Menu
Search
Filters
Close
Menu

96612 EFFECT OF OXYGEN ON THE INTERNAL CORROSION OF NATURAL GAS PIPELINES

Picture for 96612 EFFECT OF OXYGEN ON THE INTERNAL
Available for download
Product Number: 51300-96612-SG
ISBN: 96612 1996 CP
Author: C.L. Durr, J.A. Beavers
Industry: Oil and Gas Production
$0.00
$20.00
$20.00
Internal corrosion is a problem in wet natural gas gathering lines. Literature on the subject suggests that dissolved oxygen (O2) is one of the more corrosive contaminants in natural gas. Immersion tests, funded by a major gas transmission company, were performed on Cl018 (UNS G10180) specimens to assess the influence of O2 concentration on the internal corrosion of the wet gathering system in their storage field. Twenty-eight day tests were performed in a flow-through (gas phase only) autoclave at 70°F (21°C) and 1200 psi (8274 kPa) with simulated natural gas mixtures containing 10, 100, 500 and 1000 ppm ( by volume) O2. Specimens were exposed to the vapor, vapor/liquid (V/L) interface, and liquid phases of pure water and saltwater in these tests. The highest corrosion rate, based on groove depth, was measured for the V/L specimens in pure water with 1000 ppm O2. Corrosion rates, based on weight loss, generally maximized at an O2 concentration of 100 ppm. Keywords: Corrosion, Natural Gas, Carbon Steel, Pipeline, Oxygen, Internal Corrosion, C1018
Internal corrosion is a problem in wet natural gas gathering lines. Literature on the subject suggests that dissolved oxygen (O2) is one of the more corrosive contaminants in natural gas. Immersion tests, funded by a major gas transmission company, were performed on Cl018 (UNS G10180) specimens to assess the influence of O2 concentration on the internal corrosion of the wet gathering system in their storage field. Twenty-eight day tests were performed in a flow-through (gas phase only) autoclave at 70°F (21°C) and 1200 psi (8274 kPa) with simulated natural gas mixtures containing 10, 100, 500 and 1000 ppm ( by volume) O2. Specimens were exposed to the vapor, vapor/liquid (V/L) interface, and liquid phases of pure water and saltwater in these tests. The highest corrosion rate, based on groove depth, was measured for the V/L specimens in pure water with 1000 ppm O2. Corrosion rates, based on weight loss, generally maximized at an O2 concentration of 100 ppm. Keywords: Corrosion, Natural Gas, Carbon Steel, Pipeline, Oxygen, Internal Corrosion, C1018
PRICE BREAKS - The more you buy, the more you save
Quantity
1+
5+
Price
$20.00
$20.00
Product tags
Also Purchased
Picture for Impact of Oxygen Ingress in CO2 Corrosion of Mild Steel
Available for download

51314-4299-Impact of Oxygen Ingress in CO2 Corrosion of Mild Steel

Product Number: 51314-4299-SG
ISBN: 4299 2014 CP
Author: Nor Roslina Rosli
Publication Date: 2014
$0.00
Picture for 08271 Effects of Oxygen, Temperature and Salinity on Carbon Steel Corrosion in Aqueous Solutions; Mo
Available for download

08271 Effects of Oxygen, Temperature and Salinity on Carbon Steel Corrosion in Aqueous Solutions; Model Predictions versus Laboratory Results

Product Number: 51300-08271-SG
ISBN: 08271 2008 CP
Author: Steven Grise and Brian Saldanha
Publication Date: 2008
$20.00

Corrosion of carbon steel materials in brine solutions.  Model results will be compared with literature data and lab experiments. Conditions will be limited to near neutral pH (5-9), temperature  from 22oC to 55oC, and O2 atmospheres up to 101.325 kPa.
Picture for 01054 EFFECT OF OXYGEN CONTAMINATION ON THE
Available for download

01054 EFFECT OF OXYGEN CONTAMINATION ON THE INHIBITION OF CO2 CORROSION

Product Number: 51300-01054-SG
ISBN: 01054 2001 CP
Author: Egil Gulbrandsen, Jon Kvarekval and Harald Miland
$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