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Abstract

Summary

The Ithaca-operated Captain field is located offshore in the U.K. sector of the North Sea and is made up of sandstone reservoirs of high quality and permeability. Produced water re-injection maintains pressure via water injection wells in reservoirs containing high viscosity oils (typically, ∼ 40 to 140cP). This unfavourable mobility ratio water over oil of 40 has resulted in early water breakthrough at the production wells, strong water coning and large volumes of bypassed oil. Fortunately, the clean, high net to gross Captain sands make these reservoirs good candidates for enhanced oil recovery using polymer flooding. To apply this process, Anionic polyacrylamide (HPAM) in liquid form was chosen as the preferred chemical and has been used since 2011. This application of polymer flooding has proven to be extremely successful in Captain, with significant acceleration of the waterflood bypassed reserves resulting in a substantial increase in incremental oil compared with the waterflood recovery.

Following the commercial success of these initial polymer floods, has come a desire to expand the original polymer flooding process to other areas of the field. When implementing this expansion, maintaining the target polymer viscosity is of utmost importance in order to preserve the desired mobility ratio and maintain the sweep efficiency of the process. Polymer viscosity loss may result from a number of different degradation mechanisms and the question of whether the polymer is able to retain its viscosity within the reservoir became a key uncertainty for future expansion.

To determine the degree of degradation of the polymer required a novel sampling and testing procedure. In this scheme, the sampling and measurement of produced polymer viscosity was carried out despite significant operational and technical challenges.

During execution of the sampling, the primary requirement was to enable produced polymer sampling from the sandface of a long horizontal and operational production well, without degrading the polymer during the sampling procedure. This sample then had to be maintained in anaerobic conditions to ensure no chemical degradation occurred during transfer for laboratory testing.

The laboratory testing results demonstrated that the HPAM polymer product used on Captain maintains considerable viscosity in the reservoir, having travelled for 3 years though the reservoir over a distance of more than 500 feet. These results clearly demonstrate that limited mechanical, chemical and/or biological degradation had occurred in the reservoir, giving increased confidence in our investment decisions to proceed with future polymer floods in the Captain field.

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2021-04-19
2024-04-19
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References

