Abstract

ABSTRACTElectric submersible pump (ESP) systems are commonly used as an artificial lift technique by the petroleum industry. Operations of ESPs in oil wells are subjected to performance degradation due to the effect of oil viscosity. To understand this effect a numerical study to simulate the flow in three stages of a multistage mixed-flow type ESP operating with a wide range of fluid viscosities, flow rates, and rotational speeds was conducted. The problem was solved by using a commercial computational fluid dynamics (CFD) software. The numerical model was validated with experimental head curves from the literature at different viscosities and rotational speeds available for the same ESP model used in this study, and good agreement was found. Performance degradation was evaluated by analyzing the effect of viscosity on head and flow rate. In addition, a flow field analysis to compare the flow behavior when the pump operates at different viscosities was carried out. The interaction between stages was also analyzed, and the influence of a previous stage on the upstream flow was evidenced. The flow field was analyzed at a curved surface that follows the complex mixed-flow geometry of the stages. CFD proved to be useful for exploring this kind of feature, a task whose accomplishment by means of experimental methods is not trivial. Such analysis helps to understand the flow pattern behind head and flow rate degradation when the Reynolds number is decreased. The results from this work are helpful as they provide a basis to estimate performance degradation for general scenarios.

Highlights

  • Artificial lift techniques are used to increase the production of a given oil well

  • Several simulations were carried out assuming various flow rates for a given fluid viscosity and rotational speed, in order to obtain curves of head versus flow rate

  • The results presented in this paper show a reasonable amount of information to help understanding the performance degradation of centrifugal pumps by the influence of the fluid viscosity

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Summary

Introduction

Artificial lift techniques are used to increase the production of a given oil well. Electric submersible pump (ESP) systems are a common example of that technique and are used in both onshore and offshore installations. Once friction losses can increase significantly depending on the viscosity, its influence on performance degradation is twofold since a higher power input is required by the ESP, whilst the pump head and flow rate decrease. This combined effect severely decreases the pump hydraulic efficiency. Some aspects of the ESP operating with fluids of different viscosities are clarified, such as the interaction between the diffuser and the impeller Understanding all of these features is important to comprehend the phenomena associated with performance degradation and, in extension, to provide better estimations for the performance of pumps under those conditions

Pump geometry
Numerical model
Numerical implementation
Flow regime inside the ESP
Results
Comparison with experiments
Effect of viscosity on pressure head and flow rate
Effect of viscosity per stage
Effect of viscosity on the flow field
Overall comments on the results
Conclusions
Disclosure Statement
Full Text
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