International Journal Of Scientific & Engineering Research, Volume 7, Issue 7, July-2016 1173 ISSN 2229-5518 IJSER © 2016 http://www.ijser.org Natural Gas Compressibility Factor Measurement and Evaluation for High Pressure High Temperature Gas Reservoirs I.I. Azubuike, S. S.Ikiensikimama,O.D.Orodu Abstract— The Natural gas compressibility factor is an important reservoir fluid property used in reservoir engineering computations either directly or indirectly in material balance calculations, well test analysis, gas reserve estimates, gas flow in lines and in numerical reservoir simulations. Existing gas compressibility factor correlations were derived using measured data at low to moderate pressures(less than 8, 000 psia) and temperatures (less than 212 o F), and an extrapolation to High Pressure High temperature (HPHT) is doubtful. The need to understand and predict gas compressibility factor at HPHT has become increasingly important as exploration and production has moved to ever deeper formations where HPHT conditions are to be encountered. This paper presents laboratory measurement of gas compressibility factors at HP HT natural gas systems and the ev aluation of s ome selected gas compressibility factors correlations. Samples of gas mixtures were collected from the high pressure gas reservoirs from the Niger Delta region of Nigeria. Vinci PVT Cell was used to measure the gas compressibility factors for a pr essures ranging from 6,000 to 14,000 ps ia and tem peratures at 270 o F and 370 o F. T he new laboratory data was compared to some of the gas compressibility factor correlations/ models used in the petr oleum industry. Results showed that majority of the correlations studied overestimated the gas compressibility factor at HPHT. Mean relative and absolute error analysis were done based on the temperature difference; it was found that the total mean relative and absolute errors for the 370 o F cases are higher than those for 270 o F. Among all the correlations assessed, Hall and Yarborough equation performed better than other existing correlations with a mean absolute error of 3.545 and relative error of -2.668 at 270 o F. At 370 o F, Beggs and Brills correlation predicted better than other correlations studied with a mean relative error of -4.77 and absolute error of 7.187. Index Terms—Correlation, Evaluation, High Pressure, High Temperature, Gas Compressibility Factor, Gas Reservoir, Natural gas —————————— —————————— 1. INTRODUCTION In dealing with gases at low pressures, the ideal gas relationship is a convenient and generally satisfactory tool. At higher pressures, the use of the ideal gas equation-of-state may lead to errors as great as 500%, as compared to errors of 2–3% at atmospheric pressure [1]. I . I. Azubuike is currently pursuing doctoral degree program in Petroleum Engineering Department, world Bank Center of Excellence for Oil Field Chemical Research, University of Port-Harcourt, Nigeria. Dr. S. S. Ikiensikimama is currently Associate Professor in the Department of Petroleum & Gas Engineering University of Port-Harcourt, Rivers State, Nigeria. Dr. O. D. Orodo is currently Associate Professor in the Covenant University, Ota, Ogun State, Nigeria. Numerous equations-of-state have been developed in the attempt to correlate the pressure-volume-temperature (PVT) variables for real gases with experimental data. In order to express a more exact relationship between the variables P, V, and T, a correction factor called the gascompressibilityfactor, gas deviation factor, or simply the z-factor, must be introduced into the Ideal gas law. Its value reflects how much the real gas deviates from the ideal gas behaviour at a given pressure and temperature. Compressibility factor is defined and expressed as: =   (1) Introducing the z-factor to ideal gas law results to real gas equation (Equ. 2),  =  (2) where n is the number of moles of gas, P is the pressure, V is the volume and T is the absolute temperature. Gas compressibility factor can be determined on the basis of measurements in PVT laboratories. At low temperature and IJSER