Common Versus Herschel-Bulkley Drilling Fluid Models: Effect of Their Rheological Parameters on Dynamic Particle Settling Velocity

Authors

  • Mazen Ahmed Muherei Assistant Professor, Pet. Eng. Depart., Hadhramout Uni, Mukalla, Yemen

Keywords:

Drilling Fluid, Drill cuttings, Hole Cleaning, Rheology, Settling Velocity.

Abstract

Rheological modelling of drilling fluids in oil fields is usually described by Bingham plastic and Ostwald-deWaele models. These models gain popularity because their specific descriptive parameters are fairly easy to estimate. Standard methods use Fann VG meter dial reading at 600 and 300 rpm to determine these rheological parameters. Unfortunately, these points correspond to higher shear rates which seldom prevail during particle settling. Recently, many researchers pointed out that the non-Newtonian behavior of drilling fluids can be described well by the three parameters Herschle-Bulkley model. Again, the determination of its parameters using the standard API method make use of dial readings at 6 & 3 rpm to determine yield stress and 600 and 300 rpm to determine the other two parameters. Furthermore, the use of non-linear regression techniques to determine these parameters though deemed more accurate, sometimes give meaningless negative yield stress values. This work aims to investigate different techniques and shear rates to derive rheological parameters and show their influence on the magnitude of effective viscosity and hence settling velocity. It is demonstrated that very small differences among the values of the model parameters determined by different techniques/dial readings can lead to substantial differences in predicted settling velocities. Results of this work shows that the use of Herschle-Bulkley rheological parameters was by far the most accurate for representing the example muds rheograms as well as predicting the settling velocities, particularly when using non-linear regression values. Moreover, the simplified API method to determine Herschle-Bulkley rheological parameters may lead to considerable errors that may negate the usefulness of the model. It has been shown that Chien [10] correlation is sensitive to mud rheology and is suitable only for thin fluids. However, Chien [10] correlation was not affected by the annular fluid velocities.

Author Biography

Mazen Ahmed Muherei, Assistant Professor, Pet. Eng. Depart., Hadhramout Uni, Mukalla, Yemen

Assistant professor, Department of petroleum engineering

References

[1]. T. Hemphill, W. Campos and A. Pilehavari. "Yield-power law model accurately predicts mud rheology." Oil& Gas Journal, Aug. 23, pp. 91-49.
[2]. M. Zamora and F. Growcock. "The top 10 myths, misconceptions and mysteries in rheology and hydraulics." AADE Fluid Conference and Exhibition, Apr. 6-7, Houston, Texas, AADE-10-DF-HO-40, 2010.
[3]. V. C. Kelessidis, R. Maglione, C. Tsamantaki and Y. Aspirtakis. "Optimal determination of rheological parameters for Herschle-Bulkley drilling fluids and impact on pressure drop, velocity profiles and penetration rates during drilling." Journal of Petroleum Science and Engineering, vol. 53, pp. 203-224, 2006.
[4]. API RP 13D. "Rheology and Hydraulics of Oil-Well Drilling Fluids." 5th ed., American Petroleum Institute, 2006.
[5]. S. F. Chien. "Annular velocity for rotary drilling operations." Intl. J. Rock Mech. Min. Sci., vol. 9, pp. 403, 1972.
[6]. H. U. Zeidler. "An experimental analysis of the transport of drilling particles." SPEJ, vol. 14 (1), pp. 39-48, SPE 3064, 1972.
[7]. P. L. Moore. "Drilling Practice Manual." PennWell Publishing Co., Tulsa, 1974, pp. 268-276.
[8]. R. E. Walker and T. M. Mayes. "Design of muds for carrying capacity." JPT, vol. 27 (7), July, pp. 893, SPE 4975, 1975.
[9]. J. M. Peden and Y. Luo. "Settling velocity of various shaped particles in drilling and fracturing fluids." SPEDE, vol. 2 (4), Dec, pp. 337-343, SPE 16243, 1987.
[10]. S. F. Chien. "Settling velocity of irregularly shaped particles." SPEDC, vol. 9 (4), Dec, pp. 281-289, SPE 26121, 1994.
[11]. K. J. Sample, and A. T. Bourgoyne. "An experimental evaluation of correlations used for predicting cutting slip velocity." SPE Annual Technical Conference and Exhibition, Oct. 9-12, Denver, Colorado, SPE 6645, 1977.
[12]. P. Skalle, K. R. Backe, S. K. Lyomov, and J. Sveen. "Barite segregation in inclined boreholes," Journal of Canadian Petroleum Technology, special vol., PETSOC 97-76, 1999.
[13]. T. Hemphill. "Hole-cleaning model evaluated fluid performance in extended reach wells," Oil & Gas Journal, Jul. 14, pp. 56-64, 1997.
[14]. API RP 13D "Rheology and Hydraulics of Oil-Well Drilling Fluids." American Petroleum Institute, pp. 20-21, June, 1995.
[15]. T. E. Becker, J. J. Azar and S. S. Okrajni. "Correlations of mud rheological properties with cuttings-transport performance in directional drilling." SPEDE, vol. 6 (1), Mar., pp. 16-24, SPE 19535, 1991.
[16]. M. A. Muherei and S. S. Basaleh. "True power law drilling fluid model: effect of its rheological parameters on static particle settling velocity." International Research Journal of Engineering and Technology, vol. 3 (1), Jan., pp. 77-88, 2016.
[17]. T. R. Sifferman, G. M. Myers, E. L. Haden and H. A. Wahl. "Drill cutting transport in full scale vertical annuli." J. Petroleum Technology, vol. 26 (11), Nov., pp. 1295-1302, SPE 4514, 1974.
[18]. B. J. Mitchell. "Advanced Oil Well Drilling Engineering: Handbook and Computer Programs." Mitchell Engineering, USA, 10th ed., 1995, pp: 262
[19]. E. Guliyev, "The Importance of Low-end-rheology and its Influence on Particle Slip Velocity," Master thesis, Norwegian University of Science and Technology, 2013.
[20]. E. J. Novotny. "Proppant transport." SPE Annual Fall Technical Conference and Exhibition, Denver, Colorado, SPE 6813, Oct. 9-12, 1977
[21]. P. Kenny, E. Sunde and T. Hemphill. "Hole cleaning modelling: what's "n" got to do with it?." IADC/SPE Drilling Conference, New Orleans, Louisiana, IADC/SPE 35099, Mar. 12-15, 1996.

Downloads

Published

2016-02-07

How to Cite

Muherei, M. A. (2016). Common Versus Herschel-Bulkley Drilling Fluid Models: Effect of Their Rheological Parameters on Dynamic Particle Settling Velocity. American Scientific Research Journal for Engineering, Technology, and Sciences, 16(1), 155–177. Retrieved from https://asrjetsjournal.org/index.php/American_Scientific_Journal/article/view/1377

Issue

Section

Articles