mexilh现场作业的流动保证问题

Jorge Fernando Lorenzeti Canato, Christiano Da Silva Alves, Thales Barbosa Marques
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摘要

本文介绍了在mexilh气田作业中与流动保障相关的主要问题。mexilh位于巴西Santos盆地,通过海底歧管从7口气井输送到固定平台。井的平均水深约为470米,平台水深为172米。管汇与平台之间的回接长度为22公里,由两条直径为12英寸的生产管道连接。产液的热-水力剖面进入水合物形成区域,注入水合物热力学抑制剂(MEG)以防止水合物形成。这些MEG在平台上回收,然后重新注入井中。安装在水下管汇上的计量阀可为每口井分配所需的MEG用量。在8年的运行中,未见水合物堵塞造成产量损失的报道。本文还介绍了mexilh海底系统的蜡沉积管理方法。虽然预计会有一定数量的蜡沿管道积聚,但清管器运行后发现的蜡很少。据观察,蜡出现在平台工艺装置,但它似乎不积累在管道。清管器下入仅用于腐蚀监测。这里讨论的另一个问题是防垢,可以通过井下抑制剂注入来实现,但直到今天才需要。最后给出了瞬态仿真结果,对提高气体流量的操作过程具有指导意义。由于平台上没有段塞流捕集器,因此,为了避免由于大量液体段塞流到达工艺装置而导致关闭,必须仔细执行增加气体流量的程序。
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Flow Assurance Issues on Mexilhão Field Operation
This paper shows the main concerns related to Flow Assurance during Mexilhão gas field operation. Mexilhão is located in Santos Basin, Brazil and flows from seven gas wells to a fixed platform through a subsea manifold. Well’s water depth average is about 470 meters and platform’s water depth is 172 meters. The tieback between the manifold and platform is 22 kilometers and there are two production pipelines of 12-inch diameter connecting them. The thermo-hydraulic profile of the production fluid enters in hydrate formation region and hydrate thermodynamic inhibitor (MEG) is injected to prevent hydrate formation. This MEG is recovered at the platform and it is reinjected in the wells. Dosing valves located at subsea manifold distributes the desirable quantity of MEG for each well. During eight years of operation, no production loss caused by hydrate blockage has been reported. This paper also shows the method of wax deposit management in Mexilhão subsea system. Although certain amount of wax had been anticipated to accumulate along pipeline, very little wax was found after pig runs. It has been observed that wax appears in platform process plant, however it does not seem to accumulate in the pipeline. Pig runs occur only for the purpose of corrosion monitoring. Another item discussed here is scale prevention, which could be performed with downhole inhibitor injection and it has not been required until today. Finally, transient simulation results which guided the operational procedure to increase gas flow rate are shown. There is no slug catcher at the platform, then, in order to avoid shut downs due to large liquid slug arrival at process plant, the procedure to increase gas flow rate must be performed carefully.
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