SPE Production & Operations
Volume 24, Number 2, May 2009, pp. 269-276

SPE-109765-PA

A Robust Steady-State Model for Flowing-Fluid Temperature in Complex Wells

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DOI  More information 10.2118/109765-PA http://dx.doi.org/10.2118/109765-PA

Citation

  • Hasan, A.R., Kabir, C.S., and Wang, X. 2009. A Robust Steady-State Model for Flowing-Fluid Temperature in Complex Wells. SPE Prod & Oper  24 (2): 269-276. SPE-109765-PA.

Discipline Categories

  • 5 Production and Operations
  • 5.4 Production Monitoring and Control
  • 5.6 Multiphase Flow in Wells

Keywords

  • fluid temperature, wellbore fluid-flow and heat-transfer modeling, heat transfer in deepwater wells, heat flow in complex well trajectory

Summary

This paper presents an analytic model for computing the wellbore-fluid-temperature profile for steady fluid flow. Although wells with a constant-deviation angle can be handled with existing analytic models, complex well architectures demand rigorous treatment. For example, changing geothermal-temperature-gradient and deepwater wells present significant challenges. Additionally, available analytic models rarely provide calculation methods for various required thermal parameters, such as the Joule-Thompson (J-T) coefficient and fluid expansivity.

The approach taken in this study entails dividing the wellbore into many sections of uniform thermal properties and deviation angle. The governing differential equation is solved for each section, with fluid temperature from the prior section as the boundary condition. This piecewise approach makes the model versatile, allowing step-by-step calculation of fluid temperature for the entire wellbore. We present simple, thermodynamically sound approaches for estimating thermal parameters.

Success is indicated when performance of the proposed model is compared with data from three wells, producing two-phase gas/oil mixture, single-phase oil, and single-phase gas. Sensitivity of the estimated fluid temperatures to various thermal properties is also examined with our model. Overall, the effects of the J-T coefficient and liquid expansivity are found to be significant.

Introduction

Modeling fluid-temperature and density profiles in wellbores is crucial for the design of production tubulars and artificial-lift systems, gathering pressure data for real-time reservoir management, and estimating flow rates from multiple producing horizons with distributed-temperature sensors.

Significant advances have occurred in wellbore-fluid-temperature modeling since the pioneering work of Ramey (1962). Ramey’s work addressed single-phase flowing-fluid temperature in a line-source well. In this regard, models of Alves et al. (1992), Sagar et al. (1991), and Hasan and Kabir (1994) are worthy of note. In particular, these models extended application to two-phase flows. Yet, the available analytic models are inadequate for direct application to modern directional wells that traverse formation with significantly varying thermal properties with multiple changes in deviation angles. In such cases, even the simple task of estimating geothermal temperature as a function of measured depth (MD) becomes nontrivial. Obviously, geothermal gradient strongly influences heat loss of wellbore fluids, requiring careful piecewise computation. The solution presented in this paper addresses these issues and lends itself to user-friendly spreadsheet computations, if one so chooses.

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History

  • Original manuscript received: 1 August 2007
  • Meeting paper published: 11 November 2007
  • Revised manuscript received: 26 February 2008
  • Manuscript approved: 12 March 2008
  • Published online: 1 May 2009
  • Version of record: 1 May 2009