Menu
Search
Filters
Close
Menu

Save 20% on select titles with code HIDDEN24 - Shop The Sale Now

Top of Line Corrosion in Multiphase Gas Line Operational Feedbacks

Picture for Top of Line Corrosion in Multiphase Gas Line Operational Feedbacks
Available for download

The first case of top of line corrosion (TLC) in Tunu gas field was reported by Gunaltun et al in 19991. Inline
inspection (ILI) of two carbon steel pipelines distributing multiphase effluent, showed up to 50% metal
loss at 11.00 – 01.00 o’clock at several sections. Visual examination of a cut section showed that the top
of line was covered with iron carbonate layer with deep pits, and severe metal loss occurred on large
surfaces at these area.

Product Number: 51323-19486-SG
Author: Suryani, Rudi Rinaldi, Albertino Prabowo, Farih Mitraningsih, Aji Samiaji
Publication Date: 2023
$0.00
$20.00
$20.00

First Top of Line Corrosion (TLC) case was reported in 1999 in Tunu field, and since then, there were
several other pipelines from the neighboring fields, installed from 2007 to 2015 that were experiencing
TLC and was confirmed using in-line inspections (ILI). The TLC rates were found to be 0.5-1 mm/year in
average with the maximum rate of 2-3 mm/yr for gas containing CO2 up to 8.5% and around 80-90 barg
operating pressure with 80-90°C inlet temperature. Interestingly, on several pipelines, the maximum
corrosion rates happened at about 2-5 kilometers downstream the inlet risers. As part of mitigation, some
of the pipelines were designed with 10 mm corrosion allowance and when required, spray pigging and
recently, volatile corrosion inhibitor, are employed during operation at some of the pipelines. Thanks to
proper mitigations, despite high TLC rates, no adverse consequences were experienced on the pipelines.
This paper will discuss on the correlation on the field data and inspection results of the pipelines,
compares the predicted TLC rate with reality, and discusses the efficiency of various mitigation methods.
Lesson learned are also provided to illustrate the evolution of TLC mitigation strategies to ensure the
integrity of the pipelines.

First Top of Line Corrosion (TLC) case was reported in 1999 in Tunu field, and since then, there were
several other pipelines from the neighboring fields, installed from 2007 to 2015 that were experiencing
TLC and was confirmed using in-line inspections (ILI). The TLC rates were found to be 0.5-1 mm/year in
average with the maximum rate of 2-3 mm/yr for gas containing CO2 up to 8.5% and around 80-90 barg
operating pressure with 80-90°C inlet temperature. Interestingly, on several pipelines, the maximum
corrosion rates happened at about 2-5 kilometers downstream the inlet risers. As part of mitigation, some
of the pipelines were designed with 10 mm corrosion allowance and when required, spray pigging and
recently, volatile corrosion inhibitor, are employed during operation at some of the pipelines. Thanks to
proper mitigations, despite high TLC rates, no adverse consequences were experienced on the pipelines.
This paper will discuss on the correlation on the field data and inspection results of the pipelines,
compares the predicted TLC rate with reality, and discusses the efficiency of various mitigation methods.
Lesson learned are also provided to illustrate the evolution of TLC mitigation strategies to ensure the
integrity of the pipelines.

Product tags
Also Purchased
Picture for Dual Functional Corrosion Inhibitor Design And Testing For Top-Of-Line And Bottom Of Line Corrosion
Available for download

Dual Functional Corrosion Inhibitor Design And Testing For Top-Of-Line And Bottom Of Line Corrosion

Product Number: 51322-17787-SG
Author: Larry Chen, Nihal Obeyesekere, Jonathan Wylde, Michael Sim
Publication Date: 2022
$20.00

TOL corrosion is reported to occur in large diameter wet gas pipeline in stratified flow conditions
due to low fluid velocities1. With increasing distance from the inlet, the wet gas pipeline becomes
cooler as it loses heat to the environment. Such cooling causes water, hydrocarbon, and other
high vapor pressure species to condense on the pipe wall. The upper part of the pipe will
constantly be supplied with freshly condensed water while the less corrosive water saturated
with corrosion products will be drained along the pipe wall to the bottom of the line.
Picture for Role Of Acetic Acid On The Kinetics And Mechanism Of Carbon Steel Dissolution Under CO2 Top Of Line Corrosion
Available for download

Role Of Acetic Acid On The Kinetics And Mechanism Of Carbon Steel Dissolution Under CO2 Top Of Line Corrosion

Product Number: 51322-17818-SG
Author: Mariana Costa Folena, José Antônio da Cunha Ponciano Gomes, Frederick Pessu, Anne Neville, Richard Barker
Publication Date: 2022
$20.00

Top of line corrosion (TLC) is a specific corrosion mechanism observed in the oil and gas industry. This phenomena occurs under stratified or wet-gas flow regimes when the upper internal pipeline walls are sufficiently cooled (by heat transfer to the surrounding outer environment), promoting local condensation of water vapor. Carbon dioxide (CO2) and organic acids dissolving into the condensed water generate a change in the solution chemistry, ultimately influencing the corrosion kinetics of the contacting carbon steel.
Picture for Top of the Line Corrosion Mechanism for Multiphase Sour Gas Subsea Pipeline
Available for download

Top of the Line Corrosion Mechanism for Multiphase Sour Gas Subsea Pipeline

Product Number: 51323-18782-SG
Author: Faisal M. Al-Abbas, Marwan S Alsulami, Hadi F Al-Mansour Ayman A. Alabdullatif, Fadhel H. Asfoor, Mohammed M. Al Zamanan
Publication Date: 2023
$20.00

The hydrocarbon exploration in the ocean and deep sea was started as early as early as the 1850s, when the first drilling was carried out in California, USA. Other early oil explorations activities were later recorded in Pakistan (1886), Peru (1869), India (1890) and Dutch East Indies (1893). The development of an offshore industry is directly related to the development of subsea pipelines as well. As the industry expands towards deeper waters, the pipelines are required to have better materials, designs, operation practices and maintenance strategies to withstand the challenging environments. These pipelines are exposed to elevated temperatures, high pressures, and corrosive fluids.
Categories
Industry
Recently viewed
Popular tags
View all

Association for Materials Protection and Performance

© AMPP All Rights Reserved.
Membership Terms of Content Use
Contact Customer Support