An improved temperature-viscosity correlation for crude oil systems

被引:45
作者
Egbogah, Emmanuel O. [1 ]
Ng, Jack T. [1 ]
机构
[1] Amer Hydrocarbon Technol Inc, Stn T, Calgary, AB T2H 2G9, Canada
关键词
6;
D O I
10.1016/0920-4105(90)90009-R
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Egbogah, E.O. and Ng, J.T., 1990. An improved temperature viscosity correlation for crude oil systems. J. Pet. Sci. Erg., 4: 197-200. In the application of Beggs and Robinson dead-oil viscosity temperature empirical correlation to several hundred dead-oil systems, we have found a consistently significant deviation between measured and calculated viscosity values. This paper presents a modified Beggs and Robinson empirical viscosity correlation. The proposed new correlation has be en verified using a data base of about four hundred oil analysis reports (oil systems), and it shows a significantly better correlation, with a standard deviation and average error of at least 12% and 55%, respectively, better than the existing correlation of Beggs and Robinson. We have also expanded the applicability of this correlation further by the inclusion of pour point temperature in the empirical equations. The new correlation also appears to apply to a wide range of oil specific gravities and pour point temperatures.
引用
收藏
页码:197 / 200
页数:4
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