Modelling Elemental Mercury Partitioning and Transport: A Case Study of Fenris: A New Offshore High Pressure, High Temperature Gas-Condensate Field

A. R. Farrell, D. Frigo, G. Graham, B. Hugaas, Christian Vikre, J. Carney, Paul Kirchner
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Abstract

Mercury is highly toxic and corrosive to certain metals and is therefore a highly undesirable contaminant in produced hydrocarbons. Its concentration in reservoir fluids differs by over four orders of magnitude globally, which means its operational consequences can differ enormously. We present a case study of the Fenris field: a new, offshore HPHT gas-condensate tieback to Valhall (North Sea) in which mercury has been detected but there remains considerable uncertainty about its abundance in the fluids. Predictions from a cubic Equation of State (EoS) model are strongly dependent on the parameter set chosen and there is not common agreement within the industry on the most suitable. Prior to field simulations, the suitability of commercially available models was evaluated by comparing outputs with literature data. Once a suitable EoS parameter set was selected, partitioning of Hg0 over all possible phases (gas, condensate, MEG-water and liquid Hg0) was evaluated for a variety of Hg0 concentrations (due to the uncertainty thereof), as well as the influence of conditions both in the subsea flowline and in the facilities. A plausibly conservative base case was selected for the Hg0 concentration in the reservoir fluids. This allowed partitioning and transport of Hg0 to be evaluated in terms of both the quantity and concentration of Hg0 in each produced fluid stream. Specifications for mercury-removal units (MRUs) were initially set using these values. A set of simulations performed using a higher Hg0 concentration allowed for evaluation of the suitability of these values under worst-case conditions. Considerable seasonal variation was anticipated, with the fluid arrival temperature at the facilities expected to fluctuate between 0 and 10 °C with related changes in the Hg partitioning. It was identified that the greatest quantity of liquid Hg0 was expected to form in the flowline and facilities at around Year 3 following First Gas, consistent with the maximum gas rate expected over field life and winter conditions. Of particular interest is the influence of the condensation and agglomeration kinetics of liquid Hg0, which may not only change the locations where the liquid accumulates but can also affect Hg0 partitioning into the other produced phases and can therefore affect the sizing of any MRUs to achieve product specification for this contaminant. This work describes the challenges in predicting the consequences of mercury production at FEED when its expected Hg0 concentration is significant-to-high but substantially uncertain. A conservative approach was taken in modelling quantities at various locations to ensure risk is suitably managed without adopting design specifications that unduly increase capital expenditure. The paper describes the predicted risks associated with Hg0 in this new development and the steps identified to manage risks during the upcoming production stage.
元素汞的分配和输运建模:以海上高压高温凝析气田Fenris为例
汞对某些金属具有剧毒和腐蚀性,因此在生产的碳氢化合物中是非常不受欢迎的污染物。在全球范围内,它在储层流体中的浓度相差超过4个数量级,这意味着它的操作后果可能会有很大差异。我们介绍了Fenris油田的一个案例研究:在Valhall(北海)的一个新的海上高温高压凝析气回接中,已经检测到汞,但流体中的汞含量仍然存在相当大的不确定性。三次状态方程(EoS)模型的预测很大程度上依赖于所选择的参数集,而且业内对最合适的参数集没有普遍的共识。在现场模拟之前,通过将输出结果与文献数据进行比较来评估商业可用模型的适用性。一旦选择了合适的EoS参数集,就会根据各种Hg0浓度(由于其不确定性)以及海底管线和设施条件的影响,评估Hg0在所有可能相(气、凝析液、MEG-water和液态Hg0)上的分配情况。为储层流体中的Hg0浓度选择了一个看似保守的基准情况。这样就可以根据每个产出流体中Hg0的数量和浓度来评估Hg0的分配和输送。汞去除装置(mru)的规格最初是使用这些值设定的。使用较高的Hg0浓度进行的一组模拟可以评估这些值在最坏情况下的适用性。预计会有相当大的季节变化,到达设施的流体温度预计在0至10°C之间波动,并伴随汞分配的相关变化。研究发现,在第一次天然气开采后的第3年左右,预计在流水线和设施中形成最大数量的液态Hg0,这与整个油田寿命和冬季条件下的最大产气量一致。特别令人感兴趣的是液态Hg0的冷凝和团聚动力学的影响,这不仅可能改变液体积聚的位置,而且还可能影响Hg0分配到其他生产相,因此可能影响任何mru的尺寸,以达到该污染物的产品规格。这项工作描述了当预期的Hg0浓度从显著到高但基本上不确定时,在FEED预测汞生产后果时所面临的挑战。在不同地点的建模数量方面采取了保守的方法,以确保风险得到适当管理,而不会采用过度增加资本支出的设计规范。本文描述了在这一新开发中与Hg0相关的预测风险,以及在即将到来的生产阶段确定的风险管理步骤。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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