Menu
Search
Filters
Close
Menu

Save 20% on select best sellers with code MONSTER24 - Shop The Sale Now

03332 CORROSION INHIBITOR DEVELOPMENTS FOR OFFSHORE GAS GATHERING SYSTEMS ON CANADA'S ATLANTIC COAST

Picture for 03332 CORROSION INHIBITOR DEVELOPMENTS
Available for download
Product Number: 51300-03332-SG
ISBN: 03332 2003 CP
Author: M. R. Gregg, A. Sharp, K. Bartrip
$0.00
$20.00
$20.00
A laboratory inhibitor selection study was conducted to select suitable corrosion inhibitors for managing corrosion in wet sub-sea pipelines containing ethylene glycol / salt water fluid mixtures. Several inhibitors were screened using static autoclave partitioning tests simulating worst case field conditions at 248 kPa (36 psi) CO2 partial pressure and 75 ° C (167 F). All inhibitors studied afforded excellent protection against general corrosion but three chemistries were also very effective in preventing pitting attack. Uninhibited lean (~ 20% water content) and rich ( ~ 50% water content) ethylene glycol/water mixtures (MEG) were also studied under static and dynamic flow conditions to evaluate pitting corrosion tendency of sodium chloride salt spike (750 ppm, 5,000 ppm, 8,000 ppm and 80,000 ppm chloride) additions to theMEG relative inhibited fluids. Key Words: wet sub sea pipeline, CO2 corrosion, salty ethylene glycol, corrosion control, hydrate control
A laboratory inhibitor selection study was conducted to select suitable corrosion inhibitors for managing corrosion in wet sub-sea pipelines containing ethylene glycol / salt water fluid mixtures. Several inhibitors were screened using static autoclave partitioning tests simulating worst case field conditions at 248 kPa (36 psi) CO2 partial pressure and 75 ° C (167 F). All inhibitors studied afforded excellent protection against general corrosion but three chemistries were also very effective in preventing pitting attack. Uninhibited lean (~ 20% water content) and rich ( ~ 50% water content) ethylene glycol/water mixtures (MEG) were also studied under static and dynamic flow conditions to evaluate pitting corrosion tendency of sodium chloride salt spike (750 ppm, 5,000 ppm, 8,000 ppm and 80,000 ppm chloride) additions to theMEG relative inhibited fluids. Key Words: wet sub sea pipeline, CO2 corrosion, salty ethylene glycol, corrosion control, hydrate control
PRICE BREAKS - The more you buy, the more you save
Quantity
1+
5+
Price
$20.00
$20.00
Product tags
Also Purchased
Picture for 03328 CORROSION CONTROL BY pH STABILISER
Available for download

03328 CORROSION CONTROL BY pH STABILISER, MATERIALS AND CORROSION MONITORING IN A 160 KM MULTIPHASE OFFSHORE PIPELINE

Product Number: 51300-03328-SG
ISBN: 03328 2003 CP
Author: Odd Hagerup, Stein Olsen
$20.00
Picture for 08626 Corrosion Inhibitor Qualification Testing for Subsea Wet Gas Pipelines
Available for download

08626 Corrosion Inhibitor Qualification Testing for Subsea Wet Gas Pipelines

Product Number: 51300-08626-SG
ISBN: 08626 2008 CP
Author: J. Pacheco, J. Regina, P. Abrams, S. Hickman, L. Talley, and T. Martin
Publication Date: 2008
$20.00
Picture for 03320 EFFECTS OF TEMPERATURE ON EROSION-
Available for download

03320 EFFECTS OF TEMPERATURE ON EROSION-CORROSION OF 13CR

Product Number: 51300-03320-SG
ISBN: 03320 2003 CP
Author: Jianfeng Chen, John R. Shadley, Hernan Rincon, Edmund F. Rybicki
$20.00
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