DETERMINATION OF THE BEST-FIT MULTIPHASE FLOW CORRELATION FOR HIGH WATER-CUT WELLS USING PROSPER

Authors

  • Issham Ismail Department of Petroleum Engineering, Faculty of Chemical and Energy Engineering, Universiti Teknologi Malaysia, 81310 UTM Johor Bahru, Johor, Malaysia
  • Lim Teck Shern Department of Petroleum Engineering, Faculty of Chemical and Energy Engineering, Universiti Teknologi Malaysia, 81310 UTM Johor Bahru, Johor, Malaysia
  • Ariffin Samsuri Department of Petroleum Engineering, Faculty of Chemical and Energy Engineering, Universiti Teknologi Malaysia, 81310 UTM Johor Bahru, Johor, Malaysia
  • Muhamad Shafie Issham Department of Petroleum Engineering, Faculty of Chemical and Energy Engineering, Universiti Teknologi Malaysia, 81310 UTM Johor Bahru, Johor, Malaysia
  • Ling Hua Sid Department of Petroleum Engineering, Faculty of Chemical and Energy Engineering, Universiti Teknologi Malaysia, 81310 Johor Bahru, Malaysia
  • Norhafizuddin Husein@Yusof Department of Petroleum Engineering, Faculty of Chemical and Energy Engineering, Universiti Teknologi Malaysia, 81310 Johor Bahru, Malaysia
  • Natalie Vanessa Boyou Department of Petroleum Engineering, Faculty of Chemical and Energy Engineering, Universiti Teknologi Malaysia, 81310 Johor Bahru, Malaysia
  • Zainal Zakaria Department of Petroleum Engineering, Faculty of Chemical and Energy Engineering, Universiti Teknologi Malaysia, 81310 Johor Bahru, Malaysia

DOI:

https://doi.org/10.11113/jt.v80.11563

Keywords:

High water-cut well, multiphase flow correlation, pressure drop, Prosper, vertical lift performance

Abstract

Pressure drop in a vertical or deviated borehole is mainly due to hydrostatic changes and friction when the produced fluids flow to the surface. When the oil is flowing upwards, the flowing pressure along the tubing string will drop and gas starts to liberate from the oil. Thus, multiphase flow forms in the tubing string. Hence, adequate modeling of vertical lift performance is required to predict the pressure drop and subsequently the wellbore pressure. The bottomhole pressure prediction was realized by using PROSPER, a program developed by Petroleum Experts. The data of oilwell X-01 with high water cut (i.e., 56%) in field X was used in this research work. The most accurate correlation was chosen from 12 selected built-in correlations to predict the pressure drop via gradient matching. A sensitivity analysis has been done to observe the parameters that affected the vertical lift performance of a high water cut well. These parameters were tubing diameter, gas-oil ratio, wellhead pressure, water cut, and tubing roughness. The results show that Dun and Ros original correlation appeared to be the best-fit correlation for well X-01. Results from sensitivity analysis indicated that reduction of wellhead pressure from 390 psi to 285.3 psi could increase liquid rate by 13.2%. An adjustment of wellhead pressure gave the most significant impact on the production rate of well X-01 as compared to other four parameters studied.

References

Ismail, I. 1990. Optimization of Tubing Size Selection in a Mature Offshore Field. Thesis. Imperial College of London.

Brown, K. E. 1984. The Technology of Artificial Lift Methods. Vol. 4, Tulsa: PennWell.

Brown, K. E. 1990. Petroleum Production Technology of Lifting Methods. Vol. 4. Beijing: Petroleum Industry Press.

Ismail, A. S. I., Ismail, I., Zoveidavianpoor, M., Mohsin, R., Piroozian, A., Misnan, M. S. & Sariman, M. Z. 2015. Review of Oil–water through Pipes. Flow Measurement and Instrumentation. 45: 357-374.

Ismail, A. S. I., Ismail, I., Zoveidavianpoor, M., Mohsin, R., Piroozian, A., Misnan, M. S. & Sariman, M.Z. 2015. Experimental Investigation of Oil–water Two-phase Flow in Horizontal Pipes: Pressure Losses, Liquid Holdup and Flow Patterns. Journal of Petroleum Science and Engineering. 127: 409-420.

Piroozian, A., Hemmati, M., Ismail, I., Manan, M.A., Rashidi, M. M. & Mohsin, R. 2017. An Experimental Study of Flow Patterns pertinent to Waxy Crude Oil-water Two-phase Flows. Chemical Engineering Science. 164(2017): 313-332.

Bai, Y. and Bai, Q. 2005. Subsea Pipelines and Risers. 2nd ed. Amsterdam: Elsevier Science.

