将管道分流理论与全成分井筒模型相结合

Shuang Zheng, M. Sharma
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摘要

在油气井和地热井中,多相组成的井筒流动是决定流体流动和压降的重要因素。这些影响在有多个流体流入位置的长分支中变得越来越重要。由于井筒中压力、温度、流入流体速率和成分的变化,会在井筒中发生复杂的烃相行为,如相数变化、相翻转、气滑等。本文介绍了一种新的井筒模型,该模型结合了具有能量平衡的全组分流体流动和具有沿井筒多个流体进入点的管道分段流动理论。四组控制方程:组分质量守恒、动量守恒(管道分流理论)、组分守恒和能量平衡沿井筒完全隐式求解。然后将其与储层和裂缝域中的流动和能量平衡方程完全隐式耦合。然后可以获得沿井筒的主要未知数(总流量、碳氢化合物成分、含水饱和度、压力和温度)。采用闪速计算法计算烃类饱和度、密度、粘度等,根据局部流速和饱和度,根据分流理论计算出各相的流量。在第一个案例中,我们研究了一个含16种烃组分的凝析气藏的储层-井筒流动。随着压力的下降,油相从单相凝析液中析出,首先进入井筒,然后进入储层。在第二种情况下,我们模拟了黑油油藏中的二氧化碳驱油。在注入井附近观察到储层冷却,并且在生产井的产出油中观察到二氧化碳成分增加。在第三种情况下,我们研究了具有14种烃组分的低渗透挥发性油藏。考虑储层-裂缝-井筒流动,模拟了水力压裂水平井筒的生产。我们观察到,随着井筒压力的下降,气体从油相中释放出来,这大大改变了井筒压降。由于含液率的影响,轻组分随时间减少,而重组分随时间增加。在第四种情况下,我们展示了一个与点源集成的独立井眼模型。本文首次将管柱分流公式与井眼成分流动和能量平衡完全结合起来。这使得该模型可以直接用于组成油藏模拟器。井眼网格自动生成,并与储层/裂缝网格相结合,从而实现从储层到地面设施的集成无缝模拟。该模型使工程师能够在模拟复杂流体的生产/注入时准确地计算井筒内的压降和相行为。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Integrating Pipe Fractional Flow Theory with Fully Compositional Wellbore Models
Multi-phase compositional wellbore flow is important in determining the flow and pressure drop in oil, gas, and geothermal wells. These effects become increasingly important in long laterals with multiple locations for fluid influx. Complex hydrocarbon phase behavior such as change in the number of phases, phase flipping, gas slippage can happen in the wellbore because of changes in pressure, temperature and inflow fluid rate and composition along the wellbore. This paper introduces a new wellbore model which integrates fully compositional fluid flow with an energy balance and pipe fractional-flow theory with multiple points of fluid entry along the wellbore. Four sets of governing equations: component mass conservation, momentum conservation (pipe fractional flow theory), composition conservation and energy balance are solved fully implicitly along the wellbore. This is then fully implicitly coupled with the flow and energy balance equations in the reservoir and fracture domains. The primary unknowns along the wellbore (total flow rate, hydrocarbon component composition, water saturation, pressure, and temperature) can then be obtained. Flash calculations are used to calculate the hydrocarbon phase saturation, density, viscosity, etc. and the flow rate of each phase is obtained from the fractional flow theory given the local flow rate and saturations. In the first case, we study the reservoir-wellbore flow in a gas condensate reservoir with 16 hydrocarbon components. As the pressure drops, an oil phase drops out of the single phase gas condensate, first in the wellbore and then in the reservoir. In a second case, we simulate CO2 flooding in a black-oil reservoir. Reservoir cooling is observed near the injection wellbore and an increased CO2 composition is observed in the produced oil from the production wellbore. In the third case, we study a low permeability volatile oil reservoir with 14 hydrocarbon components. Production from a hydraulically fractured horizontal wellbore is simulated considering the reservoir-fracture-wellbore flow. We observe that as the pressure drops in the wellbore, gas is liberated from the oil phase and this changes the wellbore pressure drop considerably. The lighter component compositions decrease with time while the heavier component compositions increase with time because of the liquid holdup effect. In the fourth case, we showcase a stand-alone wellbore model integrated with point sources. This paper fully integrates a pipe-fractional flow formulation with compositional wellbore flow, and an energy balance for the first time. This allows the model to be used directly with compositional reservoir simulators. The wellbore mesh is automatically generated and coupled with the reservoir/fracture mesh to allow for an integrated and seamless simulation from the reservoir to the surface facility. This model allows engineers to accurately account for the pressure drop and phase behavior within the wellbore when simulating the production/injection of complex fluids.
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