海底分离可以延长棕地装置的使用寿命,提高采收率,提高能源效率。此外,海底水分离的实施还将使未来与现有设施的连接成为可能,并减少对昂贵的新运输线路的需求。现有的海底采出水散装分离器技术仅限于重力和紧凑型重力容器,如Troll和Tordis,以及Marlim管道分离器。这些都是大型装置,制造、运输和安装成本很高。此外,重力式和紧凑型重力船不适合深水安装,因此需要新颖的解决方案来减轻散装水分离器的重量和尺寸,从而使该技术对新的商业案例更具吸引力。为了研究改进的海底散水分离技术,挪威科技大学(NTNU)开发了一种多相油水测试回路。设备测试流体为ExxsolD60和wt%3.4 NaCl的蒸馏水。本文提出了一种利用多个平行管道的新型分离器设计方案。与传统的重力技术相比,该设计可以减少大水深下所需的壁厚,缩短停留时间,从而缩短分离器长度。将报告构建的中等规模原型的初始性能数据,包括在一定流量范围内的分离效率估计,含水率(WC)和水提取率(ER)。在30%,50%和70% WC下,测试流量从250L/min到750L/min不等。水的提取率从50%到100%不等。基于最初的测试活动,该概念被证明是有希望的,在中等流速下,无论是水连续流还是油连续流,都显示出良好的分离效率(>98%)。在更高的流量下,性能会下降,为了保持高效率,必须限制水的提取率。在出水口的流动条件的照片包括,提供了一个可视化的发生两相流现象在分离器内。提出的概念增加了海底分离解决方案的扩展组合,并展示了利用平行管道实现油水分离的新方法。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
An Experimental Study of a Novel Parallel Pipe Separator Design for Subsea Oil-Water Bulk Separation
As oil fields mature, the produced water content of the production stream will often increase over time, and produced water management will eventually become a bottleneck in production. Subsea separation of produced water enables prolonged lifetime of brown field installations, increased recovery rates and more energy efficient production. In addition, implementation of subsea water separation will also enable future tie-ins to existing facilities, and reduce the need for new and expensive transport lines. Existing installed subsea produced water bulk separator technologies are limited to gravity and compact gravity vessels, such as Troll and Tordis, and the Marlim pipe separator. These are large installations, which are costly to manufacture, transport and install. In addition, the gravity and compact gravity vessels are not suited for deep-water installations, and there is a need for novel solutions to both reduce the weight and size of bulk water separators, making the technology more attractive for new business cases. In order to investigate improved subsea bulk water separation technologies, a multiphase oil-water test loop has been developed at the Norwegian University of Science and Technology (NTNU). Facility test fluids are ExxsolD60 and distilled water with wt%3.4 NaCl. In this paper, a new separator design, utilizing multiple parallel pipes will be presented. The design allows reduction of required wall thickness at large water depths, shorter residence times and hence a shorter separator length compared to traditional gravity based technologies. Initial performance data of a constructed medium scale prototype will be reported, including separation efficiency estimations over a range of flow rates, water cuts (WC) and water extraction rates (ER). Tested flow rates vary from 250L/min to 750L/min at 30%, 50% and 70% WC. Water extraction rates are varied from 50% to 100% of the inlet water rate. Based on this initial test campaign, the concept proves promising, displaying good separation efficiencies (>98%) for both water continuous and oil continuous inlet flows at moderate flow velocities. At higher flow rates, performance decreases, and water extraction rates must be limited in order to maintain high efficiencies. Photos of flow conditions at the water outlet are included, providing a visualization of the occurring two-phase flow phenomena inside the separator. The presented concept adds to an expanding portfolio of proposed subsea separation solutions, and displays a new way of utilizing parallel pipes to achieve oil-water bulk separation.
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