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Tuning of the Peng-Robinson Equation of State for Gas Condensate Simulation Studies

机译:调整鹏罗宾逊型燃气凝聚仿真研究状态的方程

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Gas condensate compositional simulation studies are conducted to evaluate gas and condensate reserves. This is carried out when making comparisons of production methods for the economic development of a reservoir. The data needed for the evaluation are dew point pressure, gas compressibility factor, liquid volume and produced gas (Constant Volume Depletion, CVD data) and are nowadays determined from a tuned Equation of State (EOS). However the open literature has shown that there is no consistency in the number of Single Carbon Number (SCN) groups, EOS tuning parameters, lumping schemes and weight factors applied to the experimental when tuning an EOS for use in compositional simulation studies, particularly for gas condensate fluids. Publications have shown that the two most widely used sets of parameters from the EOS that are tuned are the Binary Interaction Coefficient (BIC) with the critical properties and acentric factor or BIC and the constants called the omegas (?'s). The number of SCN groups used for tuning varies from ten to more than forty. However there are currently no criteria for selecting the most reliable lumping scheme that will give similar accuracy to using the many SCN groups except by trial and error or by algorithms designed to test a number of schemes and from which the best one is selected. In this paper, the Peng-Robinson EOS has been tuned and tested to predict CVD data for seven gas condensate samples. Compositional analysis greater than Single Carbon Number 24 (SCN24) are required for the SCN route. The two sets of tuning parameters were used with and without the VSP. Our parametric study demonstrated that the VSP should not be applied with the ?'s when tuning the Peng-Robinson EOS. With weight factors of 1 for liquid volume, 10 for gas compressibility factor and without the VSP, the Ω's give better prediction of CVD data than the critical properties and acentric factor even with the VSP included. The SCN groups for two samples were lumped into six Multiple Carbon Number (MCN) groups using the simple Whitson's lumping scheme. Our tuning technique with the ?'s and with our new weight factors for the experimental data, gave differences of less than ±4.0 % from the tuned EOS predictions before and after lumping of the SCN group so that complex algorithms are not necessary to select an appropriate lumping scheme to reduce cost and computer time when performing simulation studies. Our tuning technique with only one regression step, showed consistency in tuning the Peng-Robinson EOS with the ?'s and could be used for simulation studies of gas condensate systems.
机译:对气体缩合物组成模拟研究进行了评估气体和冷凝水储备。这是在进行水库经济发展的生产方法的比较时进行的。评价所需的数据是露点压力,气体可压缩因子,液体体积和产生的气体(恒定体积耗尽,CVD数据),并且如今由状态的调谐方程(EOS)确定。然而,开放文献已经表明,在调整EOS中用于组合模拟研究的eos时,单碳数(SCN)组,EOS调谐参数,集合方案和重量因子的数量没有一致性,EOS调整参数,集合方案和权重因子,特别是用于气体冷凝水液体。出版物表明,从调整的EOS中使用的两个最广泛的参数集是二进制交互系数(BIC),具有关键属性和贵重因子或BIC,并且常量称为OMEGA(?')。用于调整的SCN组的数量从十个到超过四十多。然而,目前没有选择最可靠的Lumping方案的标准,这些方案将提供类似的准确性,以使用除了试验和错误之外的许多SCN组或设计用于测试许多方案的算法以及选择最佳的算法。本文已被调整和测试PENG-Robinson EOS以预测七种气体冷凝物样品的CVD数据。 SCN途径需要大于单碳数24(SCN24)的组成分析。两组调整参数与VSP一起使用。我们的参数学研究表明,在调整彭罗宾逊EOS时,不应应用VSP。对于液体体积的1个重量因子,10对于气体可压缩性因子,而没有VSP,ω也可以更好地预测CVD数据,而且即使包括VSP,也可以提高CVD数据和贵重因子。使用简单的WHITSON的绝地形方案将两个样品的SCN组分列为六个多种碳数(MCN)组。我们的调整技术与我们的新重量因子进行实验数据,从SCN组的分列之前和之后,从调谐的EOS预测中产生了小于±4.0%的差异,从而不需要复杂的算法来选择一个适当的绝地方案,以降低进行仿真研究时降低成本和计算机时间。我们的调整技术只有一个回归步骤,在调整彭罗宾逊EOS时展示了一致性,并可用于气体冷凝水系统的仿真研究。

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