Density of crude oil saturated with CO/sub 2/
F.H. Poettmann, R. S. Thompson, R. Kendall Marra
Abstract
F.H. Poettmann, R. S. Thompson, R. Kendall Marra
Abstract
A correlation for determining the density of CO/sub 2//crude-oil mixtures with engineering accuracy was developed. The correlation is based on the ideal-solution principle. Apparent liquid densities for CO/sub 2/ were correlated as a function of pseudoliquid system density and CO/sub 2/ concentration. In the final working correlation, the pseudoliquid system density is expressed as a function of psuedoliquid hydrocarbon density and CO/sub 2/ concentration. The psuedodensities are then corrected to reservoir conditions. The correlation is presented in both graphic and equation form and is easily adaptable to computer or hand-held calculator applications. The mean error for the 154 data points used to develop the correlation is + 1.39%, the average absolute error is 4.46%, and the standard deviation is 5.25%. An error analysis of the experimental data indicated that when the 20 points with the greatest deviation are removed, the mean error is +0.06%, the average absolute error is 2.8%, and the standard deviation is 2.44%. The correlation presented provides a simple method for calculating the density of CO/sub 2//crude-oil mixtures with engineering accuracy. The densities are used for calculating FVF and swelling and in other reservoir engineering calculations.
A significance statement is not available in the OpenAlex record.
A contribution statement is not available in the OpenAlex record.
Method details are not available in the OpenAlex metadata.
Findings are not separately available in the OpenAlex metadata.
Limitations are not available in the OpenAlex metadata.
Application details are not available in the OpenAlex metadata.
A correlation for determining the density of CO/sub 2//crude-oil mixtures with engineering accuracy was developed. The correlation is based on the ideal-solution principle. Apparent liquid densities for CO/sub 2/ were correlated as a function of pseudoliquid system density and CO/sub 2/ concentration. In the final working correlation, the pseudoliquid system density is expressed as a function of psuedoliquid hydrocarbon density and CO/sub 2/ concentration. The psuedodensities are then corrected to reservoir conditions. The correlation is presented in both graphic and equation form and is easily adaptable to computer or hand-held calculator applications. The mean error for the 154 data points used to develop the correlation is + 1.39%, the average absolute error is 4.46%, and the standard deviation is 5.25%. An error analysis of the experimental data indicated that when the 20 points with the greatest deviation are removed, the mean error is +0.06%, the average absolute error is 2.8%, and the standard deviation is 2.44%. The correlation presented provides a simple method for calculating the density of CO/sub 2//crude-oil mixtures with engineering accuracy. The densities are used for calculating FVF and swelling and in other reservoir engineering calculations.
Key concepts: Standard deviation, Absolute deviation, Approximation error, Mathematics, Relative standard deviation, Chemistry, Series (stratigraphy), Statistics