水合物分布形态对含水合物沉积物气水输运影响的孔隙尺度模拟

Zhuoran Li, Jiahui You, G. Qin
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引用次数: 0

摘要

气、水输运行为是影响油气产量的关键因素之一,受含水合物沉积物孔隙特征和毛细作用的控制。水合物分布形态(HDM)能显著影响HBS的孔隙结构,影响气、水的相对渗透率。为了阐明HDM在微观尺度上的影响,建立了一个相场晶格玻尔兹曼(LB)模型来描述HBS中气体和水的输运。为了模拟存在明显密度和粘度差异的非混相流体的输运,建立了具有界面跟踪方程保守形式的相场LB模型,以抑制相界面处的杂散电流。为了描述流固相互作用,对固相(水合物和颗粒)均采用回弹条件来实现防滑条件,对颗粒和水合物采用润湿性条件来描述润湿性行为。为了提高数值稳定性,采用了多松弛时间(MRT)碰撞算子,并选择了梯度算子具有8阶精度的离散化方案。在这项工作中,我们首先通过应用几个基准案例来验证我们的模型,这些案例针对密度对比明显的流体,如分层Couette/Poiseuille流动、瑞利-泰勒不稳定性。在保证相同连通性的前提下,构建了具有不同水合物饱和度(Shyd)的孔隙填充和颗粒包覆HBS的合成几何形状。在此基础上,利用LB模型模拟了两种HDM工况下稳态相对渗透率测量和排水毛管压力测量过程。结果表明:在亲水HBS中,相同体积条件下,充孔情况下气体的相对渗透率明显大于包覆情况,充孔情况下可获得更大的毛管压力;此外,随着Shyd的增加,两种HDM情况下流体相对渗透率和毛细压力的差异会显著增强。由于HDM不仅可以影响孔隙空间结构,还可以通过形成不同润湿性的固体表面来影响多孔介质的润湿性,因此不同HDM情况下流体相的分布和输运会受到明显影响。本研究采用的相场LB模型能够处理和抑制相界面处的杂散电流,保证了满意的数值稳定性和精度。因此,可以在模拟中考虑原位热力学条件下水与气的真实密度和粘度差异。通过模拟HBS中多相流过程,定量分析了HDM对气、水输运的影响。
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Pore-Scale Modellings on the Impacts of Hydrate Distribution Morphology on Gas and Water Transport in Hydrate-Bearing Sediments
Gas and water transport behavior, which is controlled by the pore characteristics and capillarity in hydrate-bearing sediments (HBS), is one of the key factors affecting the gas production. Hydrate distribution morphology (HDM) can significantly influence the pore structures of HBS, affecting the relative permeabilities of gas and water. To elucidate the impacts of HDM in microscopic scale, a phase-field lattice Boltzmann (LB) model is developed to describe the gas and water transport in HBS.To simulate the transport of immiscible fluids, which exist obvious density and viscosity contrasts, a phase-field LB model with the conservative form of interface-tracking equation is developed to suppress the spurious currents at phase interfaces. To describe the fluid-solid interactions, the bounce-back condition is applied for both solid phases (hydrate and grains) to achieve the non-slip condition and the wettability condition is applied for grains and hydrate to describe the wettability behavior. To improve the numerical stability, the multi-relaxation-time (MRT) collision operator is applied and the discretization schemes with 8th order accuracy for the gradient operator are selected. In this work, we first validated our model by applying several benchmark cases aiming at fluids with obvious density contrasts such as the layered Couette/Poiseuille flows, Rayleigh–Taylor instability. Then the synthetic geometries of the pore-filling and grain-coating HBS with several hydrate saturation (Shyd) were constructed by guaranteeing the same extent of connectivity. Then the steady-state relative permeability measurement and drainage capillary pressure measurement processes were simulated by the LB model for two HDM cases under several Shyd. The results showed that in the hydrophilic HBS, the relative permeability of gas in the pore-filling case is obviously larger than that in the grain-coating case at the same Shyd, and larger capillary pressure can be obtained in the pore-filling case. In addition, as the Shyd increased, it would notably enhance these differences of fluids relative permeability and capillary pressure between two HDM cases. Because the HDM can not only influence the pore space structures but also the wettability of the porous medium by creating solid surfaces of varying wettability, the distribution and transport of fluid phases in different HDM cases can be obviously affected. The phase-filed LB model applied in this study is capable to handle and suppress the spurious currents at phase interfaces, ensuring a satisfactory numerical stability and accuracy. Thus, the real density and viscosity contrasts between the water and gas under the in-situ thermodynamic conditions can be considered in the simulation. The impacts of HDM on the gas and water transport were quantitively analyzed by simulating multiphase flow processes in HBS.
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