Title: Sin t
1Paper Results from Averaging Model for
Cuttings Transport in Horizontal
Drilling Authors Salazar-Mendoza, R. (IMP),
and A. García-Gutiérrez (IIE). Session
Drilling Tuesday September 12, 2006
2Acknowledgements
3 4Factors affecting drill cuttings transport
The pressure gradient is considered the most
important parameter in a solid-liquid flow
- Velocity
- Drill Cuttings volume fractions
- Drill Cuttings Density
- Fluid Density
- Fluid Viscosity
5There are three main flow patterns for
solid-liquid flow (Doron and Barnea, 1996) 1)
Fully suspended flow 2) Flow with a moving bed
3) Flow with a stationary bed
Photographies from Iyoho (1980)
6 7Point Equations Fully suspended flow
Point Equations Stationary Bed
The Method of Volume Averaging (Whitaker, 1999)
Porous Medium Averaging Model ?-region
Two-Fluid Averaging Model ?-region
Closures
Closures
Condition of Local Mechanical Equilibrium
Two-Regions Averaging Model Flow with a
stationary bed
Numerical Solution
Comparation with Exp. Data
One-equation Averaging Model ?-region
Stress in the boundary ?-?
Conclusions
8Interfacial Boundary Condition
Initial Conditions
Boundary Conditions
Interfacial Jump Conditions
9- The Method of Volume Averaging
-Superficial average
-Intrinsic average
-Volume fraction
-Relation
10- The Method of Volume Averaging...
-Spatial averaging theorem and the general
transport theorem (Gray and Lee, 1977)
11- Two-Fluid Averaging Model for w-region
12 13- Condition of Local Mechanical Equilibrium
This mean that the fully suspended flow can be
characterized by a single velocity
14- One-Equation Averaging Model for w-region
where
15- Porous Medium Averaging Model for ?-region
Derived by Ochoa-Tapia and Whitaker (1995)
16 17- Final Formulation of the Two-Regions Averaging
Model for Cutting Transport in Horizontal Drilling
18 19Case 1.-Fully suspended flow
Case 2.-Flow with a stationary bed
Case 3.-Flow with a moving bed
20 21 22 23 24- Results for Cases 2 and 3
25- Results for Cases 2 and 3
26- In this work, the process of cutting transport
for the three main flow patterns was analyzed 1)
fully suspended flow, 2) flow with a stationary
bed, and 3) flow with a moving bed. - The numerical results and their comparison with
experimental data and theoretical results show
that 1) the model for a fully suspended flow is
not adequate for simulating a flow with a moving
bed nor a flow with a stationary bed, 2) the
models for a flow with a stationary bed and a
flow with moving bed allow to obtain the
theoretical flow pattern transition, as a
function of total volume fraction, which depends
on the maximum packing at the bottom of the pipe,
3) the results for the dimensionless pressure
gradient, obtained for a flow with a stationary
bed and a flow with a moving bed, are in
agreement with experimental data and theoretical
results reported in the literature
27The authors wish to thank the financial support
provided by the Instituto Mexicano del Petróleo
(IMP), the Consejo Nacional de Ciencia y
Tecnología (CONACyT), and the Secretaría de
Educación Pública (SEP) of México.