Difference between revisions of "Beggs and Robinson Oil Viscosity correlation"
From wiki.pengtools.com
(→Example. Calculation of the oil viscosity) |
|||
Line 39: | Line 39: | ||
===Input data=== | ===Input data=== | ||
:<math>T</math> = 137 F° | :<math>T</math> = 137 F° | ||
− | :<math>SG_o</math> = 22 API | + | :<math>SG_o</math> = 0.922 or 22 API |
:<math>R_s</math> = 90 scf/stb | :<math>R_s</math> = 90 scf/stb | ||
Revision as of 12:12, 28 September 2020
Contents
Beggs and Robinson oil viscosity correlation
Beggs and Robinson is an empirical correlation for the oil viscosity published in 1975 [1].
Math & Physics
Dead oil viscosity:
where:
Saturated oil viscosity (P < Pb):
where:
Undersaturated oil viscosity (P > Pb):
where:
Example. Calculation of the oil viscosity
Example source [3]
Input data
- = 137 F°
- = 0.922 or 22 API
- = 90 scf/stb
Calculate the saturated oil viscosity?
Solution
x = 1.2658
- = 17.44 cP
A = 0.719 B = 0.853
- = 8.24 cP
The solution is available in the online PVT calculator software model at www.pengtools.com
Application range
Description of the Data Used[1]:
Number of oil systems = 600
Number of dead oil observations = 460
Number of live oil observations = 2,073
Nomenclature
- = coefficient
- = coefficient
- = coefficient
- = pressure, psia
- = solution gas-oil ratio, scf/stb
- = oil specific gravity, dimensionless
- = temperature, °F
- = coefficient
- = viscosity, cP
Subscripts
- b - bubble point
- od - dead oil
- os - saturated oil
- o - undersaturated oil
References
- ↑ 1.0 1.1 Beggs, H. D.; Robinson, J. R. (September 1975). "Estimating the Viscosity of Crude Oil Systems". Journal of Petroleum Technology. 27(09) (SPE-5434-PA).
- ↑ Vasquez, M.; Beggs, H.D. (1980). "Correlations for Fluid Physical Property Prediction.". Society of Petroleum Engineers (SPE-6719-PA).
- ↑ Beggs, H. Dale (1987). Oil System Correlations (1987 PEH Chapter 22). Society of Petroleum Engineers.