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Picture for Corrosion issues in the conversion of vegetable and waste oils to produce biofuels
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Corrosion issues in the conversion of vegetable and waste oils to produce biofuels

Product Number: 51323-19308-SG
Author: Fouad Andari, Jean Kittel, François Ropital, Joana Fernandes, Laure Dodelin
Publication Date: 2023
$20.00

To limit the impact of greenhouse gas emissions on climate change, the use of conventional hydrocarbons needs to be reduced significantly. The global demand for biofuels is thus expected to grow during the present decade. Hydrogenated Vegetable Oil (HVO) is one of the predominant biofuels produced by converting lipidic feedstocks (vegetable oils, animal fats, waste cooking oils, …) through a conventional refinery hydrotreatment (HDT) process.
Picture for Corrosion Looping for Down Stream Petroleum Plants: An Enigma for RBI Engineers A Perspective From
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Corrosion Looping for Down Stream Petroleum Plants: An Enigma for RBI Engineers A Perspective From the Review of Mechanical Integrity Systems

Product Number: 51317--9178-SG
ISBN: 9178 2017 CP
Author: Muazu Mohammed
Publication Date: 2017
$20.00

A review of the issues in the implementations of Risk Based Inspection (RBI) system for refineries and petrochemicals - to simplify and harmonize corrosion loops (as captured on Process Flow Diagrams (PFDs)) and corrosion circuits as captured in piping and instrumentation diagrams (P&IDs).
Picture for Corrosion Management for Offshore Wet Sour Gas Carbon Steel Pipeline with Closed Loop MEG Regeneration System
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Corrosion Management for Offshore Wet Sour Gas Carbon Steel Pipeline with Closed Loop MEG Regeneration System

Product Number: 51323-18996-SG
Author: Chun Ho, Leow, Cheng Ai, Khoo, Hock Guan, Ong
Publication Date: 2023
$20.00

Project A is being developed by the company with two fields about 220 km distance from Bintulu, Sarawak. The fields are classified as sour with estimated H2S concentration up to 5,000 ppm and 3.8 mol% CO2. The two fields are mainly Field A1 and Field A2 with approximately 20km apart. Field A1 will have two dry xmas trees, drilled from the Platform A while Field A2 will be developed with 2 subsea wells and supporting subsea infrastructures.
Picture for Corrosion Management Improvements in Liquids-Rich Shale Play - Pipeline Internal Corrosion Mitigation Case Studies
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Corrosion Management Improvements in Liquids-Rich Shale Play - Pipeline Internal Corrosion Mitigation Case Studies

Product Number: 51324-20990-SG
Author: Monica Fernandez; Chris Jeske; Robert Terry; Ruben Carrera
Publication Date: 2024
$40.00
This paper details the process followed to enhance the pipeline internal corrosion management during operational stage in a liquids-rich shale play, focusing on pipeline internal corrosion mitigation. The process involves several key steps, encompassing a thorough review of historical data (operational conditions, fluid chemistry, corrosion coupons, chemical treatments, pigging activities, inspection results, among others), meticulous data analysis, strategic scheduling, implementation of short-term, mid-term, and long-term actions, followed by periodic monitoring to evaluate barrier performance in conjunction with an inspection plan to confirm asset integrity and optimize resource utilization. The improvements have considered industry best practices, know-how, lessons learned, valuable insights gained from past failures, challenges encountered within upstream operations for corrosion and integrity activities execution, and the actions taken to overcome them.
Picture for Corrosion Management in Hydrocracking and Hydroprocessing Units
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Corrosion Management in Hydrocracking and Hydroprocessing Units

Product Number: MPWT19-14442
Author: Hendrik J. Debruyn
Publication Date: 2019
$0.00

Hydrocracking and other refinery hydroprocessing units have a common goal to convert organic sulfur compounds to hydrogen sulfide (H2S) that can be removed, thereby producing low-sulfur refinery products. Corrosion and equipment degradation risks range from high-temperature hydrogen attacks (HTHA) to ammonium bisulfide and ammonium chloride corrosion in the downstream heat recovery and fluid separation equipment.
This paper provides an overview of corrosion management principles that can be applied to reduce operating risks in new and existing units, focusing equipment susceptible to ammonium bisulfide (NH4HS) and ammonium chloride (NH4Cl) corrosion. Best practices for materials selection, as well as designing for corrosion management through adequate provision of corrosion management related instrumentation and sampling points are covered.
Corrosion Management Learnings for Storage Tanks
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Corrosion Management Learnings For Atmospheric Storage Tanks

Product Number: 51322-17951-SG
Author: Gulnur Badalova, Mikael Johansson
Publication Date: 2022
$20.00

The terminal is subdivided for Oil, Gas and Produced Water plants. Each of these plants has number of storage tanks. The age of the tanks varies between 15-25 years.  The products held within these tanks varies, from crude oil, condensate, produced water, potable water, to off spec oil and diesel fuel.

