扩展Walsh-Towler算法计算挥发油储层流体黑油PVT特性

J. Almeida
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引用次数: 0

摘要

Walsh和Towler于1995年提出了一种算法,该算法使用恒定体积衰竭(CVD)测试的实验数据,结合商业PVT实验室报告提供的采收率计算,计算凝析气藏流体的改进Black-Oil PVT性质(Bo, Rs, Bg和Rv),作为PVT研究的一部分。该算法的目的是将Walsh - Towler方法推广到挥发性油藏流体。Walsh-Towler算法需要输入气相压缩系数、两相压缩系数、累积采出气量、累积采出油、凝析液体积分数、CVD实验各压力耗尽阶段的气体压缩系数和初始气体压缩系数Zi。该算法需要初始气体压缩系数(Zi)计算饱和压力下烃的初始摩尔数,计算每个压力阶段剩余气体摩尔分数占饱和压力初始总摩尔数的比例,并结合两相压缩系数计算每个阶段耗尽后剩余气液的总摩尔数。对于挥发油样品,初始气体压缩系数(Zi)未定义;为了克服这一限制,提出了一种改进的算法,该算法用CVD实验中产生的井流累积量取代两相压缩系数的使用,其中不需要初始气体压缩系数(对于挥挥油)。该算法可用于计算凝析油和挥发油储层流体的黑油PVT性质(Bo、Rs、Bg和Rv)。计算黑油PVT模型的常用方法是通过校准状态方程并导出凝析油和挥发油储层流体的修正黑油PVT特性。Walsh和Towler提出了一种有价值的工具,不需要使用校准过的EOS,就可以计算凝析油的黑油PVT特性。该算法将该方法推广到挥发性油藏流体。该算法严谨、直接、简单,适用于凝析油和挥发油。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Extended Walsh-Towler Algorithm to Compute Black Oil PVT Properties for Volatile Oil Reservoir Fluids
Walsh and Towler in 1995 presented an algorithm to calculate the modified Black-Oil PVT properties (Bo, Rs, Bg and Rv) of gas condensate reservoir fluids using the experimental data from the Constant Volume Depletion (CVD) test combined with the recovery calculations provided by commercial PVT laboratory reports as part of the PVT study. The purpose of the proposed algorithm is to extend the Walsh and Towler method to volatile oil reservoirs fluids. Walsh-Towler algorithm requires as input parameters the gas compressibility factor, the two- phase compressibility factor, the cumulative produced gas, the cumulative produced oil, the volume fraction of liquid condensate, at each pressure depletion stage of the CVD experiment and the initial gas compressibility factor (Zi). The algorithm requires the initial gas compressibility factor (Zi) to calculate the initial moles of hydrocarbon at the saturation pressure, to calculate the remaining mole fraction of gas at each pressure stage as a fraction of the total moles initially present at the saturation pressure and, combined with the two-phase compressibility factor, for the calculation of the total moles of gas and liquid remaining after each stage of depletion. For volatile oil samples, the initial gas compressibility factor (Zi) is undefined; to overcome this limitation a modified algorithm is proposed that replaces the use of the two-phase compressibility factor by the wellstream produced cumulative from the CVD experiment where the initial gas compressibility factor, for volatile oil, is not required. The proposed algorithm can be applied to calculate the Black-Oil PVT properties (Bo, Rs, Bg and Rv) for both Gas condensate and Volatile oil reservoir fluids. The common practice to calculate the black-oil PVT model is by calibrating an Equation of State and export the modified black-oil PVT properties for both gas condensate and volatile oil reservoir fluids. Walsh and Towler presented a valuable tool, that not requires the use of a calibrated EOS, to calculate the black-oil PVT properties for gas condensate. The proposed algorithm extends the method to volatile oil reservoir fluids. The proposed algorithm is rigorous, direct and simple to use and can be applied to both gas condensate and volatile oil.
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