Journal of Canadian Petroleum Technology
Volume 49,
Number 10,
October 2010,
pp. 15-24
Summary
Underbalanced drilling (UBD) is one of the most widely used technologies
preferred in depleted and/or low-pressured formations. In order to achieve
underbalanced conditions, drilling fluids are usually gasified. Major drilling
fluids preferred during UBD are pure gas, gas-liquid mixtures, and foams. This
study is focused on gas-liquid mixtures. As the gas is introduced, the
behaviour of the drilling fluid becomes hard to explain for many reasons. First
of all, gas is compressible and physical properties of gas are very sensitive
to changes in pressure and temperature. Second, a multiphase flow phenomenon
arises. When there is multiphase flow, flow patterns should be considered. It
is known that there is a difficulty to predict hydraulic behaviour of
gas-liquid mixtures owing to this flow pattern dependence. During a drilling
operation, one of the parameters that should be considered is hole cleaning.
Hole cleaning is a challenging task even for a single-phase drilling fluid.
Moreover, there is still a lack of information about how the cuttings are
transported when gas-liquid mixtures are used as drilling fluids. Flow-rate
optimization during UBD operations for liquid and gas phases are usually
conducted based on formation pressures only. However, considering only this
criterion as the optimization objective is misleading and may cause serious
problems during the drilling operation. In this study, gas and liquid flow
rates during UBD operations are conducted not only based on formation
pressures, but also based on effective hole cleaning. It is assumed that liquid
phase is the major contributor for cuttings transport, and gas phase is only
influencing the bottomhole pressure. A mechanistic model is introduced for
estimating the hydraulic behaviour of gas-liquid mixture drilling fluids under
different flow patterns. Based on the bottomhole pressure and effective hole
cleaning point of view, an algorithm is proposed for estimation of the optimum
required flow rates for liquid and gas phases based on the introduced
mechanistic model. Also, the model predicts the required backpressure that has
to be applied.
© 2010. Society of Petroleum Engineers
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History
- Original manuscript received:
24 March 2009
- Meeting paper published:
17 June 2009
- Revised manuscript received:
15 July 2010
- Manuscript approved:
12 August 2010
- Published online:
1 October 2010
- Version of record:
1 October 2010