Poettmann, F. H. and Carpenter, P. G. 1952. Multiphase Flow of Gas, Oil and Water through Vertical Flow Strings. Drill. and Prod. Pract. Dallas: American Petroleum Institute.

Duns Jr., H. and Ros, N. C. J. 1963. Vertical Flow of Gas and Liquid Mixtures in Wells. Proc. 6th World Petroleum Congress. Section II-Paper 22-PD6, Frankfurt. 451-465.

Fancher, G. H. Jr. and Brown, K. E. 1963. Prediction of Pressure Gradients for Multiphase Flow in Tubing. SPE Journal. March: 59-69.

Hagedorn, A. R. and Brown, K. E. 1965. Experimental Study of Pressure Gradients Occuring during Continuous Two-phase Flow in Small Diameter Vertical Conduits. Journal of Petroleum Technlogy. April: 475-484.

Orkiszewski, J. 1967. Predicting Two-phase Pressure Drops in Vertical Pipe. Journal of Petroleum Technology. 19(6): 829-838.

Govier, G. W. and Aziz, K. 1972. The Flow of Complex Mixtures in Pipes. London: Von Van Nostrand Reinhold.

Beggs, H. D. and Brill, J. P. 1973. A Study of Two Phase Flow in Inclined Pipes. Journal of Petroleum Technology. May: 607-617.

Mukherjee, H., and Brill, J. P. 1985. Pressure Drop Correlation for Inclined Two-Phase Flow. Journal of Energy Resources Technology. 107: 549-554.

Hasan, A. R. and Kabir, C. S. 1992. Gas Void Fraction in Two-phase Up-flow in Vertical and Inclined Annuli. Int. J. Multiphase Flow. 18(2): 279-293.

Piroozian, A., Hemmati, M., Ismail, I., Manan, M. A., Bayat, A. E., and Mohsin, R. 2016. Effect of Emulsified Water on the Wax Appearance Temperature of Water-in-Waxy-Crude-Oil Emulsions. Thermochimica Acta. 637: 132-142.

Pucknell, J. K., Manson, J. N. E., and Vervest, E. G. 1993. An Evaluation of Recent Mechanistic Models of Multiphase Flow for Predicting Pressure Drops in Oil and Gas Wells. Presented at Offshore European Conference, Aberdeen, September 7-10.

Yahaya, A. U. and Gahtani, A. A. 2010. A Comparative Study between Empirical Correlations and Mechanistic Models of Vertical Multiphase Flow. Presented at the 2010 SPE/DGS Annual Technical Symposium and Exhibition, Al-Khobar, Saudi Arabia, April 4-7.

Fossmark, M. G., Kulkarni, K. N., and Lauritsen, H. T. 2012. Vertical Lift Models Substantiated by Stajford Field Data. Presented at EAGE Annual Conference & Exhibition incorporating SPE Europec held in Copenhagen, Denmark, June 4-7.

Gilbert, W. E. 1954. Flowing and Gas Lift Well Performance. Drill. and Prod. Pract. Dallas: American Petroleum Institute.

Mach, J., Proano, E., and Brown, K. E. 1979. A Nodal Approach for Applying Systems Analysis to the Flowing and Artificial Lift Oil or Gas Well. SPE 8025.

Beggs, H. D. 2003. Production Optimization Using Nodal Analysis. 2nd edition, Tulsa: OGCI & Petroskill.

Wu, R. & Rosenegger L. 2000. Comparison of PVT Properties from Equation of State Analysis and PVT Correlations for Reservoir Studies. Presented at 50th Annual Technical Meeting in Calgary, Alberta, June 14-18.

Fevang, Ø, Fossmark, M. G., Kulkarni, K. N., Lauritsen, H. T. and Skjaeveland, S. M. 2012. Vertical Lift Models Substantiated by Statfjord Field Data. SPE 154803. Presentated at the EAGE Annual Conference & Exhibition, Copenhagen, Denmark, June 4-7.

Abu, T. 2007. Optimization of Gas Lift System in Varg Field. Thesis. Faculty of Science and Technology, Unversitetet Stavanger, Stavanger, Norway.

Munson, B. R., Young, D. F. and Okiishi, T. H. 2002. Fundamentals of Fluid Mechanics. 4th ed. Hoboken, New Jersey: John Wiley and Sons.

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Published

2018-02-26

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Section

Science and Engineering

How to Cite

DETERMINATION OF THE BEST-FIT MULTIPHASE FLOW CORRELATION FOR HIGH WATER-CUT WELLS USING PROSPER. (2018). Jurnal Teknologi, 80(3). https://doi.org/10.11113/jt.v80.11563