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Application and Evaluation of Scale Dissolver Treatments

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Abstract In order to provide an improved basis for the design of barium sulfate scale dissolver treatments both laboratory testing and monitoring of field applications were carried out. The deleterious effects of mixing produced water with dissolver prior to contacting scale are shown. Increasing total dissolved solids (TDS) levels can reduce dissolution depending upon temperature. Precomplexation with divalent cations reduces the capacity of the dissolver to solubilize solid scales. Magnesium may adversely affect dissolver performance at elevated temperatures. Several oil and gas wells were closely monitored during initial flowback after treatment. Samples were collected on a frequent basis and analyzed for pH, dissolver content, chlorides and various cations. The resulting data were used to construct flowback profiles for evaluation of the treatments. Evidence of scale dissolution is presented. The presence of an incompatible flush brine was discovered in one case and possible reverse order of addition of preflush and dissolver in another. The importance of establishing and following treatment procedures is briefly discussed.
NACE International
Title: Application and Evaluation of Scale Dissolver Treatments
Description:
Abstract In order to provide an improved basis for the design of barium sulfate scale dissolver treatments both laboratory testing and monitoring of field applications were carried out.
The deleterious effects of mixing produced water with dissolver prior to contacting scale are shown.
Increasing total dissolved solids (TDS) levels can reduce dissolution depending upon temperature.
Precomplexation with divalent cations reduces the capacity of the dissolver to solubilize solid scales.
Magnesium may adversely affect dissolver performance at elevated temperatures.
Several oil and gas wells were closely monitored during initial flowback after treatment.
Samples were collected on a frequent basis and analyzed for pH, dissolver content, chlorides and various cations.
The resulting data were used to construct flowback profiles for evaluation of the treatments.
Evidence of scale dissolution is presented.
The presence of an incompatible flush brine was discovered in one case and possible reverse order of addition of preflush and dissolver in another.
The importance of establishing and following treatment procedures is briefly discussed.

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