Search
Filters
Close

Celebrate World Corrosion Awareness Day with 20% off eCourses and eBooks with code WCAD2024 at checkout!

10366 Estimation of the Replacement Time Interval Due to CO2 Corrosion in Oilwells by Random Process Modelling

Product Number: 51300-10366-SG
ISBN: 10366 2010 CP
Author: Raymundo Case, PhD
Publication Date: 2010
$0.00
$20.00
$20.00
The predictive assessment of the optimum replacement time due to the corrosion damage accumulation allows the control of associated operating expenditures in oilfield operations. To such purpose a model was developed for the assessment of CO2 corrosion related damage accumulation.

The model proposed is based on the calculation of the CO2 corrosion damage accumulation and failure probability as a sequence of random processes. The distribution of failure likelihood is then assessed in terms of a Markov random process from both an Ergodic, or repair, and an Absorbent, or unhindered damage accumulation, scenarios.

The value of the optimum replacement time estimated by the model proposed was compared with an actual documented case from a mature oilfield development. The modelled results indicate that the mean transition time for failure without mitigation is around 6 years which coincide with the observed behaviour from the field. The modelled optimum replacement time interval for this case was estimated as 5 years of service time.

Keywords: CO2 corrosion, stochastical models, localized corrosion failure, reliability prediction
The predictive assessment of the optimum replacement time due to the corrosion damage accumulation allows the control of associated operating expenditures in oilfield operations. To such purpose a model was developed for the assessment of CO2 corrosion related damage accumulation.

The model proposed is based on the calculation of the CO2 corrosion damage accumulation and failure probability as a sequence of random processes. The distribution of failure likelihood is then assessed in terms of a Markov random process from both an Ergodic, or repair, and an Absorbent, or unhindered damage accumulation, scenarios.

The value of the optimum replacement time estimated by the model proposed was compared with an actual documented case from a mature oilfield development. The modelled results indicate that the mean transition time for failure without mitigation is around 6 years which coincide with the observed behaviour from the field. The modelled optimum replacement time interval for this case was estimated as 5 years of service time.

Keywords: CO2 corrosion, stochastical models, localized corrosion failure, reliability prediction
Product tags
Also Purchased
Picture for 10326 Effect of Corrosion Inhibitor Active Components on Corrosion Inhibition in a Sweet Environment
Available for download

10326 Effect of Corrosion Inhibitor Active Components on Corrosion Inhibition in a Sweet Environment

Product Number: 51300-10326-SG
ISBN: 10326 2010 CP
Author: Kenny Tsui, Jennifer E. Wong and Neil Park
Publication Date: 2010
$20.00
Picture for 10333 Inhibition of Galvanic Corrosion of Carbon Steel and Nickel Alloy in Oil and Gas Production
Available for download

10333 Inhibition of Galvanic Corrosion of Carbon Steel and Nickel Alloy in Oil and Gas Production Applications

Product Number: 51300-10333-SG
ISBN: 10333 2010 CP
Author: Feng Gui, Davion Hill, Cheolho Kang, and Carlos Joia
Publication Date: 2010
$20.00
Picture for 10325 Testing Requirements of Corrosion Inhibitor Qualification for Pipeline Applications
Available for download

10325 Testing Requirements of Corrosion Inhibitor Qualification for Pipeline Applications

Product Number: 51300-10325-SG
ISBN: 10325 2010 CP
Author: Jorge L. Pacheco, Faridah Che Ibrahim, and Robert J. Franco
Publication Date: 2010
$20.00