Most of the tanks within the facility have a similar CP arrangement and design.  Each tank base is protected by an impressed current grid mesh anode buried in compacted, clean, sand backfill beneath the tank base and is powered by a transformer-rectifier placed outside the bund wall or within an electrical switch room.  Permanent reference electrodes are installed beneath all tank bases to enable accurate potential measurements. Reference electrodes vary from Copper/Copper Sulphate, Silver/Silver Chloride to Zinc.  
Picture for Corrosion Management Review of Sour Gas Pipeline – A Case Study
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Corrosion Management Review of Sour Gas Pipeline – A Case Study

Product Number: 51323-18855-SG
Author: Muntathir M. Al-Jumaah, Faisal M. Al-Mutahhar, Muhammad A. Sherwani
Publication Date: 2023
$20.00

This paper reviews the corrosion management for a critical sour gas pipeline operated by Saudi Aramco. The 38-inch diameter pipeline transports untreated sour gas from Crude Processing Facility (CPF) to downstream Gas Plant and spans a total distance of 145 km. To prevent internal corrosion inside the pipeline, the wet sour gas is dehydrated using Tri-Ethylene Glycol (TEG) unit.
Corrosion Mechanisms Of Mild Steel In The Presence Of Formic And Acetic Acids
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Corrosion Mechanisms Of Mild Steel In The Presence Of Formic And Acetic Acids

Product Number: 51322-17944-SG
Author: Sahithi Ayyagari, Maryam Eslami, Bruce Brown, Srdjan Nesic
Publication Date: 2022
$20.00

Corrosion is a surface phenomenon, which is defined as the deterioration of a material due to chemical and/ or electrochemical reactions. The continued interest in understanding corrosion phenomena and devising mitigation methods stems from the potential influence corrosion has on infrastructural damage across diverse industries. The most prevalent forms of corrosion encountered in the oil and gas industry are referred to as sweet and sour, corresponding to aqueous CO2 and H2S environments, respectively. The presence of an aqueous phase in these environments leads to the formation of a weak acid which is understood to be detrimental to the service life of carbon steel pipelines, when not properly mitigated. 
Picture for Corrosion Mitigation Of Deepwater, 143-Km Long Multiphase Pipelines
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Corrosion Mitigation Of Deepwater, 143-Km Long Multiphase Pipelines

Product Number: 51321-16520-SG
Author: Alyn Jenkins/ Marcus Rossiter/ William Cardwell/ Michael Reid/ Brian Messenger
Publication Date: 2021
$20.00
Picture for Corrosion Mitigation Strategies in Forced Oxidation Wet Flue Gas Desulfurization Absorbers Made of U
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Corrosion Mitigation Strategies in Forced Oxidation Wet Flue Gas Desulfurization Absorbers Made of UNS S32205 Duplex Stainless Steel

Product Number: 51315-5947-SG
ISBN: 5947 2015 CP
Author: Brett Tossey
Publication Date: 2015
$0.00
Picture for Corrosion Monitoring From The Comfort Of Your Office, Home Or Car
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Corrosion Monitoring From The Comfort Of Your Office, Home Or Car

Product Number: 51321-16519-SG
Author: Art Leach
Publication Date: 2021
$20.00
Picture for Corrosion Monitoring of Oil Storage Tanks
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Corrosion Monitoring of Oil Storage Tanks

Product Number: 51319-12822-SG
Author: C Brossia
Publication Date: 2019
$20.00

Corrosion of oil storage tanks used to store crude oil and produced water in an operating oil field were identified as a potential safety issue when inspection results indicated significant wall loss due to internal corrosion. Corrosion was noted to be particularly severe in the lower sections of some tanks where sludge layers were believed to have formed. Previous attempts to monitor for corrosion using mass loss coupons and acoustic emission were found to provide less than adequate information regarding corrosion risk. Corrosion monitoring using alternate approaches utilized to provide additional information regarding possible corrosion of the tank at different locations within the tanks.
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