Optimization Strategies of Production Parameters to Prevent Hydrate Reformation in Marine Gas Hydrate Production System

Zheng Liu, Baojiang Sun, Zhiyuan Wang, Jianbo Zhang
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Abstract

In recent decades, the development of natural gas hydrates has become a research hotspot of scholars all over the world. However, the decomposed gas and water in marine gas hydrate production system may regenerate gas hydrates due to the low-temperature and high-pressure environment in seafloor. In this study, a transient temperature and pressure calculating model was established to predict the risk of hydrate reformation in production pipelines during offshore natural gas hydrate development. Using the proposed model, the region of hydrate reformation in gas hydrate production wells were predicted quantitatively. Meanwhile, the hydrate reformation management strategies through optimization of production design parameters in combination with hydrate inhibitor injection were proposed and discussed in detail. The results indicate that the risk of hydrate reformation is the highest in the drainage pipeline (DP); however, the flow in gas-water mixed transportation and gas production pipelines (MTP and GPP) basically does not satisfy the hydrate formation condition. In the process of production well design, adding additional the EH and ESP can fully eliminate the hydrate reformation risk in the DP without using the hydrate inhibitor.
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海洋天然气水合物生产系统中防止水合物重整的生产参数优化策略
近几十年来,天然气水合物的开发已成为世界各国学者的研究热点。然而,由于海底低温高压环境,海洋天然气水合物生产系统中分解的气和水可能会再生天然气水合物。为预测海上天然气水合物开发过程中生产管道水合物转化风险,建立了瞬态温度压力计算模型。利用该模型对天然气水合物生产井中水合物重整区域进行了定量预测。同时,通过优化生产设计参数,结合水合物抑制剂的注入,提出并详细讨论了水合物改造管理策略。结果表明:排水管道(DP)水合物重整风险最高;然而,气水混输产气管道(MTP和GPP)中的流量基本不满足水合物形成条件。在生产井设计过程中,在不使用水合物抑制剂的情况下,添加EH和ESP可以充分消除DP中的水合物重整风险。
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