  1. 1.Berg, S., van Wunnik, J.2017. Shear Rate Determination from Pore-Scale Flow Fields. Transport in Porous Media, 117 (2), 229–246. https://doi.org/10.1007/s11242-017-0830-3
    [Google Scholar]
  2. 2.Beteta, A et al.2020. Polymer Chemical Structure and its Impact on EOR Performance.SPE-200441-MS. SPE Virtual Improved Oil Recovery Conference 2020. Aug 31 – Sep 4.
    [Google Scholar]
  3. 3.Clifford, P J., Sorbie, K S.1985. The Effects of Chemical Degradation on Polymer Flooding.SPE 13586. Presented at the International Symposium on Oilfield and Geothermal Chemistry, Phoenix, Arizona, 9–11 April.
    [Google Scholar]
  4. 4.Dupuis, G. and Nieuwerf, J.2020. A Cost-Effective EOR Technique To Reduce Carbon Intensity With Polymer Flooding and Modular Skids.Published in the Journal of Petroleum Technology, August 2020. https://pubs.spe.org/en/jpt/jpt-article-detail/?art=7545
    [Google Scholar]
  5. 5.Dwarakanath, V et al.2016. Permeability reduction due to use of Liquid Polymers and Development of Remediation Options.SPE-179657 -MS. Presented at the SPE Improved Oil Recovery Conference.Tulsa, Oklahoma. April 11–13.
    [Google Scholar]
  6. 6.Espinosa et al.2018. Dynamic Field Rheology, Filterability and Injectivity Characterization Using a Portable Measurement Unit. SPE-190329-MS.Presented at the SPE Improved Oil Recovery Conference at Tulsa, Oklahoma, April 14–18.
    [Google Scholar]
  7. 7.Garrepally, S., Jouenne, S et al.2020, Polymer Flooding - Towards a Better Control of Polymer Mechanical Degradation at the Near Wellbore. SPE-200373-MS.Presented at the SPE Improved Oil Recovery ConferenceTulsa, Oklahoma. April 18 – 22, postponed until August 31 –September 4.
    [Google Scholar]
  8. 8.Husveg, T., Stokka, M., Jouenne, S., Husveg, R.2019. The Development of a Low Shear Valve Suitable for Polymer Flooding.Presented at the 20th European Symposium on Improved Oil Recovery, EAGE. Pau, France. April 8–11.
    [Google Scholar]
  9. 9.JacksonA C et al.Surfactant Stimulation Results in Captain Field to Improve Polymer Injectivity for EOR. SPE-195747-MS.Presented at the SPE Offshore Europe Conference and Exhibition.Aberdeen, UK, September 3–6.
    [Google Scholar]
  10. 10.Maerker, J M., 1975. Shear Degradation of Partially Hydrolyzed Polyacrylamide Solutions.Society of Petroleum Engineers Journal, Volume 15, Issue 4, Pages 311 – 322. https://doi.org/10.2118/5101-PA
    [Google Scholar]
  11. 11.Moradi-Araghi, A., Doe, P.H.1987. Hydrolysis and Precipitation of Polyacrylamides in Hard Brines at Elevated Temperatures. SPE Reservoir Engineering, 2 (02), 189–198. SPE-13033-PA. https://doi.org/10.2118/13033-PA
    [Google Scholar]
  12. 12.Nurmi, L., Sandengen, K., Hanski, S., Molesworth, P., 2018. Sulfonated Polyacrylamides -Evaluation of Long Term Stability by Accelerated Aging at Elevated Temperature. SPE-190184-MS.Presented at the SPE Improved Oil Recovery Conference at Tulsa, Oklahoma, April 14–18. https://doi.org/10.2118/190184-MS
    [Google Scholar]
  13. 13.Osterloh, W T., Law, E J.1998. Polymer Transport and Theological Properties for Polymer Flooding in the North Sea. SPE 39694.Presented at the 1998 SPHDOE Improved Oil Recovery Symposium.Tulsa, Oklahoma. April 19–22.
    [Google Scholar]
  14. 14.Poulsen et al.2018. Results of the UK Captain Field Interwell EOR Pilot. SPE-190175-MS.Presented at the SPE Improved Oil Recovery Conference in Tulsa, Oklahoma. 14–18 April.
    [Google Scholar]
  15. 15.Seright, Skjevrak, I., I. 2015. Effect of Dissolved Iron and Oxygen on Stability of HPAM Polymers. SPE Journal, 20 (03), 433–441. SPE-169030. https://doi.org/10.2118/169030-PA
    [Google Scholar]
  16. 16.Sheng, J.J.2011. Modern Chemical Enhanced Oil Recovery. Boston: Gulf Professional Publishing.https://doi.org/10.1016/B978-1-85617-745-0.00005-X
    [Google Scholar]
  17. 17.Sheng, J.J.2013. Enhanced Oil recovery Field Case Studies. Texas: Gulf Professional Publishing. https://doi.org/10.1016/C2010-0-67974-0
    [Google Scholar]
  18. 18.Shook et al.2014. Optimizing Field Development of Greenfield Polymer Floods Using Experimental Design. SPE-170007-MS.Presented at the SPE Heavy Oil Conference –Canada, Alberta, June 10–12.
    [Google Scholar]
  19. 19.Shupe, R D.1981. Chemical Stability of Polyacrylamide Polymers. SPE 9299. J. Pet. Tech, Pages 1513–1529.
    [Google Scholar]
  20. 20.Sorbie, K S., Roberts, L J.1984. A Model for calculating Polymer Injectivity Including the Effects of Shear Degradation. SPE 12654.Presented at the SPE/DOE Fourth Symposium on Enhanced Oil Recovery, Tulsa, Oklahoma, 15–18 April.
    [Google Scholar]
  21. 21.Sorbie, K.S.1991. Polymer Improved Oil Recovery (1st ed.). Glasgow: Blackie. https://doi.org/10.1002/pi.4990280317
    [Google Scholar]
  22. 22.Sorbie, K S., Skauge, A.2019. Mobilization of By-Passed Oil by Viscous Crossflow in EOR Processes.Presented at the 20th European Symposium on Improved Oil Recovery.Pau, France. April 8–11.
    [Google Scholar]
  23. 23.Sorbie, K S., Ghafri, A Y., Skauge, A., Mackay, E J.2020. On the Modelling of Immiscible Viscous Fingering in Two-Phase Flow in Porous Media. Published online: September 29. https://doi.org/10.1007/s11242-020-01479-w
    [Google Scholar]
  24. 24.Swiecinski, F., Reed, P., Andrews, W.2016. The Thermal Stability of Polyacrylamides in EOR Applications.Presented at the SPE Improved Oil Recovery ConferenceTulsa, Oklahoma, USA, 11–13 April. SPE-179558-MS. https://doi.org/10.2118/179558-MS
    [Google Scholar]
  25. 25.Theriot et al.2018. Evaluation of Viscosity Loss of Viscosified Brine Solutions due to Shear Degradation in Distribution System Components. Presented at the SPE Improved Oil Recovery Conference at Tulsa, Oklahoma, April 14–18.
    [Google Scholar]
  26. 26.UK Oil and Gas Authority (OGA). 2017. Polymer Enhanced Oil Recovery Industry Lessons Learned. Published online October 20th 2017. https://www.ogauthority.co.uk/news-publications/publications/2017/polymer-enhanced-oil-recovery-industry-lessons-learned/
    [Google Scholar]
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