Arthur Steven Metcalf, SPE, BJ Services Company, U.S.A.
Abstract
Acid stimulation using coiled tubing conveyance is becoming commonplace; however, protection of these coils from acid corrosion is challenging. Add to this the requirement for usage of materials less damaging to the environment, and the task approaches the impossible at high temperatures >250) and high acid strengths >20).
The common requirement of corrosion weight loss for jointed tubulars (N-80, J-55, L-80, CR-13, etc.) is <0.05 pounds per square foot and <0.02 to <0.03 for coiled tubing. Increasing acid strength and/or temperature causes an increase in the corrosion inhibitor package cost by nearly 400% as the conveyance tubular changes from N-8O to coiled tubing.
Included in this paper is a comparison of corrosion data generated for hydrochloric acid systems from 20 to 28% on coiled tubing, N-80 and CR-13. The inhibitor evaluated is a blend of select solvents, activated ketone, a small quantity of acetylenics, surfactant and an amine. This material is given a Group "C" designation under the Revised Offshore Chemical Notification Scheme. A summary of the information used to define this inhibitor's Group "C" designation is presented.
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