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51313-02585-Evaluating Inhibitor Performance in CO2-Saturated Erosion-Corrosion Environments

Product Number: 51313-02585-SG
ISBN: 02585 2013 CP
Author: Richard Barker
Publication Date: 2013
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Over the last decade significant advancements in chemical inhibition have enabled operators to use carbon steel pipework in oil and gas facilities where sand production is a concern. The ability of these chemicals to reduce both the electrochemical corrosion reactions and the mechanical damage attributed to particle impingement is well documented. This paper presents a review of five commercially available oilfield corrosion inhibitors (four standard corrosion inhibitors and one high shear inhibitor) in an effort to establish their performance in erosion-corrosion environments. Experiments were conducted at 45°C using a submerged impinging jet (SIJ) in CO2-saturated conditions with a fluid velocity of 14 m/s and a sand loading of 500 mg/L. A combination of gravimetric measurements in-situ electrochemistry and surface profilometry allowed the inhibitors to be assessed based on a number of different parameters (i.e. reduction in weight loss in-situ corrosion rate and total penetration depth). The result demonstrated the important of surface analysis techniques when evaluating the performance of chemicals and showed that weight loss and in-situ electrochemical techniques alone could potentially provide misleading information on inhibitor performance in laboratory tests. This evaluation is particularly important in erosion-corrosion environments on sections of pipework where no semi-protective corrosion product formation occurs.
 

Over the last decade significant advancements in chemical inhibition have enabled operators to use carbon steel pipework in oil and gas facilities where sand production is a concern. The ability of these chemicals to reduce both the electrochemical corrosion reactions and the mechanical damage attributed to particle impingement is well documented. This paper presents a review of five commercially available oilfield corrosion inhibitors (four standard corrosion inhibitors and one high shear inhibitor) in an effort to establish their performance in erosion-corrosion environments. Experiments were conducted at 45°C using a submerged impinging jet (SIJ) in CO2-saturated conditions with a fluid velocity of 14 m/s and a sand loading of 500 mg/L. A combination of gravimetric measurements in-situ electrochemistry and surface profilometry allowed the inhibitors to be assessed based on a number of different parameters (i.e. reduction in weight loss in-situ corrosion rate and total penetration depth). The result demonstrated the important of surface analysis techniques when evaluating the performance of chemicals and showed that weight loss and in-situ electrochemical techniques alone could potentially provide misleading information on inhibitor performance in laboratory tests. This evaluation is particularly important in erosion-corrosion environments on sections of pipework where no semi-protective corrosion product formation occurs.
 

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