Authors: Seyed Saied Bahrainian; Amin Nabati; Ebrahim Hajidavalloo
Addresses: Mechanical Engineering Department, Shahid Chamran University of Ahvaz, Ahvaz, 61357-83151, Iran ' Mechanical Engineering Department, Shahid Chamran University of Ahvaz, Ahvaz, 61357-83151, Iran ' Mechanical Engineering Department, Shahid Chamran University of Ahvaz, Ahvaz, 61357-83151, Iran
Abstract: In this study, viscous, non-Newtonian turbulent flow simulations are obtained through a tri-cone bit inside a bottom hole to show the effect of different rheological models on pressure drop calculations. The rheological models include Bingham plastic, Power law, and Herschel-Bulkley. Flow simulations are obtained for nozzle sizes of 7/32, 9/32, 10/32, and 11/32 inch and four different flow rates are used in each solution. A standard water-base mud is selected for this study. Rheological data are obtained using a Fann viscometer. The calculated pressure drops from CFD simulations are then compared to experimental data and Eckel-Bielstein equation. The results show that Herschel-Bulkley model has predicted the pressure drop with the least average percent error of 5.90 as compared with experimental data. This is followed by Power law and Bingham plastic rheological models, and Eckel-Bielstein equation with the absolute average percent error of 6.64, 8.00, and 17.57, respectively. [Received: May 24, 2017; Accepted: December 1, 2017]
Keywords: rheological model; flow simulation; tri-cone bit; pressure drop.
International Journal of Oil, Gas and Coal Technology, 2018 Vol.18 No.3/4, pp.305 - 323
Available online: 03 Jul 2018 *Full-text access for editors Access for subscribers Purchase this article Comment on this article