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A Novel Approach to Maximize Hydrocarbon Liquids Recovery in Gas Compression Systems

机译:一种新的气体压缩系统中烃液体恢复的新方法

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This paper evaluates a technical new approach to establish the optimum operating conditions of associated gas multistage compression systems. The target is to maximize the total steady-state hydrocarbon (HC) liquids recovery of the surface producing facilities utilizing available resources and without any the need for plant modification. Maximizing liquids removal from associated gas has several benefits to gas-oil separation plants (GOSPs) such as increasing crude oil throughput, exporting leaner gas through pipelines in addition to other advantages that will be highlighted through two implemented case studies: 1. Abu Ali Plant (Arab Extra Light crude oil producing facility). 2. Manifa Central Processing facility (Arab Heavy crude oil producing facility). The concept is basically to raise the after-cooler's operating temperature (minimize cooling) of the lower pressure compression stages, to enable shifting rich/heavier gas to the optimum side where it is more favorable for the HC heavy ends to coalesce and condense. At that point, the after-cooling is maximized to collect the liquids from the discharge knockout (KO) drum of the highest pressure compression stage. This setup, when compared to conventional setup, which is maximizing the cooling across all stages, yields higher overall HC liquid recovery from the associated gas. In case study #1, where condensate removed from the gas compression plant is normally spiked in the crude production, this approach was evaluated and field tested, resulting in gain of 2,000 barrels per day in export crude for the same GOSP feed rate. In addition, 50% drop in export gas water load and 25% drop in the HC's dew point was achieved, which helps mitigating pipeline corrosion and slugging issues in export gas transport, given the unavailability of a gas conditioning system in the facility. In case study #2, where condensate removed from the gas compression plant is segregated and shipped to downstream facilities, this approach was evaluated, field tested and resulted in a gain of approximately 5,000 barrels per day in export condensates for the same GOSP feed rate. This gain resolved a chronic low velocity issue in the export condensate pipeline and helped mitigate water, solids settling and associated corrosion problems in the pipeline as well as downstream facilities upsets.
机译:本文评估了建立相关气体多级压缩系统的最佳运行条件的技术新方法。目标是利用现有资源和无需植物改性,最大化总稳态烃(HC)液体恢复的表面生产设施。最大化从相关气体中去除的液体对燃气 - 油分离植物(GOSP)具有几种益处,例如越来越多的原油产量,除了通过两种实施的案例研究将突出的其他优点外,通过管道出口稀释剂气体:1。阿布阿里植物(阿拉伯额外的浅色原油生产设施)。 2.司法中央加工设施(阿拉伯重型原油生产设施)。该概念基本上是提高较冷却器的后压压缩阶段的操作温度(最小化冷却),以使得将富含/较重的气体转化为最佳侧,在那里它更有利地对HC重对端聚结和冷凝。此时,后冷却最大化以从最高压力压缩级的排出敲除(KO)鼓中收集液体。该设置与传统设置相比,该设置最大化在所有阶段的冷却,从相关气体中恢复更高的总HC液体。在研究中,在从气体压缩装置中除去的冷凝物通常在粗产量中掺入,评价该方法并测试了田间,导致每天2,000桶的增益,在出口原油中出现同一GSP饲料速率。此外,在鉴于设施中的燃气调节系统不可用的情况下,实现了出口气体载荷和25%的液体露点下降的25%下降,这有助于降低出口气体运输中的管道腐蚀和折叠问题。在研究#2的情况下,在从气体压缩设备中除去的冷凝物被隔离并运输到下游设施,这种方法被评估,现场测试,导致出口凝结液的出口冷凝器中约5,000桶的增益,以获得相同的GSP饲料速率。这一增益解决了出口冷凝水管道中的慢性低速问题,并帮助减轻了水,固体沉降和管道中的相关腐蚀问题以及下游设施的扰乱。

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