Abstract

The gas compressibility factor, also known as the deviation or Z-factor, is one of the most important parameters in the petroleum and chemical industries involving natural gas, as it is directly related to the density of a gas stream, hence its flow rate and isothermal compressibility. Obtaining accurate values of the Z-factor for gas mixtures of hydrocarbons is challenging due to the fact that natural gas is a multicomponent, non-ideal system. Traditionally, the process of estimating the Z-factor involved simple empirical correlations, which often yielded weak results either due to their limited accuracy or due to calculation convergence difficulties. The purpose of this study is to apply a hybrid modeling technique that combines the kernel ridge regression method, in the form of the recently developed Truncated Regularized Kernel Ridge Regression (TR-KRR) algorithm, in conjunction with a simple linear-quadratic interpolation scheme to estimate the Z-factor. The model is developed using a dataset consisting of 5616 data points taken directly from the Standing–Katz chart and validated using the ten-fold cross-validation technique. Results demonstrate an average absolute relative prediction error of 0.04%, whereas the maximum absolute and relative error at near critical conditions are less than 0.01 and 2%, respectively. Most importantly, the obtained results indicate smooth, physically sound predictions of gas compressibility. The developed model can be utilized for the direct calculation of the Z-factor of any hydrocarbon mixture, even in the presence of impurities, such as N 2 , CO 2 , and H 2 S, at a pressure and temperature range that fully covers all upstream operations and most of the downstream ones. The model accuracy combined with the guaranteed continuity of the Z-factor derivatives with respect to pressure and temperature renders it as the perfect tool to predict gas density in all petroleum engineering applications. Such applications include, but are not limited to, hydrocarbon reserves estimation, oil and gas reservoir modeling, fluid flow in the wellbore, the pipeline system, and the surface processing equipment.

Highlights

  • Fluid properties are directly involved in all flow and volumetric calculations in the upstream and downstream zones of the petroleum industry

  • Its thermodynamic behavior is governed by the ideal gas Equation of State (EoS) Vm = RT/p, where Vm denotes molar volume; density ρ and compressibility c at pressure p and at temperature T are given respectively by: ρ=

  • The objective of this study is to develop a numerical model to predict the Z-factor of hydrocarbon gases by fitting the Standing–Katz chart so as to overcome the weaknesses of the existing methods

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Summary

Introduction

Fluid properties are directly involved in all flow and volumetric calculations in the upstream and downstream zones of the petroleum industry. For the case of natural gas, various calculations need to be run including the estimation of hydrocarbon reserves in a reservoir, the study of the gas flow in the reservoir and the wellbore, and its thermodynamic behavior through the pipelining system until its arrival at the sales point and further transportation to the end user, whereas the latter could be a home user, a plant, or an electric power generation unit. The accurate determination of gas density is of utmost importance, directly related to the conversion of flow rates from line conditions to standard ones where rates are commonly reported. Its thermodynamic behavior is governed by the ideal gas Equation of State (EoS) Vm = RT/p, where Vm denotes molar volume; density ρ and compressibility c at pressure p and at temperature T are given respectively by: ρ=

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