一种用于相位行为高效建模的代理Peng-Robinson EOS

M. Zhao, R. Okuno
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摘要

状态方程(EOS)组分模拟通常用于模拟各种油藏和地表过程的相行为与流体流动之间的相互作用。然而,由于其计算成本,迫切需要使用EOS进行有效的相位行为计算。本研究的目的是建立一个基于Peng-Robinson EOS的快速多相闪速模拟的逸度系数代理模型。本研究中实现的代理模型是在Peng-Robinson EOS只有一个根时绕过逸度系数的计算,而这种情况在油藏条件下经常出现。在Peng-Robinson模型的基础上,采用具有超过3000万个逸度系数的人工神经网络(ANN)对代理逸度模型进行训练。利用Am、Bm、Bi和ΣxiAij四个参数准确地预测了Peng- Robinson逸出系数。由于这些标量参数是通用的,而不是特定于特定的成分、压力和温度,因此代理模型与原始的Peng-Robinson EOS一样适用于石油工程应用。代理模型应用于多相闪速计算(分相和稳定性),当Peng-Robinson EOS有一个根时,可以绕过三次方程解和逸度系数计算。当EOS有多个根时,可以解析计算原始逸度系数,但这种情况仅在油藏条件下偶尔发生。一个案例研究表明,与传统的EOS计算相比,代理逸度模型的加速系数为3.4%。案例研究还展示了准确的多相闪蒸结果(稳定性和相分裂)以及具有不同(数量)组分的不同流体情况的可互换代理模型。这是可能的,因为它预测了变化空间中的Peng-Robinson逸度,而不是特定于成分,温度和压力。基于同样的原因,非零二值迭代参数不会影响模型的适用性、准确性、鲁棒性和效率。由于代理模型是特定于单个组件的,因此可以使用代理模型的组合来为任何组件的混合建模。通过对训练超参数和训练数据采样方法的调优,使人工神经网络建模的平均绝对百分比误差降低到0.1%以下。据我们所知,这是第一个适用于任何混合物的Peng-Robinson逸度的广义代理模型。该模型保留了传统的快速迭代、收敛鲁棒性和手动参数调整选项。
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A Proxy Peng-Robinson EOS for Efficient Modeling of Phase Behavior
Equation-of-state (EOS) compositional simulation is commonly used to model the interplay between phase behavior and fluid flow for various reservoir and surface processes. Because of its computational cost, however, there is a critical need for efficient phase-behavior calculations using an EOS. The objective of this research was to develop a proxy model for fugacity coefficient based on the Peng-Robinson EOS for rapid multiphase flash in compositional flow simulation. The proxy model as implemented in this research is to bypass the calculations of fugacity coefficients when the Peng-Robinson EOS has only one root, which is often the case at reservoir conditions. The proxy fugacity model was trained by artificial neural networks (ANN) with over 30 million fugacity coefficients based on the Peng-Robinson EOS. It accurately predicts the Peng- Robinson fugacity coefficient by using four parameters: Am, Bm, Bi, and ΣxiAij. Since these scalar parameters are general, not specific to particular compositions, pressures, and temperatures, the proxy model is applicable to petroleum engineering applications as equally as the original Peng-Robinson EOS. The proxy model is applied to multiphase flash calculations (phase-split and stability), where the cubic equation solutions and fugacity coefficient calculations are bypassed when the Peng-Robinson EOS has one root. The original fugacity coefficient is analytically calculated when the EOS has more than one root, but this occurs only occasionally at reservoir conditions. A case study shows the proxy fugacity model gave a speed-up factor of 3.4% in comparison to the conventional EOS calculation. Case studies also demonstrate accurate multiphase flash results (stability and phase split) and interchangeable proxy models for different fluid cases with different (numbers of) components. This is possible because it predicts the Peng-Robinson fugacity in the variable space that is not specific to composition, temperature, and pressure. For the same reason, non-zero binary iteration parameters do not impair the applicability, accuracy, robustness, and efficiency of the model. As the proxy models are specific to individual components, a combination of proxy models can be used to model for any mixture of components. Tuning of training hyperparameters and training data sampling method helped reduce the mean absolute percent error to less than 0.1% in the ANN modeling. To the best of our knowledge, this is the first generalized proxy model of the Peng-Robinson fugacity that is applicable to any mixture. The proposed model retains the conventional flash iteration, the convergence robustness, and the option of manual parameter tuning for fluid characterization.
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