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Liquid inventory and three phase surge wave data from the Midgard gas condensate fields in the North Sea

机译:北海Midgard凝析气田的液体清单和三相浪涌数据

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This paper presents data from the Midgard gas condensate field in the North sea. The production is tied back to Asgard B. Field tests were conducted to measure the accumulation of water/MEG and condensate volumes in two 20" flowlines at different production rates. Here, data from one of these flowlines are presented. During reduced rates when liquid starts to accumulate in the flowlines, long liquid surge waves are experienced topside. The onset of the surges is well inside the friction dominated pressure drop domain. The surges are separated into two parts, a condensate surge followed by a water/MEG surge. The duration and frequency of the surges varies. Up to 2 hour long surges are observed. Likewise, the time period between each surge varies considerably. Only quite small pressure fluctuations (~1 bar) are recorded at the well heads when the surges propagate through the ~300 m high riser. Only a minor effect is seen on the pressure before the topside chokes. The gas flow rate is reduced somewhat during the arrival of the surges. To the authors knowledge the mechanism behind the three phase surge waves is poorly understood. The surge wave regime causes problems for the operation topside. It is especially the handling of the water/MEG phase which reaches its limit when the surges become too large. This defines the minimum turn down rate for the flowlines. One has also experienced problems with hydrate formation in the periods between each surge. During the liquid accumulation period no liquid water/MEG phase arrives topside. The likely scenario is that hydrate particles are formed as water condenses out when the gas propagate through the riser and experiences Joule Thompson cooling due to the pressure drop. The hydrate particles can then clog small bore piping topside.
机译:本文介绍了北海Midgard凝析气田的数据。该生产与Asgard B息息相关。进行了现场测试,以测量不同生产率下两条20“流水线中水/ MEG和冷凝水体积的累积。此处显示了其中一条流水线的数据。开始在流动管线中积聚,在顶部经历了长的液体浪涌波,浪涌的开始点在以摩擦为主的压降域之内,浪涌被分为两部分,冷凝浪涌和水/ MEG浪涌。浪涌的持续时间和频率各不相同,最多可观察到2小时的浪涌,同样,每次浪涌之间的时间间隔也有很大变化,当浪涌在整个井壁中传播时,在井口仅记录到很小的压力波动(〜1 bar)。大约300 m高的立管,仅对顶侧节流阀前的压力产生微小影响,在波涌到来时气体流速有所降低。人们对三相电涌波背后的无知还缺乏了解。浪涌状态会给操作顶部带来问题。当浪涌变得太大时,尤其是水/ MEG相的处理达到了极限。这定义了出油管线的最小下调速率。在每次波动之间的一段时间内,人们也遇到了水合物形成的问题。在液体积累期间,没有液态水/ MEG相到达顶部。可能的情况是,当气体通过立管传播并由于压力下降而经历焦耳汤普森冷却时,水冷凝时会形成水合物颗粒。然后,水合物颗粒会堵塞小口径管道的顶部。

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