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Picture for 05520 The First ETFE Lined Dual-Laminate
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05520 The First ETFE Lined Dual-Laminate Equipment: A Case Study, After 13 Years of Service

Product Number: 51300-05520-SG
ISBN: 05520 2005 CP
Author: Debra McCauley, DuPont; Steven R. Linnemann, RL Industries Inc.
Publication Date: 2005
$20.00

Development of the new fluoropolymer Ethylene-tetrafluoroethylene (ETFE) and severe service environment conditions prompted ETFE’s use as a fabric backed lining laminate in dual-laminate fiberglass reinforced plastic (FRP) storage tanks – the first ever such use of this fluoropolymer.
Picture for 11360 Corrosion in Crude Distillation Unit Overhead Operations: A Comprehensive Review
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11360 Corrosion in Crude Distillation Unit Overhead Operations: A Comprehensive Review

Product Number: 51300-11360-SG
ISBN: 2011 11360 CP
Author: Brian Chambers, Sridhar Srinivasan, Kwei Meng Yap, Mark Yunovich
Publication Date: 2011
$20.00

 The purpose of this paper will be to: (a) review published literature to characterize and classify speciation related to the types of impurities encountered in opportunity crudes; and (b) describe and categorize published case studies of corrosion in crude unit overhead operations.
Picture for Qualification of Scale Dissolver Acid Systems for 3CR Alloyed Steel and 13CR Stainless Steels Well Materials
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51318-10969-Qualification of Scale Dissolver Acid Systems for 3CR Alloyed Steel and 13CR Stainless Steels Well Materials

Product Number: 51318-10969-SG
Author: Lucrezia Scoppio / Emilia Imbimbo / Sten Axelsen / Perry Nice / Giuseppe Mortali
Publication Date: 2018
$20.00

A corrosion testing program was performed aimed at evaluating scale dissolver packages to determine which package(s) were least corrosive and acceptable for use in wells constructed with 3Cr80 alloyed steel and L80 13 Cr (API 5CT grade) (1) tubulars.
Picture for Corrosion Behavior of Austenitic Stainless Steels and Nickel alloys in Simulated High Temperature Gethermal Environment
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51318-11058-Corrosion Behavior of Austenitic Stainless Steels and Nickel alloys in Simulated HT Geth. Environm.

Product Number: 51318-11058-SG
Author: Andri Isak Thorhallsson / Sigrun Nanna Karlsdottir / Andri Stefansson
Publication Date: 2018
$20.00

A 3-week corrosion testing of UNS N06625 was conducted in supercritical fluid at 350°C and 10 bars to simulate a geothermal environment where other alloys had been tested. Some localized corrosion occurred at a rate similar to previous results.
Picture for Corrosion Properties Of Alloy 35Mo In Crude Distillation Unit Overhead Service Conditions
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Corrosion Properties Of Alloy 35Mo In Crude Distillation Unit Overhead Service Conditions

Product Number: 51321-16833-SG
Author: Karen Picker; Josefin Eidhagen; Jonas Howing
Publication Date: 2021
$20.00
Picture for Impact of Vapor Phase Corrosion Inhibitors (VPCI) to Mitigate Corrosion in Refinery Overhead Systems
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Impact of Vapor Phase Corrosion Inhibitors (VPCI) to Mitigate Corrosion in Refinery Overhead Systems

Product Number: 51324-21227-SG
Author: Pradeep Lakshmanappa; Amutha Nagarajan; Indrajyoti Mukherjee; Sathees Kesavan; Hitesh Bagaria
Publication Date: 2024
$40.00
Corrosion in crude distillation unit overhead lines is primarily caused by hydrochloric acid at the dew point. Various other contaminants including air, organic acids, H2S, NH3, tramp amines, HCN, mercaptans, phenols, etc. also play a role in overhead corrosion. Mitigation strategies include process solutions such as wash water systems and temperature control, and chemical solutions including amine-based neutralizers and film-forming inhibitors. Despite implementing these strategies, corrosion is invariably observed in the overhead system. Conventional “non-volatile” filmers rely on free liquid to cover the metallurgy. However, the complex nature of overhead geometry and fluid flow make complete metal coverage challenging. This necessitates a different strategy to achieve protection. Here, we present a first of its kind Vapor Phase Corrosion Inhibitor (VPCI) for protecting overhead systems. Several VPCI candidates were studied in the lab for performance, volatility, and risks (emulsification, pentane solubility, amine salt fouling, thermal stability). Promising VPCI was field trialed in several refineries.
Picture for Troubleshooting Of Main Fractionator Overhead Corrosion in Condensate Splitting Unit Using Ionic Equilibria Modelling
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Troubleshooting Of Main Fractionator Overhead Corrosion in Condensate Splitting Unit Using Ionic Equilibria Modelling

Product Number: 51323-19325-SG
Author: Sudharsanan Soundararajan
Publication Date: 2023
$20.00

This twin train Condensate Splitting Unit (CSU) is basically an atmospheric distillation unit processing predominantly Middle Eastern condensate along with other non-system condensate. The products from this unit are Light/Heavy Naphtha, Kerosene, Light/Heavy Gas Oil and Atmospheric residue. There is no desalter in this unit and preheated feed is flashed in Pre-flash column to separate out light and medium naphtha.
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