Study of the two-phase liquid loading phenomenon by applying CFD techniques

Authors

  • J Vieiro
  • M Asuaje
  • G Polanco

DOI:

https://doi.org/10.1260/1750-9548.7.4.301

Abstract

In order to understand the liquid loading phenomenon, 2D (axisymmetric) numerical simulations were performed. This phenomenon appears when the gas velocity reduces to a value below the critical speed of drop extraction in two-phase production wells, and as consequence liquid is accumulated in the tubing, increasing the pressure drop and reducing the flow rate within the tube. Simulations were made using air-water as working fluids over a vertical pipe of 4 meters long through a commercial package of CFD. Comparison between the simulation results and the experimental data available in the literature shows a good capability of homogeneous models to predict the flow characteristics for a given velocity range close to the critical gas velocity; over 100% of this parameter the model significantly overestimates the pressure drop.

References

Lea, J. F., Nickens, H. V. and Wells, M. R., Gas well deliquification, Second Edition, Gulf Professional Publishing, 2008.

Turner, R. G., Hubbard, M. G. and Dukler, A. E., Analysis and Prediction of Minimum Flow Rates for the Continuous Removal of Liquid from Gas Wells, Journal of Petroleum Technology, 1969, 21 (11), 1475-1482. https://doi.org/10.2118/2198-pa

Hinze, J. O., Fundamentals of the Hydrodynamic Mechanism of Splitting in Dispersion Processes, AIChE Journal, 1955, 1 (30), 289-295. https://doi.org/10.1002/aic.690010303

Coleman, S. B., Clay, H. B., McCurdy, D. G. and Norris, L. H. III, The Blowdown-Limit Model, Journal of Petroleum Technology, 1991, 43 (3), 339-343. https://doi.org/10.2118/20282-pa

Han, H., A study of entrainment in two-phase upward cocurrent annular flow in a vertical tube, Ph. D. Thesis, University of Saskatchewan, 2005.

Zhu, Z. F., A Study of the Interfacial Features of Gas-Liquid Annular Two-Phase, M. Sc. Thesis, University of Saskatchewan, 2004.

Van 't Westende, J. M. C., Kemp, H. K., Belt, R. J., Portela, L. M., Mudde, R. F. and Oliemans, R. V. A., On the role of droplets in cocurrent annular and churn-annular pipe flow, International Journal of Multiphase Flow, 2007, 33, 595-615. https://doi.org/10.1016/j.ijmultiphaseflow.2006.12.006

Parvareh, A., Rahimi, A., Alizadehdakhel, A. and Alsairafi, A. A., CFD and ERT investigations on two-phase flow regimes in vertical and horizontal tubes, International Communications in Heat and Mass Transfer, 2010, 37 (3), 304-311. https://doi.org/10.1016/j.icheatmasstransfer.2009.11.001

Celik, I. B., Ghia, U., Roache, P. J. and Freitas, C. J., Procedure for Estimation and Reporting of Uncertainty Due to Discretization in CFD Applications, Journal of Fluids Engineering, 2008, 130 (7). https://doi.org/10.1115/1.2960953

Zabaras, G., Dukler, A. E. and Moalem-Maron, D., Vertical upward cocurrent gas-liquid annular flow, AIChE Journal, 1986, 32 (5) 829-843. https://doi.org/10.1002/aic.690320513

Fore, L. B., and Dukler, A. E., Droplet deposition and momentum transfer in annular flow, American Institute of Chemical Engineers Journal, 1995, 41 (9), 2040-2047. https://doi.org/10.1002/aic.690410904

Published

2013-12-31

How to Cite

Vieiro, J., Asuaje, M. and Polanco, G. (2013) “Study of the two-phase liquid loading phenomenon by applying CFD techniques”, The International Journal of Multiphysics, 7(4), pp. 301-312. doi: 10.1260/1750-9548.7.4.301.

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Section

Articles