
Unico to Exhibit at the Southwest Petroleum Short Course April 20-21
Unico will once again be showcasing its innovative artificial lift controls at the 52nd annual Southwest Petroleum Short Course in Lubbock, Texas, on April 20-21. Come learn what makes us The New Standard in Well Control. Products to be featured include our sophisticated sucker-rod (SRP), progressing cavity (PCP), and electric submersible (ESP) pump controllers, our new natural gas-powered artificial lift system, remote communication options, and much more. This is our second year at the Short Course, and last year we had a great response. Visit us at booths #34 and #35 to see what sets us apart from the rest. For further information, please contact us.
On-Line Correlations Calculator Predicts Fluid Properties
With this issue, Unico debuts its Correlations Calculator, a convenient tool for predicting the fluid properties of a well from limited information.
Measurements of the physical properties of a fluid are essential to reservoir and production engineering. To perform their calculations, petroleum engineers need to know a fluid's viscosity, density, dissolved gas content, and other factors, as well as how these properties vary with temperature and pressure.
Such information, however, is not usually readily available. In the early stages of a well it can be difficult or economically impractical to obtain reliable measurements. Fluid samples, if available, can be subjected to pressure-volume-temperature analyses to determine their properties, but samples are often suspect and PVT analyses usually apply only at reservoir temperature.
One solution is to use what are known as correlations. By studying field data and fitting curves to measured results, engineers have developed empirical relationships that relate various fluid properties. These correlations are useful tools for estimating fluid properties from limited information. A variety of methods have been developed and published in the literature over the years that produce varying degrees of success depending upon the application.
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FLUID PROPERTIES
Bubble-Point Pressure
Reservoir engineers need to know the bubble-point or "saturation" pressure the pressure at which gas first bubbles out of solution as the pressure on the oil is decreased. While this can be determined from a PVT analysis of a fluid sample or calculated if the composition is known, this information is frequently unavailable. Correlations estimate the bubble point as a function of reservoir temperature, stock-tank oil gravity, dissolved-gas gravity, and solution gas/oil ratio at the initial reservoir pressure.
Gas/Oil Ratio
The gas/oil ratio is a measure of the amount of gas remaining dissolved in solution at pressures below the bubble-point pressure. This information is required by both reservoir and production engineering calculations. While not easily measured, the ratio can be estimated by working the bubble-point correlation backwards and solving for the gas/oil ratio.
Oil Formation Volume Factor
Saturated oil taken from a reservoir to the surface will shrink as the dissolved gas evolves from the fluid. The formation volume factor (FVF) provides a measure of this shrinkage. It is the volume occupied by 1 STB oil and any dissolved gas at some elevated pressure and temperature. Engineers use this to compare tank volumes to reservoir volumes and flow rates at the surface to those downhole under varying conditions. Liquid volume is also affected by temperature. If pressure is increased above the bubble point, the fluid is compressed and its viscosity increases. Reservoir engineers need to relate tank volumes to reservoir volumes at different pressures and constant reservoir temperature. Production engineers need to convert flow rates on the surface to those at various pressures and temperatures as the fluid is produced.
Viscosity
Viscosity is a measure of the fluid's resistance to flow that results from internal friction as the fluid molecules are sheared. Reservoir and production calculations necessitate knowledge of viscosity at various pressures and temperatures. A PVT analysis can be used to measure viscosity at reservoir temperature, but correlations are useful for estimating the changes with temperature as the fluid flows through the production system. Viscosity increases as API gravity and temperature decrease. Dissolved gas lightens the fluid and decreases its viscosity, while increasing the pressure on an undersaturated oil causes its viscosity to increase.
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Correlations can be grouped into two basic categoriesthose that assess gas content and those that predict viscosity. Correlations in the first group are helpful in estimating the amount of gas dissolved in the fluid and at what pressure that gas will evolve. They also estimate the influence of gas on fluid volume and density. Correlations in the second group predict the viscosity of the fluid for gas-free or "dead" oil, saturated oil, and undersaturated oil.
We will be introducing various correlation methods from both categories in upcoming issues of Solutions. The first two correlations we'd like to examine are the Standing and Beal methods.
Standing's Correlation
The Standing correlation, presented by M. B. Standing in 1952, estimates bubble-point pressure, gas/oil ratio, oil formation volume factor, and oil density based upon 105 experimental readings from California wells exhibiting the following range of data:
Bubble-point pressures: 130 to 7,000 psia
Reservoir temperature: 100° to 258° F
Gas/oil ratio: 20 to 1,425 scf/STB
API: 16.5° to 63.8°
Gas gravity: 0.59 to 0.95
With the Standing correlation, gas/oil ratio is determined from the oil API gravity and the investigated pressure and temperature. Bubble-point pressure and oil formation volume factor are dependent upon the API gravity, gas/oil ratio, and investigated temperature. Oil density is calculated using the oil formation volume factor and the oil API gravity, gas/oil ratio, and investigated temperature.
The Standing method estimated bubble-point pressure within 4.8% or 106 psi when used with the study data. The method should provide reasonable results with wells having a similar composition to the study wells, which had virtually no nitrogen or hydrogen sulfide and minimal carbon dioxide.
Beal's Correlation
C. Beal (1946) introduced a correlation showing how oil gravity and reservoir temperature could predict viscosity in dead oils. The correlation was based on measurements from 665 oil samples. The original correlation was presented graphically, but it has since been converted to an equation for convenience.
Beal's correlation estimates dead oil viscosity using the oil API gravity and investigated temperature. Saturated oil viscosity is based upon the dead oil viscosity and adjusted for the gas content using the gas/oil ratio. The unsaturated oil viscosity is calculated using the saturated viscosity, bubble-point pressure, and investigated pressure. Gas/oil ratio and bubble-point pressure can be estimated using a correlation such as Standing's.
Visit www.unicous.com/oilgas/corrcalc.php and try the Standing and Beal methods for yourself. As new correlations are introduced in Solutions, we will be adding them to the Correlations Calculator.
For more information, please contact us.
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