基于主支管合流模型的天然气水合物相平衡研究

S. Deng, Yali Liu, Xia Wei, L. Tao, Yanfeng He
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引用次数: 0

摘要

相变是制约天然气水合物开发的主要因素,易造成完井段(筛孔段-提井段)堵塞,造成工程损失。针对前人对裸眼完井技术下天然气水合物压降法开采完井段汇合机理研究的缺陷,本文将完井段天然气水合物流动简化为主支管汇合模型。首先,建立物理模型。在能量守恒定律和Peng-Robinson方程的基础上,推导了温度-压力耦合模型。然后,利用Fluent软件模拟了Main-Branch模型中温度梯度和压力梯度的变化。得到了不同流速下的天然气水合物相图和P-T环境。最后,对理论模型与数值模拟进行对比分析,对所建立的模型进行了验证。通过本文的研究,可以通过降压的方式防止完井段堵塞,为降压提取天然气水合物时压降的控制提供理论指导。这对后期天然气水合物的开采和连续生产具有重要意义。
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Study on the Phase Equilibrium of Gas Hydrate Based on Main-Branch Pipe Confluence Model
Phase change, a major factor that restricts the development of gas hydrate, is likely to cause blockage in well completion section (sieve section – wellbore lifting section), thus resulting in the engineering losses. In view of the defects in the previous studies on the confluence mechanism of completion section of gas hydrate pressure drop method mining under openhole completion technology, the flow of gas hydrate in the well completion section was simplified as the Main-Branch pipe confluence model in this paper. Firstly, a physical model was established. On the basis of the energy conservation law and the Peng-Robinson equation, the temperature and pressure coupling model was also derived. Then, the Fluent software was used to simulate the temperature gradient and pressure gradient changes in the Main-Branch model. The gas hydrate phase diagram and P-T environment under different velocity were obtained. Finally, the contrast analysis between theoretical model and numerical simulation was carried out and the established model was verified. Through the study of this paper, it is possible to prevent blockage of the well completion section by means of depressurization, which can provide theoretical guidance for the control of pressure drop when gas hydrate is extracted by depressurization. It is important for the exploitation and continuous production of gas hydrate in the later stage.
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