海上天然气平台设施有效单乙二醇Meg注入优化:夏季和冬季作业水合物控制的新案例研究

Salu A. Samusideen, Mohammed Abdo Alwani, A. Kurdi
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摘要

本文的目的是展示五种操作水合物抑制系统的创新选择,旨在消除未来湿法天然气生产的限制,并在25年的生命周期内优化资本和运营成本。在冬季,将单乙二醇(MEG)注入海上气田的湿天然气干线中,作为水合物抑制的一种手段。使用过的MEG应该在陆上天然气厂的MEG再生装置(MRU)中回收,在那里湿天然气被进一步处理。为了达到特定的MEG纯度,MRU在生产中经常面临挑战,这导致将稀释的MEG溶液注入海上系统,从而降低了湿式天然气的最大允许生产能力。本文从五个不同的选项来描述研究。方案1代表了当前的运行方案,即在MRU服务的情况下维持现有系统,而方案2则探讨了关闭陆上天然气厂的MRU,并在冬季从天然气厂向海上平台泵送新的MEG。选项3是关闭天然气厂的MRU,在冬季从岸上的海滩阀门站(BVS)泵送新鲜MEG。选项4探索在MRU服役的情况下维持现有系统,并升级储罐,以解决富MEG流的非稳态特性。方案5探讨了在冬季从燃气厂抽出稀MEG,将富含MEG储存在储罐中进行MEG再生,并在夏季通过现有系统回收MEG,包括将稀MEG储存在储罐中以供冬季使用。评估结果表明,与方案1相比,方案2和方案3可以在较低的MEG注入速率和较低的生命周期成本(LCC)下轻松满足冬季所需的水合物抑制规格。评估还表明,与方案1不同,方案4和方案5将确保MRU的运行不会因MEG储罐中的低水平而中断,并将在干线中保持高纯度的MEG。综上所述,方案5具有最低的LCC,这是最具经济吸引力的方案。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Effective Mono Ethylene Glycol Meg Injection Optimisation at Offshore Gas Platform Facility: A Novel Case Study for Hydrate Control During Summer and Winter Operation
The objective of this paper is to show five innovative options of operating the hydrate inhibition system which aims to eliminate future wet natural gas production limitations and optimize capital and operation expenses during a 25-year life cycle period. Mono-Ethylene Glycol (MEG) is injected in wet natural gas trunk lines from an offshore gas field, as a means of hydrate inhibition during the winter season. The used MEG is supposed to be recovered in MEG Regeneration Unit (MRU) at onshore gas plant, where the wet natural gas is further processed. The MRU often faces challenges in producing to achieve specified MEG purity, which consequently results in injecting a diluted solution of MEG into the offshore systems, and thereby lowering the maximum allowable production capacity of wet natural gas. This paper describes the study in five different options. Option 1 represents the current operating scenario of maintaining the existing system with MRU in service, while option 2 explores shutting down MRU at onshore gas plant, and pumping fresh MEG during winter days from the gas plant to the offshore platforms. Option 3 explores shutting down MRU at the gas plant and pumping fresh MEG during winter days, but from a Beach Valve Station (BVS) at an onshore location. Option 4 explores maintaining the existing system with MRU in service and upgrade the storage tanks to address the unsteady state nature of rich MEG flow. Option 5 explores pumping lean MEG during winter days from the gas plant, storing rich MEG in tanks for MEG regeneration and reclaiming MEG through the existing system during the summer including storing lean MEG in tanks for winter usage. The evaluation has shown that options 2 and 3 can easily meet the required hydrate depression specification during winter period, at far lower MEG injection rates and at a substantially lower life cycle cost (LCC) compared to option 1. The evaluation also showed that options 4 and 5 will ensure MRU operation not interrupted due to low-low levels in MEG storage tanks and will maintain high purity MEG in the trunk lines, which is different from option 1. In conclusion, option 5 has the lowest LCC which is the most economically attractive option.
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