SPE Drilling & Completion
Volume 25, Number 1, March 2010, pp. 53-57

SPE-121742-PA

Design and Development of a Novel Process To Treat Drilling-Fluid Slops: A Positive Environmental and Economic Impact

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DOI  More information 10.2118/121742-PA http://dx.doi.org/10.2118/121742-PA

Citation

  • Dixit, R. and Patel, A. 2010. Design and Development of a Novel Process To Treat Drilling-Fluid Slops: A Positive Environmental and Economic Impact. SPE Drill & Compl  25 (1): 53-57. SPE-121742-PA. doi: 10.2118/121742-PA.

Discipline Categories

  • 2.5.4 Waste Management

Keywords

  • slop, water, ozone, oil-in-water, demulsifier

Summary

Slop mud, created by water contamination of invert drilling fluids during displacement and cleaning activities, has been successfully treated at source to recover the drilling-fluid phase and water phase. This method included treating the slop mud with a biodegradable demulsifier. The recovered drilling fluid can be reconditioned to acceptable properties for reuse or can be sent for disposal. The recovered/separated slop water phase is contaminated with hydrocarbons and cannot be discharged in an offshore environment unless it meets the discharge criteria of < 30 mg/L of oil in water. Thus, it becomes imperative for the operator to treat the water at source, reduce the enormous expenses associated with transportation/disposal, and embark upon a potentially significant environmental issue. This was achieved by development of an on-site treatment process including filtration, ozonation, and phase separation.

A synthetic-based drilling fluid contaminated with water was separated with a biodegradable demulsifier. The addition of the surfactant resulted in phase separation (i.e., separated drilling-fluid and water phases). As tested by the approved International Organization for Standardization (ISO) method, the separated water phase was found to have oil-in-water content of 4,000 mg/L, which is unacceptable for discharge. The separated water then was treated with ozone. The ozone-treated water was allowed to separate in two phases (i.e., clarified water phase and organic rich phase). The oil-in-water content of the clarified ozone-treated water phase was found to be 30 mg/L, thus reducing the oil-in-water content by 99%.

This paper will present the demulsification methodology, chemistry of ozonolysis, and results obtained to meet or exceed the oil-in-water discharge limits of 30 mg/L. The environmental and economic impact of the process will be discussed.

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History

  • Original manuscript received: 19 February 2009
  • Meeting paper published: 20 April 2009
  • Manuscript approved: 15 April 2009
  • Published online: 22 December 2009
  • Version of record: 11 March 2010