Amistad油田海底采气设施热数值模拟

Félix Gallo Cruz, A. Sola, Joshua Andre Rosero, J. Gonzalez
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引用次数: 0

摘要

为避免固体沉淀物堵塞造成的非生产时间,对Amistad气田两条海底天然气生产流线进行了热数值模拟;由于该油田的作业条件和产气过程中记录的问题,对生产流体的热力学、热损失和多相行为进行全面研究,对于预防和控制固体形成和流动堵塞至关重要。从研究生产流体的压力-温度图开始,通过分析流体相的热学和输运特性来确定气体的热力学行为,以确定可能在流线内沉淀的固体类型(水合物)。采用数值和解析两种方法进行传热分析,数值方法采用计算流体力学(CFD)方法,并在ANSYS-CFX软件的支持下进行;从文献中得到的分析模型被用来验证它。多相流的水动力行为和压力损失由Beggs & Brill(1973)相关性确定,并与开源DWSIM软件工具性能进行对比。由于整体换热系数在CFD模拟中的重要性和影响,在继续进行数值模拟之前确定了总体换热系数。CFD模拟包括三个阶段:选择最优管道模型、网格细化和验证所开发的两相流换热现象模型。一旦通过稳态模拟定义了热损失模型,考虑到目前使用的标准管道和三种低导热聚合物作为替代材料,适当地代替碳钢或作为隔热涂层,进行瞬态模拟来计算气流突然停止情况下的气体冷却时间;这些是聚丙烯、聚氨酯和高密度聚乙烯。最后,选取文献中得到的5个水合物降水解析相关性和2条软件降水平衡曲线,利用模拟结果定义系统降水情景。根据P-T图,由于生产流体的组成和井的操作条件,唯一可能在钢管道中沉淀的固体是甲烷水合物。流线的热梯度是数值传热分析中最相关的结果,它显示了管道中流体达到最低温度的临界点,即水下水流的温度。根据产生的热梯度,从井口开始,两条钢丝的临界点为5560英尺,而第二条钢丝由于其长度限制,实际上要短一些,为5300英尺。通过对这些点的压力和温度条件的分析,建立了考虑所有平衡曲线的两种降水情景。然后,其中一种方案确认了该油田两条生产线中存在水合物,从而更清楚地认识到问题,包括发生降水的时间、距离以及压力和温度的关键条件。随后,将其他推荐材料的三种热损失分析与基本情况的结果进行比较,以确定最有效的管道配置,以避免水合物的形成,结论是,如果适当使用任何聚合物作为隔热材料或管道材料,则不会在整个管道中发生沉淀。此外,研究了多相流引起的水动力现象的影响,确定了雾流模式,其中流体的液相以小水滴的形式分散在气相中。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Thermal-Numerical Simulation of the Gas Offshore Production Undersea Facilities at the Amistad Field
Thermal numerical simulation of two undersea flowlines of natural gas production at Amistad field was developed in order to avoid non-productive time caused by plugging of solid precipitation; due to the operation conditions and recorded problems during gas production in this field, a complete study of thermodynamics, heat losses and multiphase behavior of the production fluid becomes imperative to prevent and control solid formation and flow blockage. The thermodynamic behavior of gas was analytically determined based on the thermal and transport properties of fluid phases, beginning with the study of the pressure-temperature diagram of the production fluid to define the type of solids that could precipitate within the flow lines (hydrates). The heat transfer analysis was determined applying two methods, one numerical and one analytical, the numerical by the computational fluid dynamics (CFD) method with the support of the ANSYS-CFX software; and the analytical model obtained from the literature that was used to validate it. The hydrodynamic behavior of multiphase flow and pressure losses were determined by the Beggs & Brill (1973) correlation and were contrasted with the open source DWSIM software tool performance. The overall heat transfer coefficient was determined before continuing with the numerical modeling due to its importance and influence in the CFD simulation, which covers three stages: selection of the most optimum pipeline model, mesh refining, and validation of the developed model for a heat transfer phenomenon in two-phase flow. Once the heat loss model was defined by a steady state simulation, a transient simulation was carried out to calculate the gas cooling time in a case of sudden flow shutdown, considering the standard pipe currently used and three polymers of low thermal conductivity as proposed alternate materials instead of carbon-steel or as or as thermal insulation coatings, as appropriate; these are polypropylene, polyurethane and high density polyethylene. Finally, five analytical correlations of hydrate precipitation obtained from the literature and two software precipitation equilibrium curves were selected to define the precipitation scenarios of the system using the simulation results. According to the P-T diagram, the only solids that could be precipitated in the steel pipelines are methane hydrates due to the composition of the production fluid and the operating conditions of the wells. The thermal gradient of the flowlines is the most relevant result of the numerical heat transfer analysis, this one shows the critical points of the pipes where the fluid reaches its lowest temperature, that is, the temperature of the underwater current. The critical point from the wellhead for both steel lines is 5560 [ft] according to the resulting thermal gradient, although for the second line, it is actually a bit shorter due to its length limit, 5300 [ft]. From the analysis of pressure and temperature conditions at these points, two scenarios of precipitation were established considering all the equilibrium curves. Then, one of the proposed scenarios confirmed the presence of hydrates in these two production lines of the field, providing a clearer realization of the problem that includes the time, distance and critical conditions of pressure and temperature where precipitation occurs. Subsequently, the three analyzes of heat loss of the other proposed materials were compared with the results of the base case to determine the most effective pipeline configuration to avoid the formation of hydrates and it was concluded that precipitation will not occur throughout the entire flowline if any of the polymers is applied as thermal insulator or pipe material, as appropriate. In addition, the effects of the hydrodynamic phenomenon caused by the multiphase flow were studied, determining a mist flow pattern, where the liquid phase of the fluid is dispersed within the gaseous phase in the form of small water droplets.
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