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首页> 外文期刊>In Situ >DEVELOPMENT OF EQUATIONS STATE FOR GAS CONDENSATES FOR COMPOSITIONAL PETROLEUM RESERVOIR SIMULATION
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DEVELOPMENT OF EQUATIONS STATE FOR GAS CONDENSATES FOR COMPOSITIONAL PETROLEUM RESERVOIR SIMULATION

机译:组合油气藏天然气凝析方程状态的开发。

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In this paper, we describe our experience in the development of an equation-of-state (EOS) model for compositional reservoir simulation studies of gas condensates, especially those near the critical point. We focused on the following tasks: (1) heavy-end pseudoization; (2) selection of the measured data to match and the EOS parameters to adjust; and (3) evaluation of model predictive capability.We compared several methods for each of the above tasks for a number of gas condensates, one of which is a near-critical gas condensate showing experimentally significant compositional change with depth. The combination of the different methods offers up to 44 different heavy-end descriptions. The Peng-Robinson (PR) EOS was then used with these fluid descriptions to predict the phase behavior of gas condensates. We observed that none of these 44 heavy-end descriptions is significantly better than the others, although they give very different properties of pseudocomponents. Tuning EOS-parameters to match experimental data is necessary' in order to well describe the phase behavior of gas condensates. The matched experimental data should include both phase amount and volume information. The initial guesses significantly affect the quality of the matches; those initial guesses using the Gaussian quadrature method for lumping lead in general to satisfactory matches. Tuning molecular weights of pseudocomponents (critical properties and acentric factor vary with them through correlations) in combination with independently tuning pseudocomponent critical properties is found to be a better procedure than other available tuning procedures. The model developed using this procedure can well capture the compositional variation and other associated property changes with depth for near-critical gas condensates tested in this work. The volume-shift parameters need to be used after the model matches phase-amount data.
机译:在本文中,我们将描述我们在状态方程(EOS)模型的开发中的经验,该模型用于凝析气尤其是临界点附近的凝析气成分储层模拟研究。我们专注于以下任务:(1)重型伪造; (2)选择要匹配的测量数据和调整EOS参数; (3)模型预测能力的评估。针对多种凝析气,我们比较了上述每种任务的几种方法,其中一种是近临界凝析气,显示出随深度的实验性显着变化。不同方法的组合最多提供44种不同的高端描述。然后,将Peng-Robinson(PR)EOS与这些流体描述一起使用,以预测气体冷凝物的相态。我们观察到这44个高端描述中没有一个比其他描述明显更好,尽管它们给出了伪组件的不同特性。调整EOS参数以匹配实验数据是必要的,以便很好地描述凝析气的相态。匹配的实验数据应包括相量和体积信息。最初的猜测会严重影响比赛的质量;那些最初使用高斯求积法进行猜测的方法通常会得出令人满意的结果。发现伪组分的分子量的调节(临界特性和中心因数通过相关性随它们的变化而变化)与独立地调节伪组分的临界特性相结合是比其他可用的调节程序更好的过程。使用此程序开发的模型可以很好地捕获此工作中测试的近临界气体凝析物随深度变化的成分变化和其他相关属性变化。在模型匹配相位量数据之后,需要使用音量偏移参数。

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